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Title Development of monolithic columns for separation of inorganic anions and cations in capillary liquid chromatography( 本文 (Fulltext) ) Author(s) ASTER, RAHAYU Report No.(Doctoral Degree) 博士(工学) 甲第471号 Issue Date 2015-03-25 Type 博士論文 Version ETD URL http://hdl.handle.net/20.500.12099/51029 ※この資料の著作権は、各資料の著者・学協会・出版社等に帰属します。

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Page 1: Development of monolithic columns for separation …repository.lib.gifu-u.ac.jp/.../51029/3/ek0471.pdfsupercritical fluid chromatography (SFC) as shown in Table 1-1. Chapter 1 4 Table

TitleDevelopment of monolithic columns for separation of inorganicanions and cations in capillary liquid chromatography( 本文(Fulltext) )

Author(s) ASTER, RAHAYU

Report No.(DoctoralDegree) 博士(工学) 甲第471号

Issue Date 2015-03-25

Type 博士論文

Version ETD

URL http://hdl.handle.net/20.500.12099/51029

※この資料の著作権は、各資料の著者・学協会・出版社等に帰属します。

Page 2: Development of monolithic columns for separation …repository.lib.gifu-u.ac.jp/.../51029/3/ek0471.pdfsupercritical fluid chromatography (SFC) as shown in Table 1-1. Chapter 1 4 Table

Development of monolithic columns for separation of

inorganic anions and cations in capillary liquid

chromatography

(キャピラリー液体クロマトグラフィーにおける無機陰イオ

ンおよび陽イオンの分離のためのモノリスカラムの開発)

2015

ASTER RAHAYU

Page 3: Development of monolithic columns for separation …repository.lib.gifu-u.ac.jp/.../51029/3/ek0471.pdfsupercritical fluid chromatography (SFC) as shown in Table 1-1. Chapter 1 4 Table

Development of monolithic columns for separation of

inorganic anions and cations in capillary liquid

chromatography

(キャピラリー液体クロマトグラフィーにおける無機陰イオ

ンおよび陽イオンの分離のためのモノリスカラムの開発)

ASTER RAHAYU

Material Engineering Division

Graduate School of Engineering

Gifu University

JAPAN

2015

Page 4: Development of monolithic columns for separation …repository.lib.gifu-u.ac.jp/.../51029/3/ek0471.pdfsupercritical fluid chromatography (SFC) as shown in Table 1-1. Chapter 1 4 Table

Development of monolithic columns for separation of

inorganic anions and cations in capillary liquid

chromatography

A dissertation submitted to the Gifu University in partial fulfillment of

the requirements for the degree of Doctoral of Philosophy in Material

Engineering

By

ASTER RAHAYU

2015

Page 5: Development of monolithic columns for separation …repository.lib.gifu-u.ac.jp/.../51029/3/ek0471.pdfsupercritical fluid chromatography (SFC) as shown in Table 1-1. Chapter 1 4 Table

Contents

i

Contents

Contents i

Preface v

Chapter 1

Introduction 1

1.1. History of chromatography 1

1.2. Principle and classification of chromatography 3

1.3. Monolithic stationary phase in liquid chromatography 5

1.3.1 Organic polymer-based monolithic 5

1.3.2 Silica-based monolithic columns 6

1.3.3 Organic-inorganic hybrid monolithic columns 7

1.4. Ion chromatography 7

1.5. Objective of the present research 8

1.6. References 10

Chapter 2

Polymer monolithic methacrylate base modified with

tosylated-polyethylene glycol monomethyl ether as a stationary

phase for capillary liquid chromatography 12

2.1 Introduction 12

2.2 Experimental 14

2.2.1 Apparatus 14

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Contents

ii

2.2.2 Reagents and materials 14

2.2.3 Preparation of monolithic column 15

2.2.4 Modification of glycidyl methacrylate 16

2.3 Result and discussions 17

2.1.1 Preparation of PEG-monolith 17

2.1.2 Effect of modification condition 20

2.1.3 Optimization of eluent 24

2.1.4 Mechanical stability 28

2.1.5 Application to real sample 29

2.2 Conclusions 31

2.3 References 32

Chapter 3

Preparation of hybrid monolithic stationary phase with

allylsulfonate for the rapid and simultaneous separation of

cations in capillary ion chromatography 34

3.1 Introduction 34

3.2 Experimental 36

3.2.1 Apparatus 36

3.2.2 Reagents and materials 37

3.2.3 Preparation of AS-hybrid monolith 37

3.3 Result and discussions 38

3.3.1 Preparation of AS-hybrid monolithic column 38

3.3.2 Separation of common inorganic cations on ion-exchange mode 41

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Contents

iii

3.3.3 Comparison of AS-hybrid and particle-packed capillary 43

3.3.4 Characterization and mechanical stability of AS-hybrid monolithic

column 44

3.3.5 Reproducibility of AS-hybrid monolithic column 48

3.3.6 Application to real samples 49

3.4 Conclusions 51

3.5 References 52

Chapter 4

“One-pot” approach for fabrication of 3-sulfopropyl

methacrylate-co-ethylene dimethacrylate monolithic column for

capillary liquid chromatography 54

4.1. Introduction 54

4.2. Experimental 56

4.2.1 Apparatus 56

4.2.2 Reagent and materials 56

4.2.3 Preparation of SPMP-co-EDMA monolithic column 57

4.3. Result and discussion 58

4.3.1. Preparation of SPMP-co-EDMA 58

4.3.2. Separation of common inorganic cations in ion-exchange mode 61

4.3.3. Separations at high flow rate 64

4.4. Conclusions 66

4.5. References 66

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Contents

iv

Chapter 5

Conclusions and future perspective 68

5.1. Conclusions 68

5.2. Future Perspective 70

5.3. References 71

List of figures 72

List of tables 75

List of publications 76

List of presentations 77

Curriculum vitae 79

Acknowledgements 80

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Preface

v

Preface

Chromatography is the true phenomena that allow to broaden the scope of

sorption, which was discovered in 1903 by the Russian scientist Mikhail Semenovich

Tswett. Later day this phenomenon has influenced the development of analytical

chemistry especially for the rapid and powerful separation technique. Chromatography

has now served as a basis for the development of the most effective instrumental

method of investigation and analysis.

For more than 50 years, liquid-solid chromatography found by Tswett has

developed into gas chromatography (GC), thin layer chromatography (TLC) and liquid

chromatography (LC). Afterwards, in 1969 Kirkland introduced principles and tools of

high performance liquid chromatography (HPLC). HPLC is a popular method of

analysis because it is easy to learn, to use and is not limited by the volatility or stability

of the sample compound. Lately, many applications have been developed in LC

including separation, identification, purification, and quantification of various

compounds.

In addition to the mobile phase, stationary phase is one of the main components

in LC. Stationary phases may be divided from the physical property in particulate

packing material and monolithic material. The term silica-based packing material

usually means particulate material that usually consists of a specific stationary phase

material. Then it is packed and contacted with the mobile phase in the column. Recently,

a continues material that consist of both through-pore and meso-pore has been

successfully fabricated, i.e. monolithic material and it has excellently permeability

compared to the conventional material. Nowadays, the analysis method that considers

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Preface

vi

the environmental aspect became the most famous choice. The users of LC still prefers

to choose the method with the higher column efficiency, rapid analysis, and excellent

selectivity.

In this study, the development of monolithic column stationary phases as one

of the alternative to achieve the satisfaction in analysis, simple preparation, rapid and

great separation of inorganic cations and anions will be focused. Polymeric monolith

and silica organic-inorganic hybrid monolith which were fabricated in a simple way and

applied to rapid analysis of the inorganic compounds in the environment will also be

discussed.

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Chapter 1

1

Chapter 1

Introduction

1.1. History of chromatography

Chromatography is a method for separation of complex mixture discovered at

the very beginning of the twentieth century by Russian–Italian botanist Michael

Semenovich Tswett (1872-1919). On March 21st 1903 at the regular meeting of the

biology section of the Warsaw Society of Natural Sciences, he gave a detailed

description about the newly discovered phenomena of adsorption-based separation of

complex mixtures, which he later called “chromatography” as a transliteration from

Greek “color writing” which is taken from his paper “A new category of adsorption

phenomena and its application to biochemical analysis” [1]. He remarked: “Especially

instructive is the observation of adsorption phenomena during filtrations through

powder. First a colorless then yellow (carotene) liquid flows out of the lower end of the

funnel, and in the upper layer of an inulin column there is formed a green ring, below

which a yellow border appears. During the subsequent flow of pure ligroin through the

inulin column, both rings, green and yellow, considerably broaden and spread

downwards…

…On the basic of the foregoing, there appears the possibility of developing a

new method of physical separation of different substances dissolved in organic liquids.

The method is based on the ability of the solutes to form physical adsorption

compounds with different mineral and organic solids” [2]. In the first chromatographic

work, for the first time, it was used for developing variant of chromatography in

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Chapter 1

2

addition to the frontal version however only missing the term “chromatography”, as the

aspect that naturally does not prevent from considering it to be the first work on

chromatography.

Three years after the first chromatographic work, in the 1906, Tswett

introduced the term “chromatography”: “If a petroleum ether solution of chlorophyll

is filtered through a column of adsorbent (for this purpose I use mainly calcium

carbonate, tightly packed into narrow glass tubes) the pigments, according to their

position in the adsorption sequence, are deposited in separate colored zones along the

column from the top to down, due to the fact that the pigments with stronger adsorption

displace those which are retained more weakly. This separation becomes practically

perfect if, after the extract of pigments has passed through the column of adsorbent, the

latter is washed with pure solvent” [3]. However only a small number of various

applications of the method were being reported for the next 25 years because at the time

of the discovery, the chromatographic method was not appreciated among the scientist

as well as when L. S. Palmer in the United States and C. Dhere in Europe independently

published the description of a similar separation processes after almost 10 years. In

1931, Lederer, Kuhn and Winsterstein developed the chromatographic methods that are

still being improved into advanced techniques, which can be applied in various

applications [4-5]. In 1941, A. J. P. Martin and R. L. M. Synge at Cambridge University,

UK, discovered partition chromatography for which they were awarded the Noble Prize

in 1952.

In the present day, chromatography becomes an extremely versatile technique

in various separation techniques. It can separate gases and volatile substances by gas

chromatography (GC), in volatile chemicals and materials of extremely high molecular

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Chapter 1

3

weight (including biopolymers) by liquid chromatography (LC) and if necessary very

inexpensively by thin layer chromatography (TLC). All three techniques, GC, LC and

TLC have common features that classify them as chromatography systems.

Chromatography has therefore been defined as follows,

“Chromatography is a separation process that is achieved by distributing the

components of a mixture between two phases, a stationary phase and a mobile phase.

Those components held preferentially in the stationary phase are retained longer in the

system than those that are distributed selectively in the mobile phase. As a consequence,

solutes are eluted from the system as local concentrations in the mobile phase in the

order of their increasing distribution coefficients with respect to the stationary phase;

ipso facto a separation is achieved” [6].

1.2. Principle and classification of chromatography

Originally, chromatography is one of separation process based on their

different distribution between two non-miscible phases. One is the stationary phase that

remains in a fixed position, and the other is mobile phase that moves through the system.

Generally, chromatography can be classified by various ways; on the basis of interaction

of solute to the stationary phase, on the basis of shape of separation bed, and techniques

by physical state of mobile phase. For the classification based on interaction, there will

be divided into four types of chromatography; adsorption, partition, ion-exchange and

size-exclusion. Furthermore, on the basis of shape of separation bed will be two types;

tubular and planar chromatography. Afterwards, the classification based on techniques

by physical state of mobile phase, there will be divided into three types; GC, LC and

supercritical fluid chromatography (SFC) as shown in Table 1-1.

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Chapter 1

4

Table 1-1. Classification of chromatography

Classification Name of chromatography Abbreviation

Interaction of solute to the stationary phase

1. Adsorption Adsorption chromatography -

2. Partition Partition chromatography -

3. Ion-exchange Ion-exchange chromatography IC

4. Size-exclusion Size-exclusion chromatography SEC

Permeation Gel permeation chromatography GPC

Filtration Gel filtration chromatography GFC

Shape of separation bed

1. Tubular Column chromatography -

2. Planar Thin-layer chromatography TLC

Paper chromatography PC

Techniques by physical state of mobile phase

Mobile phase Stationary phase

1. Gas Solid

Gas chromatography GC Liquid

2. Liquid Solid

Liquid chromatography LC Liquid

3. Supercritical fluid Supercritical fluid chromatography SFC

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Chapter 1

5

1.3. Monolithic stationary phase in liquid chromatography

In late 1980s monolithic columns in capillary liquid chromatography were

introduced by Hjertén with development of the continuous bed [7]. Afterwards, it

becomes highly popular and has been gaining rising attention and used in various

applications and many developments in term of both their manufacture and uses.

Monolith columns have pore structure with bimodal pore size distribution, mesopores at

the surface of the skeleton structure and also through pores (macropores) between the

skeleton. The existence of mesopores and through-pores can give the great effect on

separation efficiency and generate low pressure drop as well as enhance mass transfer

kinetics that can be used in higher flow rates in rapid separations on the long length of

columns [8]. Based on the basic chemical nature of monoliths, monolithic columns can

be divided into organic polymer-based and silica-based monolithic columns [9-10].

1.3.1 Organic polymer-based monolithic

In early 1990s, organic polymeric-based monolithic columns were introduced

by Svec and Fréchet with the rigid polymer rod [11]. Generally, polymer monolithic

column is a continuous porous polymer which is prepared from a mixture of initiator,

monomer solution including monomers and crosslinking monomer and porogens that

are polymerized “in-situ” in a column or capillary. The preparations of polymer

monolithic columns usually use a radical polymerization that include styrene-,

methacrylate-, and acrylamide based materials. Since monomer and crosslinker are the

primary part of the formed material, the characteristics of the monolith depend on the

composition of the polymerization mixture. The polymer-based monolithic columns

have some distinct advantages including high stability in a wide pH range, facileness in

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Chapter 1

6

preparation process, easiness for modification and good permeability [12-13].

Unlimited choice of matrix and surface chemistries can lead to variation of

polymer mixture using a wide variety of monomers for any purpose [14-15]. Most of

the polymerizations are radical polymerization by thermally [16-17] or UV

radiation-activation [18]. In addition, the use of gamma radiation has also been

established as has microwave irradiation most recently [19]. The polymer monolith can

be divided in three types of organic polymer-based monolithic columns that are most

frequent produced: acrylamide-based, methacrylate-based, and styrene-based polymers

[20].

1.3.2 Silica-based monolithic columns

Silica-based monolithic columns were excellently developed by Nakanishi and

Tanaka based on hydrolysis of tetramethoxysilane in acidic solution, suitable porogen

i.e. polyacrylic acid, polyethylene oxide, and followed by the maceration of the gel in a

basic solution leading to the formation of mesopores [21-22]. Generally, silica-based

monolithic columns are prepared using sol-gel technology to form continuous sol-gel

network throughout the column formed by the gelation of a sol solution within the

capillary tube. This process allowed to form small-sized skeletons and large

through-pores with the through-pore size and skeleton size ratios much greater than

0.25–0.4 found for conventional column packed with particles [23]. Silica based

monolithic columns could demonstrate great mechanical stability and strength, solvent

resistance and then high efficiency.

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Chapter 1

7

1.3.3 Organic-inorganic hybrid monolithic columns

In order to combine the distinct advantage from both of organic polymer-based

and silica-based monolithic columns, the organic-inorganic hybrid monolithic columns

have been attracting great attention. The organic functional moieties can be incorporated

into the organic silica matrixes via the sol-gel process to give various properties, such as

good mechanical stability and solvent resistance. In the preparation of organic-inorganic

hybrid, the organic moieties are covalently incorporating into the monolithic matrix via

the co-condensation of organofunctional tri-alkoxysilane [(RO)3Si-R´: where R´

represents organofunctional group] and conventional tetra-alkoxysilane

(tetramethoxysilane or tetraethoxysilane) by sol-gel process in order to avoid the time

consuming during post modifications process of the silica monoliths [24]. Recently, a

lot of effort and focus from many researchers are used on the organic-inorganic hybrid

monolithic columns in many purposes and target research.

1.4. Ion chromatography

Ion chromatography (IC) is the separation and quantitative analysis of ionic

solutes, such as inorganic anions, cations, transition metals and low molecular-weight

organic acids and bases using the ion exchange method of liquid chromatography. The

separation process of ionic solutes was based on ionic interaction of analyte molecules

that are retained on the column. The stationary phase surface displays ionic functional

groups that interact with analyte ions of opposite charge. The types of ion

chromatography are distinguished into cation-exchange chromatography and

anion-exchange chromatography.

The essential property in ion exchange chromatography is a charged group. It

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Chapter 1

8

was determined based on the type and strength or the ion exchanger including their total

number and availability determines the capacity. It can be divided into four categories of

groups that shown in Table 1-2 [25].

Table 1-2. Functional groups used on ion chromatography

Functional Groups Examples Types

-O-CH2-CHOH-CH2-O-CH2-CHOH-CH2-N+(CH3)3

Quaternary

Amine

Strongly

Anion-Exchanger

-O-CH2-CH2-N+H(CH2CH3)2 Tertiary Amine

Weakly

Anion-Exchanger

-O-CH2-CHOH-CH2-O-CH2-CH2-CH2-SO3- Sulfopropyl

Strongly

Cation-Exchanger

-O-CH2-COO- Carboxymethyl

Weakly

Cation-Exchanger

1.5. Objective of the present research

The stationary phase is an important part in the liquid chromatography system.

Many types of the stationary phases were developed in order to achieve the best

separation profile for various purposes. Monolithic column is one of the separation

media that has attracted a great attention for widely application in capillary liquid

chromatography due to their advantages since it was introduced in late of 1980s. The

format of monolith can be compared to a single large “particle” that does not contain

inter-particular voids. The main objective of present research is to develop a monolithic

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Chapter 1

9

column for capillary liquid chromatography. Polymer monolith-based and

organic-inorganic-silica-hybrid monolithic columns were focused for fabricating as

stationary phases in capillary liquid chromatography and determination of inorganic

anions and cations in real samples.

Chapter 2 describes the preparation of polymer monolithic columns by

introducing PEG into the monolith using pyridine to improve the column efficiency in

separation of anions since for the PEG stationary phase bromide and nitrite coelute. The

mechanism for interaction of anions in PEG-monolithic column was based on cations

trapped among PEG chain and the positively charged pyridine that work as the anion

exchange sites in the PEG-monolith. The present system would be applied to the

determination of these anions in seawater as well as public drinking water samples.

Chapter 3 describes a simple preparation of the strong cation-exchange hybrid

monolithic column with single-step-thermal-treatment “one-pot” approach. Strong

cation-exchange sites were introduced from an organic monomer. In order to check

performance of this method, nine common inorganic cations were separated

simultaneously and determined by using eluent of CuSO4 via indirect UV detection. The

present method was also applied for direct simultaneous determination of cations in

groundwater as well as effluent of domestic wastewater treatment system samples in

capillary ion chromatography.

Chapter 4 describes a simple preparation “one-pot” approach of capillary

polymer monolithic column with sulfonate groups as strong cation-exchange site.

3-sulfopropyl methacrylate potassium salt was introduced as the monomer with

sulfonate functional groups. Performance of the present method was applied to

simultaneous determination of common cations by using eluent of CuSO4 via indirect

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Chapter 1

10

UV detection.

Chapter 5 describes whole conclusions of the achievement completed in this

research concerned in development of monolithic columns as promised stationary

phases in capillary liquid chromatography.

1.6. References

[1] K. I. Sakodynskii, “Michael Tswett Life and Work”, Carlo Erba Strumentazione,

Milan, Italy.

[2] R. Kuhn, A. Winterstein, and E. Lederer, Phyisiol. Chem. 197, (1931), 141-160.

[3] A. J. P. Martin and R. L. M. Synge, J. Biochem, 35, (1941), 91-121.

[4] A. Braithwaite and F. J. Smith, “Chromatographic Methods”, 5th

ed., 1996,

Kluwer Academic Publisher, Dordrecht.

[5] D. Harvey, “Modern Analytical Chemistry”, 2000, Mc Graw Hill, New York.

[6] R. P. W. Scott, “Principles and Practice of Chromatography”, 2003, Chrom-Ed

Book Series, 01-02, www.library4science.com.

[7] S. Hjertén, J. L. Liao, and R. Zhang, J. Chromatogr., 473, (1989), 273–275.

[8] A. Sabarudin, J. Huang, S. Shu, S. Sakagawa, and T. Umemura, Anal. Chim.

Acta, 736, (2012), 108- 114.

[9] G. Guiochon, J. Chromatogr. A, 1168, (2007), 101–168.

[10] I. Gusev, X. Huang, and C. Horvath, J. Chromatogr. A, 855, (1999), 273-290.

[11] F. Svec and J. M. J. Fréchet, Anal. Chem., 64, (1992), 820–822.

[12] T. Nakaza, A. Kobayashi, T. Hirano, S. Kitagawa, and H. Ohtani, Anal. Sci., 28,

(2012), 917-920.

[13] Y. Zhong, W. Zhou, P. Zhang, and Y. Zhu, Talanta, 82, (2010), 1439- 1447.

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Chapter 1

11

[14] D. Moravcova, P. Jandera, J. Urban, and J. Planeta, J. Sep. Sci., 27, (2004),

789-800.

[15] Y. Li, B. Gu, H. D. Tolley, and M. L. Lee, J. Chromatogr. A, 1216, (2009),

5525-5532.

[16] E.G. Vlakh and T.B. Tennikova, J. Chromatogr A, 1216, (2009), 2637–2650.

[17] F. Svec and J. M. J. Fréchet, Macromolecules, 28, (1995), 7580–7582.

[18] R. Bakry, C. W. Huck, and G. K. Bonn, J. Chromatogr. Sci., 47, (2009), 418-431.

[19] Y. P. Zhang, X. W. Ye, M. K. Tian, L. B. Qu, S. H. Choi, A. I. Gopalan, and K. P.

Lee, J. Chromatogr. A 1188, (2008), 43–49.

[20] D. Moravcov, P. Jandera, J. Urban, and J. Planeta, J. Sep. Sci.,26, (2003), 1005–

1016.

[21] K. Nakanishi, H. Minakuchi, N. Soga, and N. Tanaka, J. Sol-Gel Sci. Technol., 8,

(1997), 547-552.

[22] H. Minakuchi, K. Nakanishi, N. Soga, N. Ishizuka, and N. Tanaka, J.

Chromatogr. A, 762, (1997), 135-146.

[23] K.K. Unger, “Porous Silica. Its Properties and Use as Support in Column Liquid

Chromatography”, Chapter 5, Volume 16, Elsevier, Amsterdam, 1979,

[24] J. D. Hayes and A. Malik, Anal. Chem, 72, (2000), 4090-4099.

[25] C. Eith, M. Kolb, A. Seubert, and K. H. Viehweger, “Practical Ion

Chromatography, An Introduction”, 2nd

ed, 2007, Metrohm Ltd, Herisau.

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Chapter 2

12

Chapter 2

Polymer monolithic methacrylate base modified

with tosylated-polyethylene glycol monomethyl

ether as a stationary phase for capillary liquid

chromatography

2.1 Introduction

Monolithic beds have recently been developed for liquid chromatography (LC) [1].

Their advantages include low column backpressure, simple preparation, requirement of

very small amount of stationary phase for a single column, wide application, no use of

retaining frits to hold the stationary phase and ease of modification. The porous

monoliths consist mesopores and through-pores, which makes them highly porous

compared to conventional particle-packed columns. Consequently, monolithic column

can conduct the eluent with high flow rate. Basically, monoliths can be synthesized

from inorganic material such as silica [2-5] or organic materials such as polymer [6,7]

that contain a cross-linking agent, monomers and some porogen in a column tube by

in-situ polymerization.

Polymer monolithic stationary phases for ion exchange chromatography (IEC)

were fabricated and the separation efficiency was investigated in this study. The

fabrication of the polymer monolith usually involves a reactive moiety of the monolith;

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Chapter 2

13

in this case epoxy group was used, which is then directly modified with functional

groups that contain ion-exchange property, such as amino groups [6].

Polyethylene glycol (PEG) is a hydrophilic macromolecule, which only shows

mild hydrophilic interaction with proteins at higher salt concentration, and hardly

affected the bioactivity of protein under adequate protein purification condition [4].

PEG-functionalized polymer monolith provides the stationary phase for the separation

of large and small molecules [6, 8]. PEG has been used for stationary phase in reversed

phase liquid chromatography. Beside hydrophobic interaction, PEG could also be used

for the separation of anions even though PEG does not possess any ion exchange site.

Several packing materials which were physically coated and chemically bonded by PEG

for IEC have been developed while materials in the form of monolith have been very

limited. Rong et al. developed and examined the PEG stationary phase by physically

coating for ion chromatography. Lim et al. and Takeuchi et al. have successfully

examined the PEG bonded stationary phase for separation of inorganic anions [9-12].

Linda et al. has successfully reacted the PEG with primary amino groups of an

aminopropylsilica packing column for separation of inorganic anions [13]. The PEG

moiety could form a helix-like conformation in the organic-aqueous media. The

separation of anions based on trapping the eluent cations fixed on the oxygen atoms of

the PEG chain by ion-dipole interaction that work as the anion-exchange site for

separation of anions [14]. Furthermore, the trapping of the cations on the PEG is similar

with trapping on the crown ethers since crown ethers are cyclic PEG, but the former is

more flexible [9]. The PEG monoliths have been made and synthesized from

PEG-functionalized monomers or cross-linkers for size-exclusion, cation-exchange, and

anion-exchange chromatography. Monolithic columns have higher permeability than

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Chapter 2

14

particle packed columns, which lead to rapid separation of analytes. However, PEG

monoliths for the separation of anions have been little reported in the literature. The

focus of this study is a polymeric monolith, which requires shorter fabrication time and

more robust over a wide range of pH compared to silica-based monoliths. PEG was

introduced into the monolith using pyridine will be prepared to improve the column

efficiency in the separation of anions since for the PEG stationary phase bromide and

nitrite coelute. The PEG monolith was then used as the stationary phase for the rapid

and direct determination of inorganic anions in seawater sample as well as public

drinking water sample in capillary ion chromatography.

2.2 Experimental

2.2.1 Apparatus

The chromatographic separation was carried out using a capillary LC system

constructed by an L.TEX-8301 Micro Feeder (L.TEX corporation, Tokyo, Japan)

equipped with an MS-GAN 050 gas-tight syringe (0.5 mL, Ito, Fuji, Japan) as a pump, a

Model 7520 (Rheodyne, Cotati, CA, USA) injector with an injection volume of 0.2 µL,

a 100 mm x 0.32 mm i.d. of microcolumn and a UV-1575 intelligent UV/vis detector,

(JASCO, Tokyo, Japan) that was operated at 210 nm. The data was acquired using a

Chromatopac C-R7A data processor (Shimadzu, Kyoto, Japan). The inlet pressure was

monitored with an L.TEX-8150 Pressure Sensor (L.TEX).

2.2.2 Reagents and materials

Glycidyl methacrylate (GMA) (97%) and ethylene dimethacrylate (EDMA)

(97%) were obtained from Wako while n-decyl alcohol, 3-(trimethoxysilyl)propyl

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Chapter 2

15

methacrylate (γ-MAPS, 98%) and 2,2’-azobisisobutyronitrile (AIBN) were obtained

from TCI (Tokyo, Japan). 1,4-Butanediol, pyridine and 1,4-dioxane were obtained from

Nacalai Tesque (Kyoto, Japan). Polyethylene glycol monomethyl ether

p-toluenesulfonate (Tosylated-PEG, M.W.1000) was obtained from Aldrich (Rockford,

IL, USA). Potassium chloride was of extra pure reagent grade (Nacalai Tesque).

Purified water was produced in the laboratory by using a GS-590 water distillation

system (Advantec, Tokyo, Japan). All the solutions used in this study were prepared

from extra pure reagents obtained from Nacalai Tesque.

2.2.3 Preparation of monolithic column

The fused silica capillary tube (0.320 mm i.d. x 0.450 mm o.d.) was purchased

from GL Sciences (Tokyo, Japan). Fused silica capillary tube was washed using 1 M

NaOH solution, deionized water and 1 M HCl in sequence. 30 % (v/v) of γ-MAPS in

acetone was used for providing methacrylate groups on the inner wall surface of the

capillary tube; the tube was sealed at both ends and thermally treated in a water bath at

60˚C for 24 h. Thereafter, the capillary tube was washed with acetone and dried using

nitrogen gas for 30 min. As shown in Table 2-1, mixture solutions of monomer,

cross-linker and porogen were prepared at various compositions. Then, 0.2 mL of the

solution was completely mixed with 2 mg of AIBN, i.e. the polymerization initiator. The

mixture solution was then subjected to ultrasonic vibration for 5 min before it was

injected into the pretreated capillary tube. Thermal polymerization was carried out in

the water bath at 60˚C for 24 h. The capillary tube was rinsed with methanol thoroughly

after polymerization to remove unreacted reagents and porogenic solvents. The

morphology of the monolith was examined by using scanning electron microscopy

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16

(SEM; S-4800, Hitachi, Tokyo, Japan).

2.2.4 Modification of glycidyl methacrylate

Table 2-1. Various polymerization conditions.

*Not applicable a Glycidyl methacrylate (GMA) was always used as a monomer.

b Ethylene dimethacrylate (EDMA) was used as a cross-linker.

c Three kind of alcohols i.e. ethanol, 1,4-butanediol and decanol were used as porogen.

d The volume ratio of monomer + cross-linker to porogen.

e 1,4-Dioxane and pyridine were used as the solvents of tosylated-PEG during the modification.

Subsequently, polyethylene glycol (PEG) group was attached into the glycidyl

methacrylate monolith using polyethylene glycol monomethyl ether tosylate

(tosylated-PEG). Tosylated-PEG was dissolved in 0.5 mL of 1,4-dioxane and pyridine

(50/50,v/v). The solution was passed through to the glycidyl methacrylate monolith and

the reaction was carried out by heating in the oven at 75 ˚C for 4-8 h, and washing it

with methanol at a flow rate of 4 µL/min for 2 h.

Column Monomera

Crosslinkerb

Porogenc Mixture Modification N Max

% (v/v) % (v/v) % (v/v) ratiod

conditione Plates/m

M1 7.5 2.5 90 10/90 75 ˚C, 6 h *

M2 15 5 80 20/80 75 ˚C, 6 h 3346

M3 22.5 7.5 70 30/70 75 ˚C, 6 h 5275

M4 30 10 60 40/60 75 ˚C, 6 h 1558

M5 17.5 2.5 80 20/80 75 ˚C, 6 h 4383

M6 12.5 7.5 80 20/80 75 ˚C, 6 h 3076

M7 10 10 80 20/80 75 ˚C, 6 h 1389

M8 15 5 80 20/80 75 ˚C, 4 h 2944

M9 15 5 80 20/80 75 ˚C, 5 h 3218

M10 15 5 80 20/80 75 ˚C, 7 h *

M11 15 5 80 20/80 75 ˚C, 8 h *

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Chapter 2

17

2.3 Result and discussions

2.1.1 Preparation of PEG-monolith

PEG monolith was prepared firstly from polymerization of GMA and EDMA

under normal temperature for polymerization condition (60 ˚C) and was modified using

tosylated-PEG dissolving into 1,4-dioxane and pyridine. The good composition of

monolith is a great importance in production site. Generally, the performance of the

monolith column was influenced by ratio of monomer to porogen. Hence, investigation

of the ratio of monomer to porogen is necessary for achieving the best methacrylate

base before continuing modification step. Firstly, the ratio of monomer to porogen was

mainly investigated by keeping the cross-linker content. The resolution between two

anions, i.e., IO3- and BrO3

- is shown in Table 2-2.

Table 2-2. Resolution of the analytes for various total monomer to porogen ratios.

a The volume ratio of monomer to porogen.

b The resolution between IO3

- and BrO3

-.

The monomer/porogen ratio is 20/80 has the best separation profile of anions

with resolution approximately 1.15-1.77. When the monomer content was decreased to

10/90, the resolution value could not be calculated because all the anions appeared at

the same retention time. Conversely, when the monomer content was increased up to

30/70 and 40/60, the separation of anions was deteriorated and some of the anion peaks

Mixture ratioa

Resolutionb

10/90 0

20/80 1.15-1.77

30/70 1.00-1.36

40/60 0.85-1.16

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18

were overlapped each other; it was evidenced by resolution values of 1.00-1.36 and

0.85-1.16, respectively. Less amount of porogen also can cause the tight or fully-packed

structure of the monolith in the capillary tube. The morphology of the monolith surface

was also observed by using SEM, as shown in Figure 2-1. Theoretically, by increasing

the ratio of porogen, the through-pores will also be increased; on the other hand, when

the ratio of the porogen is less, the surface of the monolith will become fully packed and

will thus increase the back pressure. From the four SEM photos, showing the

morphology of monoliths with the monomer/porogen ratio is 40/60, 30/70, 20/80 and

10/90, it is clearly shown that the monoliths were attached tightly to the inner-wall of

the silica capillary tubes, and the estimation ranges of the monolith skeleton are 1-1.5,

2-2.5, 3-4 and 3.5-4 µm, respectively. The reference monolith M2 was chosen as the

starting point to continue preparation of the PEG monolith.

Additionally, the availability of the monomer GMA in this polymerization, also

will take an important part because GMA has an epoxy functioning group. Since GMA

is used as the monomer to form the methacrylate base, more reactive epoxy groups will

be available for the reaction (during the modification) when the amount of GMA in the

mixture solution is increased. The increasing number of epoxy group from GMA in the

methacrylate base will also increase the amount of PEG attached into the methacrylate

base, and thus has affected the efficiency of the column. On the other hand, EDMA is a

highly reactive cross-linker containing ethylene bridge, which provides good

permeability. Starting from M2 prepared with 15% of GMA, the availability of epoxy

group was investigated.

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Chapter 2

19

Fig. 2-1. Scanning Electron Microscope images of PEG-monolithic column.

Monomer:porogen is 40/60 (A), 30/70 (B), 20/80 (C) and 10/90 (D).

Table 2-1 shows the efficiency of each column for various contents of GMA in

the PEG monolith. These proved that increasing GMA content from 10 % up to 17.5%

(v/v), the column efficiency also increases from 1468 to 4373, in terms of the theoretical

plates/m. Although the theoretical plates/m of each column was not very high compared

to the others, the PEG monolith can separate 5 anions completely in a short elution time

while maintaining a good resolution.

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Chapter 2

20

2.1.2 Effect of modification condition

Modification condition also has affected the performance of the elution profile

of each column. PEG moiety could form helix-like conformation by adjusting itself in

the organic aqueous media. As expected, the solvent which contains the amine

functional group could take part in attaching the PEG group into the methacrylate base

and the tosylated group from tosylated-PEG modifier would be a leaving group in the

modification reaction. The modification of methacrylate base was carried out by

attaching tosylated-PEG which was dissolved in 1,4-dioxane and pyridine. The scheme

of the expected reaction is shown in Figure 2-2.

O

O

O

Methacrylate based

+ H3C

SO

O O

OCH3n

N O

O

+

Tosylated-PEG was dissolved in 1.4 dioxanePyridine and

O

O

H3C

SOH

O O

+

Tosylated leaving groupPEG-monolith

O-PEG

N

Fig. 2-2. Schematic diagram of the expected reaction for the preparation of

PEG-monolithic column.

Methacrylate base already has the epoxy groups as reactive sites, firstly the

reactive nucleophiles that were introduced by pyridine worked to open the epoxy group

and another hydroxyl group from the opened epoxide was reactive for attaching the

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Chapter 2

21

PEG. Since the nucleophiles are required for attaching the PEG groups, pyridine was

chosen in this research. Pyridine has been used as a precursor in some reactions and

could be as the supplier of nucleophiles. On the other hand, since tertiary amine in

pyridine could work as the anion exchange site, separation profiles were compared

between PEG-monolith and monolith without PEG chain.

Fig. 2-3. Separation of inorganic anions on the stationary phase with and

without PEG groups. Operating conditions: Analytes, 1 mM of

each iodate (1), bromate (2), nitrite (3), bromide (4) and nitrate

(5); PEG-monolith M2 column (100 x 0.32 mm i.d.); 100 mM of

sodium chloride eluent; 4 µL/min flow rate; 210 nm wavelength

of UV detection and 0.2 µL injection volume.

The elution of five inorganic anions on the stationary phase with and without

PEG was displayed in Figure 2-3. When the monolith just modified with pyridine

without attaching any PEG groups, five inorganic anions could not be separated well

unlike when monolith was modified with PEG. Hence, attaching PEG groups onto the

0 10 20

0.004 Abs

Time (min)

1

2

3

4

5

1

2

3

4 5

Unmodified with PEG group

Modified with PEG group

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22

monolithic column could improve the separation performance of anions compared to

without any PEG groups on the column that has 1433 theoretical plates/m for nitrate.

Reaction time will take an important part in modification condition. It was found

that the reaction time of attaching the PEG into the methacrylate base affected the

profile of separation of anions. Decreasing the reaction time gives longer elution time of

each anion. When the reaction time increased from 4 to 6 h, the elution time of the

anions become shorter as displayed in Figure 2-4. Unfortunately, the reason of this fact

is not certain. The column efficiency increased from 2944 to 3346 theoretical plates/m

for nitrate at a flow rate of 4 µL/min. However, when the reaction was done for 7 and 8

h, the column efficiency could not be evaluated because the peaks of anions were totally

broaden, and the elution order of the anions were irregular compared to those obtained

at lower reaction times as displayed in Figure 2-5. This condition might be due to

optimum reaction conditions that are already achieved and longer modification will only

cause damage to some of the reagents used. The separation profiles obtained when

modification at lower times was very different than those modified for 7 or 8 h;

technical problem (misconduct) during the preparation and modification reaction also

likely to be one caused. Attaching the PEG into the methacrylate base at 75˚C for 6 h

showed the best separation profile.

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23

Fig. 2-4. Effect of modification condition for separation of inorganic

anions (4 to 6 h reaction time). Operating condition is in

figure 2-3.

Fig. 2-5. Effect of modification condition for separation of inorganic anions

(7 and 8 h reaction time). Operating condition is in figure 2-3.

0 10 20

4 h

5 h

6 h

0.004 Abs

Time / min

1

2

3

45

0 10 20

7 h

8 h

Time / min

0.001 Abs

1

2

3

4 5

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Chapter 2

24

2.1.3 Optimization of eluent

Some salt aqueous solutions such as LiCl, NaCl, KCl, RbCl, CsCl, NH4Cl,

MgCl2, SrCl2 and CaCl2 were used as the mobile phase. The retention time of 5

inorganic anions was affected by the eluent cations which were trapped among the PEG

chains and functioned as the anion-exchange sites in the PEG monolithic stationary

phase. The positively charged pyridine also works as the anion exchange site in the PEG

monolith for the separation of 5 anions. The existence of the positive charge on the

pyridine was found to have a positive effect on the separation of anions because the

elution order of these anions on the PEG stationary phase was found similar to those

observed in the conventional ion exchange chromatography except coeluting for

bromide and nitrite. In addition, the eluent cations also affect the retention behavior of

the anions because eluent cations were expected to be trapped onto the PEG chains by

ion-dipole interaction with the oxygen atom of the multiple PEG chains [14].

Unfortunately, the elution of bromide and nitrite were overlapped for PEG stationary

phase. Hence, existence of positive charge on pyridine could solve this problem.

Figure 2-6 shows the retention behavior of 5 anions using aqueous solution as

the eluent. Different eluent cations gave the different elution time of anions. The

retention of anions decreased when hydrated cation with smaller size was used as the

eluent. In this case eluent CsCl showed the shortest retention of anions, whereas some

peaks of the anions were overlapped.

Conversely, using the divalent cation i.e. MgCl2, the retention of anions was

decreased although the MgCl2 has a bigger size. This could probably be explained by

the fact that the retention of anions was not solely influenced by the size of ionic radii of

the trapped eluent cations [15]. Unlike crown ethers (i.e. cyclic PEG) stationary phases,

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Chapter 2

25

in which only cations with a specific size are trapped within the cavity of crown ethers,

the eluent cations investigated in this study were found to be trapped regardless of their

ionic radius. The ionic radii increases in the following order: Li+ (0.090 nm) < Na

+

(0.116 nm) < K+ (0.152 nm) < Rb

+ (0.166 nm) < Cs

+ (0.181 nm) for the monovalent

cations, and Mg2+

(0.086 nm) < Ca2+

(0.114 nm) < Sr2+

(0.132 nm) for the divalent

cations [15].

Fig. 2-6. Chromatograms of inorganic anions with various chloride eluents.

Operating conditions: Analytes, 1 mM each of iodate (1), bromate

(2), nitrite (3), bromide (4) and nitrate (5); PEG-monolith M2

column (100 x 0.32 mm i.d.); 100 mM aqueous solution of various

chloride eluent, as indicated; 4 µL/min flow rate; 210 nm

wavelength of UV detection and 0.2 µL injection volume.

0 10 20Time/min

LiCl

NaCl

KCl

CsCl

RbCl

NH4Cl

MgCl2

CaCl2

SrCl2

1

2

3

45 0.004 Abs

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26

By the right retention of anions should also follow this order, however,

irregular retention behaviors were observed. Nevertheless, NH4+ with ionic size slightly

bigger than K+ was found having exceptional retention for these anions. On the other

hand, MgCl2 showed the shorter retention time than monovalent cations even CsCl, as

shown in Figure 2-6. Therefore, we could conclude that the retention of anions was not

solely affected by the size (ionic radii) of the cations. Unfortunately, the reason for this

phenomenon is yet to be elucidated. In Figure 2-6, KCl shows the best resolution among

the others and thus it was used for the following experiments.

Fig. 2-7. Effect of potassium chloride concentration (log [KCl]) on retention

(log k) of inorganic anions. Operation conditions as in figure 2-3.

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Chapter 2

27

Moreover, the effect of concentration of salt was investigated. Figure 2-7 shows

the logarithm of retention factor (log k) of anions as logarithm function of the eluent

concentrations. From the figure it can be seen that the plot of each anion was almost

linear and the slopes were -0.52, -0.90, -0.78, -0.80 and -0.94, respectively.

Theoretically, in this case if ion exchange is involved in the retention of anions, the

slopes of each anion should be -1.0 because the analyte anions and the chloride anions

are also monovalent. Since the slope for each anion is nearly to -1.0, the coordination of

cations which were trapped in the PEG chain could work during separation of anions in

ion exchange mode. By increasing concentration of cations in the mobile phase, the

coordinated cation could increase but the anions retention time decreased. The relative

standard deviations (RSDs) of retention time, peak height and peak area of five anions

were calculated under the same operating condition. The results of this condition are

provided in Table 2-3. The relative standard deviations (RSDs, for n=7) of retention

time, peak height and peak area were less than 2.27% for all the analyte anions. In other

words, these values show the quite satisfactory repeatability of the PEG column.

Table 2-3. Relative standard deviation of retention time, peak area and peak

height. Operating condition as in Figure 2-3.

RSD (% n = 7)

Retention Peak area Peak height

IO3- 0.46 1.79 1.56

BrO3- 0.62 2.33 2.02

NO2- 0.73 1.28 0.96

Br- 0.65 2.19 2.27

NO3- 0.5 1.00 0.86

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Chapter 2

28

2.1.4 Mechanical stability

Monolithic column stationary phase should have an excellent mechanical

stability and permeability. The mechanical stability of the column can be obtained by

calculating the swelling propensity (SP) factor and also by plotting the pressure drop to

the flow rate. SP factor is a measure of the shrinkage and swelling of materials in

different solvents. To determine the SP value, deionized water and organic solvent were

compared at the same flow rate. SP factors were calculated based on the methods of

Nevejans and Verzele [16],

SP = 𝑝 (solvent) – 𝑝 (water)

𝑝 (water)

where p is the pressure relative to the viscosity, p = P/η. Generally, no swelling occurs

in the column if SP = 0 whereas more swelling occurs if the SP value is higher. On the

other hand, a negative value indicates shrinkage of the monolith [17]. In this study, the

SP value of column M2 was determined by using water as the eluent for 30 min and the

pressure drop was marked. Furthermore, eluent was changed to methanol and waiting

until the system was stabilized, and the pressure drop was marked again. The THF is

also operated in the same way as methanol for determination of SP. The SP value of

monolith M2 was found to be around 0.34, meanwhile for methanol and THF was 0.64,

respectively. These values give evidence that there is no significant swelling and

shrinkage of the PEG monolith rod observed. Hence these monoliths could work on

different polarities with the high flow rate compared to other polymer monolith

materials reported with SP values from 0.16~1.1 [1,16,18-19].

Figure 2-8 shows a pressure drop plotted against flow rates indicates an

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29

excellent linearity with around R2 0.995. Instead of water, methanol and THF were both

utilized with flow rate up to 10 µL/min, the pressure drop in the system was still less

than 1.9, 1.5 and 1.4 MPa, respectively. This result indicated that the PEG monolithic

column could be operated for a fast, efficient analysis at a higher flow rate and with less

pressure drop. Owing to a pressure drop plotted against flow rates the permeability

values calculated for water and methanol as mobile phase were 8.0×10-13

and 5.3×10-13

m2, respectively. These values are relatively higher than the range for polymer

methacrylate-based monoliths around 0.15~8.4×10-14

m2

[20].

Fig. 2-8. Back pressure of M2 as a function of flow rate of water, methanol

and THF.

2.1.5 Application to real sample

In order to know the ability of this method, the water samples: seawater of

Padang beach and the public drinking water were collected from Padang city, West

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Chapter 2

30

Sumatera-Indonesia, then used as application. The seawater and public drinking water

samples were applied in this method within a few days after collection. As prior

treatment, the samples were filtered through a 0.45 µm membrane filter for ion

chromatography sample. By using this method, bromide could be determined in the

seawater with concentration 44 ppm (Figure 2-9) and the nitrate was determined around

1.9 ppm in the public drinking water (Figure 2-10).

Fig. 2-9. Separation of anions contained in seawater sample. Operating

conditions as in Figure 2-3.

0 5 10 15 20 25

Time / min

0.004 Abs

Seawater

1

2

3

4

5

Standard

4

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31

Fig. 2-10. Separation of anions contained in public drinking water sample.

Operating conditions as in Figure 2-3.

The detected nitrate is still under maximum limit of the public drinking water

permission in the Padang city, West Sumatera-Indonesia. The anion-exchange capacity

of the stationary phase was not high enough to separate the water-dip with iodate, which

disturbed the accurate determination of iodate.

2.2 Conclusions

The simple and rapid method with poly(ethylene glycol) monolithic column by

thermal in situ polymerization for analyzing 5 anions has been reported. The

chromatographic experiments were shown that PEG monolith can be an alternative for

short determination of anions. Introduction of PEG-groups could improve theoretical

plates of the monolith compared without any PEG-groups. The PEG groups also have

satisfaction in mechanical stability that was proved by the fact that there is no

0 5 10 15 20 25

0.004 Abs

Standard

Public drinking water

Time / min

1

2

3

4

5

5

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32

significant swelling and shrinkage of the PEG monolith and it could be worked on

different polarities with the high flow rate. The present method allows determination of

anions contained in the seawater sample without any pretreatment before analyzing. The

bromide in seawater Padang beach and nitrate in public drinking water in Padang City

Indonesia have been determined by this method to be 44 ppm and 1.9 ppm, respectively.

2.3 References

[1] Y. Li, M.L. Lee, J. Jin, and J. Chen, Talanta, 99, (2012), 91-98.

[2] N. Tanaka, H. Kobayashi, N. Ishizuka, H. Minakuchi, K. Hosoya, and T. Ikegami,

J. Chromatogr. A, 965, (2002), 35-49.

[3] N. Ishizuka, H. Kobayashi, H. Minakuchi, K. Nakanishi, K. Hirao, K. Hosoya, T.

Ikegami, and N. Tanaka, J. Chromatogr. A, 960, (2004), 85-96.

[4] O. Nunez, T. Ikegami, K. Miyamoto, and N. Tanaka, J. Chromatogr. A, 1175,

(2007), 7-15.

[5] Siswoyo, L. W. Lim, and T. Takeuchi, Anal. Sci., 28, (2012), 107-113.

[6] F. Kitagawa, K. Kubota, K. Sueyoshi, and K. Otuska, J. Pharm. Biomed. Anal., 53,

(2010), 1272-1277.

[7] R. Wang, Y. Zhang, G. Ma, and Z. Su, Colloids and Surf., 51, (2006), 93-99.

[8] J. Courtois, E. Bystrom, and K. Irgum, Polymer, 47, (2006), 2603-2611.

[9] L. W. Lim, L. Rong, and T. Takeuchi, Anal. Sci., 28, (2012), 205-213.

[10] L. Rong and T. Takeuchi, J. Chromatogr. A, 1024, (2004), 131-135.

[11] L. Rong, L. W. Lim, and T. Takeuchi, J. Chromatogr. A, 1128, (2006), 68-72.

[12] T. Takeuchi, B. Oktavia, and L. W. Lim, Anal. Bioanal. Chem., 393, (2009),

1267-1272.

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Chapter 2

33

[13] R. Linda, L. W. Lim, and T. Takeuchi, J. Chromatogr. A, 1294, (2013), 117-121.

[14] T. Takeuchi and L. W. Lim, Anal. Sci., 26, (2010), 937-941.

[15] L. W. Lim, K. Tokunaga, and T. Takeuchi, Chromatography, 35, (2014), 95-101.

[16] F. Nevejans and M. Verzele, J. Chromatogr., 350, (1985), 145-150..

[17] L. Trojer, S. H. Lubbad, C. P. Bisjak, and G. K. Bonn, J. Chromatogr. A, 1117,

(2006), 56-66.

[18] S. H. Lubbad and M. R. Buchmeiser, J. Sep. Sci., 32, (2009), 2521-2529.

[19] W. Wieder, S. H. Lubbad, L. Trojer, C. P. Bisjak, and G. K. Bonn, J. Chromatogr. A,

1191, (2008), 253-262.

[20] D. Moravcova, P. Jandera, J. Urban, and J. Planeta, J. Sep. Sci., 27, (2004),

789-800.

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Chapter 3

34

Chapter 3

Preparation of hybrid monolithic stationary

phase with allylsulfonate for the rapid and

simultaneous separation of cations in capillary

ion chromatography

3.1 Introduction

Since monolithic columns appeared as a separation media in liquid

chromatography in the late of 1980s, they have attracted a great attention for wide

application in capillary liquid chromatography due to their advantages, such as easy

preparation compared to conventional particulate-packed columns and low back

pressure [1-4]. Based on the precursors used, monolithic columns can be divided into

two types: the organic-polymer-based and inorganic silica-based column. The former

has good points such as easy preparations, good stability in a wide pH range and the

flexibility of various combinations of monomers and cross-linkers. The latter provides

good mechanical stability and good solvent resistance. However, its fabrication process

is still time-consuming.

Recently, the organic-inorganic-silica-hybrid monolithic columns have been

developed rapidly since they are combining the advantages of both silica- and

organic-polymer-based monolithic columns such as exhibiting flexibility, low density,

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35

low cost, good stability and long shelf-life with excellent biocompatibility and

mechanical properties [5]. The incorporation of organic functional groups into the

inorganic silica monolith matrix was useful for avoiding the time-consuming

post-modification of common silica monoliths. One-pot approach was introduced as a

new strategy for more effective and sophisticated way in preparation of the monolithic

column for achieving various target separations. After reported by Zou in 2009 [6],

one-pot approach has been developed in different temperature of precondensation as

well as polymerization, then applied for separation of enantiomer, protein, peptides and

biomolecular species [7-10].

In liquid chromatography, strong cation-exchange (SCX) monolithic columns

have been widely applied for separation of proteins, peptides and inorganic cations

[11-13]. The SCX monolith was synthesized by in-situ preparation of polymer-based

organic and silica-based inorganic monoliths column with sulfonate functionalities

arising from the versatile post-modifications and in-situ chemical reactions. Generally,

the detections of compounds were reported using a UV detector and a photodiode array

detector (PAD). Nevertheless, hybrid monolith columns with SCX moieties have been

very little reported in the literatures. Zou et al. prepared strong cation-exchange

stationary phase for electrochromatography by sol-gel process, then applied for

separation of β-blockers and alkaloids extracted from traditional Chinese medicines

(TCMs) [14]. Zhang et al. successfully prepared sulfonate hybrid monolithic column by

one-pot approach with constant precondensation temperature but different

polymerization temperature before it is applied to proteome analysis [15]. Yang et al.

reported (potassium 3-sulfopropyl methacrylate)-silica hybrid monolithic columns have

been prepared in the same temperature of precondensation and polymerization process.

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Then it was applied for separation of different kinds of compounds including anilines,

alkylbenzenes and phenols by capillary electrochromatography (CEC) [16]. Most of

them were reported on the applications of hybrid monolithic column in CEC. In this

study, hybrid monolithic column for rapid and simultaneous separation of inorganic

cations in ion-exchange mode will be focused. The hybrid monolithic column with

sodium allylsulfonate (SAS) as organic monomer will be prepared by a single-step

thermal-treatment one-pot manner. The polycondensation and polymerization will be

carried out in short time at single temperature for time-saving and high efficiency

purposes. Sulfonate groups as strong cation exchange moieties were provided from SAS

and they could be directly added to the hydrolysis solution. Then the optimized

condition of allylsulfonate (AS)-hybrid monolithic column was applied for

simultaneous determination of cations in groundwater as well as effluent of domestic

wastewater treatment system in capillary ion chromatography. To the best of our

knowledge, this could be the first time that strong cation-exchange hybrid monolithic

columns have been established for rapid and simultaneous determination of inorganic

cations in ion-exchange chromatography mode.

3.2 Experimental

3.2.1 Apparatus

The chromatography separation was carried out using a capillary LC system

constructed by an L.TEX-8301 Micro Feeder (L.TEX corporation, Tokyo, Japan)

equipped with an MS-GAN 050 gas-tight syringe (0.5 ml, Ito, Fuji, Japan) as a pump, a

Model 7520 injector with an injection volume of 0.2 µl (Rheodyne, Cotati, CA, USA), a

100 mm x 0.32 mm i.d. of microcolumn and a UV-2075 intelligent UV/VIS detector,

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37

(JASCO, Tokyo, Japan) that was operated at 210 nm. The data was acquired using a

Chromatopac C-R7A data processor (Shimadzu, Kyoto, Japan). The inlet pressure was

monitored with L.TEX-8150 Pressure Sensor (L.TEX). The morphology of the column

was characterized by an S-4800 scanning electron microscope (Hitachi, Tokyo, Japan).

The characteristic of surface area and pore size distribution were measured by 3-Flex

Surface Characterization Analyzer (Micrometrics, Norcross (Atlanta), Georgia, City,

State, USA).

3.2.2 Reagents and materials

Tetramethoxysilane (TMOS), vinyltrimethoxysiane (VTMS), SAS,

2,2’-azobisisobutyronitrile (AIBN) and urea were obtained from TCI (Tokyo, Japan).

Polyethylene glycol (PEG, M.W.10000) was obtained from Aldrich (Rockford, IL,

USA). The copper (II) sulfate was of extra pure reagent grade (Nacalai Tesque, Kyoto,

Japan). Purified water was produced in the laboratory by using a GS-590 water

distillation system (Advantec, Tokyo, Japan). All other reagents used in the experiment

were of guaranteed reagent grade. All the cation solutions used in this study were

prepared from extra pure reagents obtained from Nacalai Tesque.

3.2.3 Preparation of AS-hybrid monolith

The fused silica capillary tube (0.320 mm i.d. x 0.450 mm o.d.) was purchased

from GL Sciences (Tokyo, Japan). Prior to use, fused silica capillary tube was washed

sequentially with 1M NaOH solution, deionized water, 1M HCl and deionized water for

30 min each, and dried by nitrogen at room temperature for further use. The AS-hybrid

monolithic column was prepared by mixing and stirring of TMOS (0.18 ml), VTMS

(0.06 mL), acetic acid (0.5 mL), urea (45 mg) and PEG (10000 MW, 54 mg) at 0 ˚C for

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38

1 h and hydrolyzing it to form a homogenous solution. Then 35-50 mg of SAS and 2 mg

of AIBN were added into the mixture solution with 15 min of sonication for mixing.

After that, it was manually introduced into the pretreated capillary tube to the

appropriate length by syringe and both ends of the tube were sealed. The condensation

and polymerization were carried out at 60 ˚C for 12 h. The obtained AS-hybrid monolith

columns were then flushed with methanol in order to remove the PEG and other

residuals.

3.3 Result and discussions

3.3.1 Preparation of AS-hybrid monolithic column

In this research, AS-hybrid monolithic column was prepared based on one-pot

manner that simultaneous mixing of silane monomers and organic monomers. The

scheme of the expected reaction for preparing the sulfonate hybrid is based on two

major reactions, as shown in Figure 3-1: the polycondensation of hydrolyzed precursors

of TMOS and VTMS, and the copolymerization of SAS and vinyl organic monomers.

Fig. 3-1. Schematic diagram of the expected reaction for the preparation of AS-hybrid

monolithic column.

The temperature is one of the sensitive factors in the preparation of AS-hybrid

monolith during polycondensation that can give a good performance and permeability.

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39

The columns were synthesized at 50 °C (column F) until 80 °C (column H) with AIBN

as the initiator. The mechanical stability results of the AS-hybrid monolith at different

temperatures of polycondensation were shown in Table 3-1. By changing the

temperature from 50 °C to 80 °C keeping the reaction time 12 h, the permeability value

decreased from 11×10-12

to 5.5×10-12

m2 and the pressure drop as well increased from

0.2 to 0.4 MPa (under operational condition 2 µL/min). The preparation of AS-hybrid

monolith at 60 °C was found the highest value of theoretical plates 19017 plate/m (in

the case of NH4+ as the analyte). Based on this, the temperature at 60 ºC was then

applied in the following preparation of AS-hybrid monolith.

Table 3-1. Effects of preparation parameters on the fabrication of AS-hybrid monolith

column.

a) Sodium allylsulfonate (SAS) as organic monomer b) System operated with CuSO4 at flow rate 2 µL/min

The organic monomer and silane were simultaneously mixed in the developed

“one-pot” manner. The quantity of organic monomer in this reaction should be

Back k

Pressureb) Permeability

(mg) (h) (°C) (MPa) 10-12

(m2) (plates/m)

A 35 9 60 0.2 11 6107

B 35 12 60 0.2 11 19017

C 35 18 60 0.5 4.4 4214

D 35 24 60 0.6 3.3 12707

E 35 36 60 0.8 2.6 8603

F 35 12 50 0.2 11 15869

G 35 12 70 0.3 7.3 19001

H 35 12 80 0.4 5.5 15636

I 30 12 60 0.2 11 8795

J 40 12 60 0.2 11 14100

K 45 12 60 0.2 11 14220

L 50 12 60 0.2 11 14618

ColumnSAS

a) Time Temp N max

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40

examined because it affects the formation of the hybrid monolith column. The

precondensation mixture was prepared with different amounts of SAS, i.e., 30, 35, 40,

45 and 50 mg. As shown in Table 3-1, the permeability values of the column were stable

at 11×10-12

m2 when the amount of SAS were 30, 35, 40, 45 and 50 mg (column I, B, J,

K, and L). Additionally, the theoretical plates were different by changing the amount of

SAS. By these results, the optimum amount of SAS that provided the best theoretical

plates in precondensation mixture was 35 mg (in the case of NH4+ as the analyte).

Further increased amount of SAS would result in increasing the amount of unreacted

residuals that are difficult to be eluted during the preparations of AS-hybrid monolith.

Fig. 3-2. The relationship of preparation time and the amount of sulfonate groups

(denoted as cation-exchange capacity) of the AS-hybrid monolith.

Figure 3-2 shows the relationship of preparation time and the amount of

sulfonate groups (denoted as cation-exchange capacity) of the AS-hybrid monolith. The

precondensation and prepolymerization conditions were kept at 60 °C and 35 mg as the

amount of SAS added. As seen in Figure 3-2, the cation-exchange capacities of the

AS-hybrid monolith columns (A-E) that were prepared for 9, 12, 18, 24, and 36 h were

0.74, 0.80, 0.81, 0.82 and 0.83 mequiv/mL, respectively. The capacity linearly increased

0

0.5

1

1.5

9 12 18 24 36

Cati

on

-exch

an

ge

cap

asi

ty

(meq

uiv

/mL

)

Reaction time (hour)

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41

by the longer preparation time of up to 10 h and was nearly constant at longer

preparation time. These indicated that the capability of a monolithic column as

AS-hybrid monolith could be successfully achieved by changing preparation time of the

AS-hybrid monolith, and these monolithic capillary columns could be produced by

different capacities of up to 0.83 mequiv/mL.

3.3.2 Separation of common inorganic cations on ion-exchange mode

The sulfonate groups of the AS-hybrid monolithic column work as a strong

cation-exchange site that interacts with positively charged compounds through

electrostatic interaction. The common inorganic cations were used to examine the

cation-exchange characteristic of the AS-hybrid monolith. The common cations were

indirectly detected with UV absorption at 210 nm and copper (II) sulfate as eluent.

Fig. 3-3. Separation of inorganic cations on the AS-hybrid monolith.

Operating conditions: Analytes, 1 mM of each Li+ (1), Na

+ (2),

NH4+ (3), K

+ (4), Rb

+ (5), Cs

+ (6), Mg

2+ (7), Ca

2+ (8), and Sr

2+

(9); SCX hybrid monolith column (100 x 0.32 mm i.d.); 5 mM of

CuSO4 eluent; 2 µL/min flow rate; 210 nm wavelength of UV

detection and 0.2-µL injection volume.

0 10 20

1.2

3

4

5

6

7 8

90.002 Abs

Time / min

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As shown in Figure 3-3, common inorganic cations such as Li+, Na

+, NH4

+, K

+,

Rb+, Cs

+, Mg

2+, Ca

2+ and Sr

2+ were separated well except peaks of overlapped Li

+ and

Na+.

These suggest that the cation-exchange capacity of the AS-hybrid was not high

enough to separate the Li+ and Na

+ because the ionic radius of Li

+ (0.090 nm) is close to

Na+ (0.116 nm). The resolution between two cations, i.e., Mg

2+, Ca

2+ of the As-hybrid

was 0.66. Furthermore, the separation performance of cations was quite better for some

peak when used longer capillary column (15 cm of length) with the resolution between

two cations, i.e., Mg2+

and Ca2+

was 0.96. However by changing the length of capillary

column did not show the significant changes for separation of Li+ and Na

+. The

separation was carried out at flow rate 2 µL/min with 0.2 MPa of pressure drop. In

addition, the effect of copper (II) sulfate concentration (log [CuSO4]) as the eluent on

the retention factor (log k) was investigated.

Fig. 3-4. Effect of copper (II) sulfate concentration (log [CuSO4]) on

retention (log k) of inorganic cations. The symbols in the figure

represent as (●) Li+, (△) Na

+, (▲) NH4

+, (□) K

+, (▼) Rb

+, (■)

Cs+, (+) Mg

2+, (×) Ca

2+, (◆) Sr

2+. Operating conditions as in

figure 3-3.

0 0.2 0.4 0.6 0.8 1 1.2

-0.3

0

0.3

0.6

0.9

1.2

Log [CuSO 4]

Lo

g k

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43

Figure 3-4 shows the logarithm of the retention factor (log k) of cations as the

function of the logarithm of the eluent concentrations. The retention of each cation

decreased with increasing the concentration of eluent, which indicates that the

separation mechanism of the cations on the AS-hybrid monolith involved cation

exchange.

3.3.3 Comparison of AS-hybrid and particle-packed capillary

In order to know the performance of AS-hybrid column, the mechanical stability

of an AS-hybrid monolithic capillary column was compared with a particle-packed

capillary column. As a packing material, IC cation SW (5 µm) (Tosoh, Tokyo, Japan)

was packed on a 100 mm x 0.32 mm i.d. microcolumn. Figure 3-5 shows the separation

performance of IC cation SW under operating conditions for 5 mM CuSO4 as the eluent

and 2 µL/min as the flow rate. The packing material could separate the common

inorganic cations especially for monovalent (Li+ and Na

+) as well as divalent (Mg

2+ and

Ca2+

) whereas NH4+, K

+, Rb

+ and Cs

+ were poorly separated. The higher

cation-exchange capacity of particle-packed column than As-hybrid might be one of the

reason why the separation was better. The packed capillary column with

cation-exchange capacity around 0.99 mequiv/mL had lower theoretical plate (11240

plates/m) compared to the AS-hybrid (19017 plates/m) (in the case of NH4+ as the

analyte). In addition, the pressure drop for the packed capillary column reaches 1.5 MPa

and the elution time was more than 90 min. On the contrary, AS-hybrid only reached 0.2

MPa and the elution time was only 15 min. These results indicate that the AS-hybrid

monolith has better performance in terms of speed and the pressure drop than the

packed capillary column under the same operating condition.

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44

Fig. 3-5. Separation of inorganic cations on a cation-exchanger packed

capillary column. Packing material, IC cation SW (5µm) packed

into 100 x 0.32 mm i.d. Operating conditions as in Figure 3-3.

3.3.4 Characterization and mechanical stability of AS-hybrid

monolithic column

After optimization of the preparation condition, the AS-hybrid monolith was

subsequently characterized. The scanning electron microscopy (SEM) photos of

AS-hybrid monolith capillary column prepared under the optimum condition were

shown in Figure 3-6A. It is shown that the AS-hybrid monolith formed is attached to the

inner wall of the capillary tube. It is because the silanol groups at the inner wall of the

capillary tube are an important part in the polycondensation during preparation of

0 20 40 60 80

0.002 Abs

Time (min)

7 8

9

21

3

4

5

6

Fig. 5

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45

AS-hybrid monolith column [17]. A uniform organic-silica hybrid monolithic matrix

with large through-pores was obtained, leading to little pressure drop as shown in Figure

3-6B and 3-6C.

A. 320 × B. 600 ×

C. 3000 ×

Fig. 3-6. Scanning electron microscope images of AS-hybrid monolith.

Magnification = 320x (A), 600x (B), and 3000x (C)

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46

The effect of the flow rate on the pressure drop across the AS-hybrid monolith

column for four different solvents was displayed in Figure 3-7. This figure shows that

the pressure drop of each solvent has good linear relationship with flow rate. When the

flow rate was raised up to 10 µL/min, the pressure drop increased maximum up to 2.6

MPa (for THF), this means that the AS-hybrid monolith had good performance and

could be operated at higher flow rate and less pressure drop.

The mechanical stability of the AS-hybrid monolith was examined by

calculating the permeability and the swelling propensity (SP) factor. By plotting the

pressure drop against the flow rate, permeability and SP factor could be obtained. The

calculation of the permeability (B0) followed Darcy’s law Equation (1) [18], where F is

the flow rate of the mobile phase, η is the viscosity of the mobile phase, L is the

effective length of the column, r is the inner radius of the column and △P is the

pressure drop across the column. The permeability was measured by pumping water

through the column with increasing the flow rate from 0.5 to 4 µL/min, leading to the

increase in the pressure drop from 0.1 to 0.4 MPa. The permeability value of AS-hybrid

monolith was 11×10-12

m2 under optimum operation condition (flow rate; 2µL/min).

This indicated that AS-hybrid monolith can run excellently with mechanical stability

under high-pressure drop.

0 2

FηLB

r P

(1)

(solvent) - (water)SP =

(water)

p p

p (2)

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47

The As-hybrid monolithic column stationary phase was characterized by pore

structure consisting of pore size distribution and surface area which was determined by

nitrogen adsorption isotherms method. A narrow size distribution was around 1 nm with

the pore volume of 0.5 cm3/g and the BET surface area was measured around 164 m

2/g.

The pore size in the As-hybrid monolithic column was smaller than the other hybrid

columns [19, 20], which may be associated to the presence of the sulfonate groups on

the surface of pore in the hybrid monolithic column.

The swelling propensity (SP) was calculated by using the Equation (2) [21],

where p is the pressure drop relative to the viscosity, p = ΔP/η. In general, the SP value

of non-swelling material is zero. The swelling occurs more when the SP shows higher

value whereas a negative value of SP indicates shrinkage of the monolith [22]. In this

study, the SP value of AS-hybrid monolith (Column B) was determined by using water

as the eluent for 30 min and the pressure drop was marked. The eluent was then

changed to THF and waits until the system became stable, and the pressure drop was

marked. Acetonitrile was also operated with the same way as water in determination of

SP. The SP value determined by applying THF and acetonitrile was found to be around

0.64, and 0.11, respectively. These values indicated that AS-hybrid monolith shows no

significant swelling and shrinkage of the AS-hybrid monolith rod observed, hence these

monoliths could work on different polarities with the high flow rate compared to the

packing materials reported with SP values from 0.05~7.4 [19].

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48

Fig. 3-7. Back pressure of column B as a function of flow rate of (◇)water,

(▲)methanol, (□)acetonitrile, and (●)THF.

3.3.5 Reproducibility of AS-hybrid monolithic column

The repeatability of the retention time (tR) and the peak height were calculated

under the optimum conditions as seen in Table 3-2. The relative standard deviations

(RSDs), for n=6 of the retention time and peak height were found less than 1.96% for

all the analyte cations. This value showed the satisfactory reproducibility of the

AS-hybrid monolith. Based on this result, the AS-hybrid monolith in our study showed

better improvement on performance than in other previous literatures that determination

of common inorganic cations using diol-group bonded silica gel with

1,3-propanesultone [23], which indicated that the AS-hybrid monolith columns had

exceptional reproducibility, and the preparation of organic-inorganic hybrid monolithic

column using “one-pot” approach manner was feasible.

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49

Table 3-2. Summarized data for the retention time (tR), relative standard deviations

(RSDs), limits of detection (LODs) of common inorganic cations. Operation condition

as in Figure 3-3.

In addition, the limits of detection of these nine common inorganic cations

were determined by injection of 0.2-µL volume of the sample, 1 mM each of cation, and

the detection limits were calculated at signal-to-noise ratio of 3. The detection limits

obtained by this method ranged from 0.09 – 0.93 ppm for the cations as shown in Table

3-2.

3.3.6 Application to real samples

The one-pot approach method of AS-hybrid monolith columns were applied for

the determination of common inorganic cations in the real samples. Two different

samples, one is groundwater sample from Padang City, Indonesia, and another is the

effluent of onsite domestic wastewater treatment system that was collected from Gifu

city, Japan, were used for application. The water samples were examined by the method

LOD

Retention time Peak height S/N = 3 (ppm)

Li+ 5.70 0.49 1.96 0.09

Na+ 5.70 0.49 1.96 0.09

NH4+ 7.00 0.59 1.83 0.08

K+ 7.52 0.57 1.90 0.21

Rb+ 7.88 0.53 1.94 0.50

Cs+ 8.21 0.40 1.71 0.93

Mg2+ 13.70 0.51 1.96 0.14

Ca2+ 14.40 0.60 1.85 0.23

Sr2+ 15.30 0.52 1.95 0.72

Cations tR (min)RSD (%, n = 6)

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50

within a few days after collection. As prior treatment, the samples were filtered through

a 0.45 µm membrane filter for ion chromatography sample. Figure 3-8 shows

chromatograms of groundwater and standard mixture of nine common inorganic cations.

It can be seen that these inorganic cations are properly detected. The concentrations of

inorganic cations for Na+, NH4

+, Cs

+, Mg

2+ and Ca

2+ were 9.1, 1.6, 5.7, 6.3 and 41.9

ppm, respectively. On the other hand, a chromatogram of the effluent of onsite domestic

wastewater treatment system for Na+, K

+, Mg

2+ and Ca

2+ was successfully obtained,

where the concentration of each cation was 27.5, 4.5, 3.5, and 28.3 ppm, respectively

(Figure 3-9).

Fig. 3-8. Separation of cations contained in groundwater sample.

Groundwater sample (A); standard inorganic cations (B);

operating conditions as in Figure 3-3.

0 10 20

(A)

(B)

1.2

3

4

5

6

7 8

9

Time (min)

0.002 Abs

7

8

2

3 6

Fig. 8

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Chapter 3

51

Fig. 3-9. Separation of cations contained in the onsite domestic

wastewater treatment system sample. The onsite domestic

wastewater treatment system sample (A); standard inorganic

cations (B); operating conditions as in Figure 3-3.

3.4 Conclusions

An AS-hybrid monolithic capillary column with strong cation-exchange

moieties was successfully fabricated for the simultaneous separation of common

inorganic cations in ion-exchange chromatographic mode. The simple and easy

preparation with incorporation of SAS into the silica monolith matrix was carried out by

single-step thermal-treatment one-pot manner. Nine common inorganic cations (Li+, Na

+,

NH4+, K

+, Rb

+, Cs

+, Mg

2+, Ca

2+ and Sr

2+) could be satisfactorily separated with

sufficient relative standard deviations and low limits of detection. The satisfactions of

0 10 20

(A)

(B)

0.002 Abs

1.2

3

45

6

7 8

9

Time / min

2

4

7

8

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Chapter 3

52

AS-hybrid monolith columns in mechanical stability were proved by the fact that no

significant swelling or shrinkage occurred in the columns and it could also work in

solutions with different polarities at high flow rates. This method showed the elution of

cations within 15 min with the pressure drop of only ca. 0.2 MPa, which has better

performance in terms of speed and the pressure drop than the particle-packed capillary

column. Based on the results in our work and compared to other literatures, we found a

novel application of an AS-hybrid monolithic column for rapid and simultaneous

determination of both common monovalent and divalent inorganic cations in

ion-exchange chromatography mode.

3.5 References

[1] F. Svec, J. Sep. Sci., 27, (2004), 1419-1430.

[2] G. Guiochon, J. Chromatogr. A, 1168, (2007), 101-168.

[3] N. Ishizuka, H. Kobayashi, H. Minakuchi, K. Nakanishi, K. Hirao, K.

Hosoya, T., Ikegami, T. Tanaka, J. Chromatogr. A, 960, (2002), 85-96.

[4] V. S. Aguiar, C. B. G. Bottoli, Microchem. J. 109, (2013), 51-57.

[5] T. Zhu, K. H. Row, J. Sep. Sci., 35, (2012), 1294-1302.

[6] M. Wu, R. Wu, F. Wang, L. Re, J. Dong, Z. Liu, H. Zou, Anal. Chem., 81,

(2009), 3529-3536.

[7] Z. Zhang, M. Wu, R. Wu, J. Dong, J. Ou, H. Zou, Anal. Chem., 83, (2011),

3616-3622.

[8] M. Wu, R. Wu, R. Li, H. Qin, J. Dong, Z. Zhang, H. Zou, Anal. Chem., 82,

(2010), 5447-5454.

[9] Z. Lin, H. Huang, S. Li, J. Wang, X. Wang, X. Tan, L. Zhang, G. Chen, J.

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Chapter 3

53

Chromatogr. A, 1271, (2013), 115-123.

[10] H. Xu, Z. Xu, L. Yang, Q. Wang, J. Sep. Sci., 34, (2011), 2314-2322.

[11] K. Zhao, L.Yang, X. Wang, Q. Bai, F. Yang, F. Wang, Talanta, 98, (2012), 86–

94.

[12] R. Wu, H. Zou, H. Fu, W. Jin, M. Ye, Electrophoresis, 23, (2002), 1239–1245.

[13] Y. Ueki, T. Umemura, J. X. Li, T. Odake, K. I. Tsunoda, Anal. Chem., 76,

(2004), 7007-7012.

[14] C. Xie, J. Hu, H. Xiao, X. Su, J. Dong, R. Tian, Z. He, H. Zou, J. Sep. Sci., 28,

(2005), 751-756.

[15] Z. Zhang, F. Wang, B. Xu, H. Qin, M. Ye, H. Zou, J. Chromatogr. A, 1256,

(2012), 136–143.

[16] H. Yang, Y. Chen, Y. Liu, L. Nie, S. Yao, Electrophoresis, 34, (2013), 510-517.

[17] Y. Tian, L. Zhang, Z. Zeng, H. Lis, Electrophoresis, 29, (2008), 960–970.

[18] R. D. Stanelle, L.C. Sander, R. K. Marcus, J. Chromatogr. A, 1100, (2005),

68-75.

[19] L. Yan, Q. Zhan, W. Zhang, Y. Feng, L. Zhang, T. Li, Y. Zhang, Electrophoresis,

26, (2005), 2935-2941.

[20] J. Ma, G. Yang, C. Yan, Y. Gu, L. Bai, Y. Duan, J. Li, Anal. Methods, 4, (2005),

247-253.

[21] F. Nevejans and M. Verzele, J. Chromatogr,. 350, (1985), 145-150.

[22] L. Trojer, S. H. Lubbad, C. P. Bisjak and G. K. Bonn, J. Chromatogr. A, 1117,

(2006), 56-66.

[23] L. Rong, Z. Liu, M. Ma, J. Liu, Z. Xu, L.W. Lim, T. Takeuchi, Anal. Sci., 28,

(2012), 367-371.

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Chapter 4

54

Chapter 4

“One-pot” approach for fabrication of

3-sulfopropyl methacrylate-co-ethylene

dimethacrylate monolithic column for capillary

liquid chromatography

4.1. Introduction

The polymer monolithic columns were introduced in the late 1980s with the

development of the continuous bed by Hjertén [1]. Afterwards, polymer monolithic

columns have attracted increasing attention in various applications in liquid

chromatography. Many developments have been made within the field in terms of their

fabrication and applications. The polymer monolithic columns possess many advantages

such as easiness of preparations, good stability in a wide pH range and the flexibility of

various combinations of monomers and cross-linkers. Polymer monolithic columns are

produced by in-situ thermal polymerization of organic monomers, including

cross-linkers and porogen for forming the porosity in the monolith.

Recently, wide range combinations of the polymer mixture are used for the

synthesis of polymer monoliths. Because the monomer and crosslinker are an integral

part of the formed material, the characteristics result of the monolith depends on the

composition of the polymerization mixture. During the last decade, polymer monolithic

columns represent polymethacrylate and polyacrylate monoliths based [2, 3]. Most of

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Chapter 4

55

them are used for separation of mainly macromolecules such as nucleic acid, proteins,

and peptides [4-6]. However, the post-modifications were required during these

preparations as well as the application to separation of small analytes especially to ion

chromatography (IC) such as inorganic anions and cations [7-10]. The separation of ions

occurs in electrostatic interactions among analytes and stationary phase containing

ion-exchange site.

Monolithic columns with strong-cation exchange site have been widely applied

for separation of proteins, peptides and inorganic cations [11-13]. Silica hybrid has been

successfully prepared by single thermal preparation containing sulfonate groups as

strong cation exchange site for proteome analysis using 3-sulfopropyl methacrylate

potassium salt as functional monomer [14]. The potassium (3-sulfopropyl

methacrylate)-silica hybrid monolithic column for the capillary electrochromatography

(CEC) separation of different kinds of compounds including anilines, alkylbenzenes and

phenols also was reported by Yang et al.[15]. However, single step thermal preparation

of polymeric monoliths column with the sulfonate groups from functional monomer for

the separation of cations has been little reported in the literatures.

In order to eliminate the consuming of time for post-modifications, in the

present study, a single step thermal preparation of organic polymer monolithic column

consisting the polymerization of sulfonate monomer was examined. 3-Sulfopropyl

methacrylate potassium salt (SPMP) was chosen as functional monomer to introduce

sulfonate functional groups worked as cation-exchange site. The present method could

represent a simpler and more convenient way to prepare polymer monolithic columns.

The chromatographic performances were investigated through separation of small

mixture of common inorganic cations.

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Chapter 4

56

4.2. Experimental

4.2.1 Apparatus

The chromatographic separation was carried out using a capillary LC system

constructed by an L.TEX-8301 Micro Feeder (L.TEX corporation, Tokyo, Japan)

equipped with an MS-GAN 050 gas-tight syringe (0.5 mL, Ito, Fuji, Japan) as a pump, a

Model 7520 (Rheodyne, Cotati, CA, USA) injector with an injection volume of 0.2 µL,

a 100 mm x 0.32 mm i.d. of microcolumn and a UV-1575 intelligent UV/VIS detector,

(JASCO, Tokyo, Japan) that was operated at 210 nm. The data was acquired using

Chromatopac C-R7A data processor (Shimadzu, Kyoto, Japan). The inlet pressure was

monitored with an L.TEX-8150 Pressure Sensor (L.TEX).

4.2.2 Reagent and materials

3-Sulfopropyl methacrylate potassium salt (SPMP) and ethylene dimethacrylate

(EDMA) (97%) were obtained from Wako. n-Decyl alcohol, 3-(trimethoxysilyl)propyl

methacrylate (γ-MAPS, 98%) and 2,2’-azobisisobutyronitrile (AIBN) were obtained

from TCI (Tokyo, Japan) and 1,4-butanediol, was obtained from Nacalai Tesque (Kyoto,

Japan). The copper (II) sulfate was of extra pure reagent grade (Nacalai Tesque, Kyoto,

Japan). Purified water was produced in the laboratory by using a GS-590 water

distillation system (Advantec, Tokyo, Japan). All other reagents used in the experiment

were of guaranteed reagent grade. All the cation solutions used in this study was

prepared from extra pure reagents obtained from Nacalai Tesque.

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Chapter 4

57

Preparation of SPMP-co-EDMA monolithic column

The fused silica capillary tube (0.320 mm i.d. × 0.450 mm o.d.) was purchased

from GL Sciences (Tokyo, Japan). Fused silica capillary tube was washed using 1 M

NaOH solution, deionized water and 1 M HCl in sequence. 30 % (v/v) of γ-MAPS in

acetone was used for anchoring the inner wall surface of the capillary tube and

providing the methacrylate groups to the wall; the tube was sealed at both ends and

thermal-treated in a water bath at 60˚C for 24 h. Thereafter, the capillary tube was

washed with acetone and dried using nitrogen gas for 30 min. The various compositions

of polymerizations mixture solutions of SPMP as functional monomer, cross-linker and

porogen were investigated as shown in Table 4-1. Then, 0.1 mL of the solution was

completely mixed with 2 mg of AIBN as the polymerization initiator. The mixture

solution was then subjected to ultrasonic vibration for 5 min before it was injected into

the pretreated capillary tube. Thermal polymerization was done in the water bath at

60˚C for 24 h. The capillary tube was rinsed with methanol thoroughly after

polymerization to remove unreacted reagent and porogenic solvents.

Table 4-1. Various polymerization conditions.

a 3-sulfopropyl methacrylate potassium salt (SPMP) was used as functional monomer.

b Ethylene dimethacrylate (EDMA) was used as cross-linker.

c 1-propanol, 1,4-butanediol and water were used as porogen.

d The volume ratio of monomer + cross-linker to porogen.

e 60 ºC was the polymerization temperature and kept for 24 h.

Column Monomera

Crosslinkerb

Porogenc Mixture Polymerization

% (v/v) % (v/v) % (v/v) ratiod

conditione

SPMP1 7.5 2.5 90 10/90 60 ˚C, 24 h

SPMP2 15 5 80 20/80 60 ˚C, 24 h

SPMP3 22.5 7.5 70 30/70 60 ˚C, 24 h

SPMP4 30 10 60 40/60 60 ˚C, 24 h

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Chapter 4

58

4.3. Result and discussion

4.3.1. Preparation of SPMP-co-EDMA

The preparation of cation-exchange monolithic stationary phase with different

cation-exchange capacities was investigated. Sulfonate groups could be directly

incorporated into the polymer matrix by using 3-sulfopropyl methacrylate potassium

salt (SPMP) as a functional monomer. The performance of the monolith column was

influenced by ratio of monomer to porogen. Firstly, the ratio of monomer to porogen

was mainly investigated by keeping the cross-linker content. Figure 4-1 shows the

relationship of the mixture ratio of monomer and porogen of SPMP-co-EDMA

monolithic column and the amount of sulfonate groups that was denoted as

cation-exchange capacity. The polymerization temperature was kept at 60 ºC for 24 h.

As can be seen in Figure 4-1, the cation-exchange capacities of monolith columns

immersed for 10/90, 20/80, 30/70 and 40/60 (% monomer and porogen) were 0.50, 0.52,

0.58, and 0.69 mequiv/mL, respectively. Hence, increasing the ratio of monomer

affected the amount of sulfonate groups that was denoted as cation-exchange capacity.

Furthermore, the capacities linearly increase with increase in the ratio of monomer

confirmed that the functional monomer SPMP plays a role in the process of

polymerization and sulfonation.

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Chapter 4

59

Fig. 4-1. Effect of the mixture ratio of monomer and porogen of

SPMP-co-EDMA monolithic column on cation-exchange capacity.

The polymerization temperature was kept at 60 ºC.

Additionally, amount of porogen that worked for forming the pore in the

monolith affected the pressure drop of the system. Theoretically, less amount of porogen

offer the tight or fully pack of the monolith in the capillary tube and show the higher

pressure drop system. Figure 4-2 shows the relationship between pressure drop and

percentage of porogen. When monolith formed by 60 % amount of porogen shows the

highest pressure drop system up 0.9 MPa and when 90 % amount of porogen was used,

the pressure drop was only 0.5 MPa. By this plot it can be confirmed that increasing the

percentage of porogen in a mixture solution of polymerization will decrease the pressure

drop of system.

0

0.2

0.4

0.6

0.8

1

10/90 20/80 30/70 40/60

Cat

ion

-exch

ange

capas

ity

(meq

uiv

/mL

)

Mixture ratio

(% monomer/porogen)

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Chapter 4

60

Fig. 4-2. Effect of the mixture ratio of monomer and porogen of

SPMP-co-EDMA monolithic column on pressure drop. The column

(100 x 0.32 mm i.d.), flow rate was kept at 4 µL/min, 10 mM of

CuSO4 eluent.

Temperature plays the vital role in skeleton in forming the pore of monolithic

column, so the preparation temperature was also carefully optimized by the

polymerization was kept for 24 h. The monolith could not be well formed at 40 ºC. The

monolith matrix was not formed and detached from inner wall of the capillary wall,

which can be ascribed to incompleteness of the polymerization with anchor of the

methacrylate groups in the inner wall. At the high temperature, the homogeneity of the

monolith with tight anchoring to the inner wall surface of capillary would improve. In

other words, the pressure drop of the system will increase as a result influenced by the

amount of polymer formed at high temperature. The polymerization at the low

temperature (50ºC) only showed 0.3 MPa of pressure drop. Contrarily, 1.2 MPa was

reached when polymerization was done at 80 ºC.

0

0.5

1

1.5

60 70 80 90

Pre

ssure

dro

p (

MP

a)

Amount of porogen

(%)

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Chapter 4

61

Because it uses functional monomer, the large polymer is formed at long time

of polymerization, so the increase of the cation-exchange capacity of the monolith was

observed. Figure 4-3 described the effect of the polymerization time on cation-exchange

capacity. As has been predicted, the cation-exchange capacity increased with increasing

polymerization time. It was increased from 0.50 to 0.69 mequiv/mL when the

polymerization was carried out from 6 to 36 h, respectively.

Fig. 4-3. Effect of polymerization time of SPMP-co-EDMA monolithic column on

cation-exchange capacity. The polymerization temperature was kept at

60 ºC.

4.3.2. Separation of common inorganic cations in ion-exchange mode

The sulfonate groups introduced from 3-sulfopropyl methacrylate potassium salt

as monomer in monolithic column work as a strong cation exchange site that interacts

with positively charged compounds through electrostatic interaction. The common

inorganic cations were used to examine the cation-exchange characteristic of the

SPMP-co-EDMA monolithic column. The cations were indirectly detected with UV

absorption at 210 nm and copper (II) sulfate as eluent. Firstly, in order to check the

capability of SPMP-co-EDMA monolith column, the separation performance and

0

0.2

0.4

0.6

0.8

1

6 12 18 24 36

Cat

ion

-exch

ange

capas

ity

(meq

uiv

/mL

)

Polymerization time (h)

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Chapter 4

62

selectivity of cation-exchange column thus produced were evaluated by separating the

monovalent and divalent cations, mixture of NH4+ and Mg

2+ were injected as analyte.

From Figure 4-4, it can be seen that the cations with different positive charge could be

separated on the column by using 5 mM CuSO4 as the eluent. However, the broadening

peak of Mg2+

was found. It seems that the sulfonate group which works as

cation-exchange site was not strong enough to separate monovalent and divalent cations.

Figure 4-5 demonstrated the separation of monovalent cations on the SPMP-co-EDMA

monolithic column using 5 mM copper (II) sulfate. It is found that the Na+, NH4

+ and

K+ could be separated on 10 cm column with the number of theoretical plate 1628

plates/m for NH4+.

Fig. 4-4. Separation of cation on SPMP4 monolith column. Operating

conditions: Analytes, 1 mM each of NH4+, and Mg

2+. Column (100

x 0.32 mm i.d.); 5 mM of CuSO4 eluent; 4 µL/min flow rate; 210

nm wavelength of UV detection and 0.2 µL injection volume.

0 10 20 30

NH4+

Mg2+

0.02 Abs

Time (min)

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Chapter 4

63

Fig. 4-5. Separation of monovalent cation on SPMP4 monolith column.

Analytes, 1 mM each of Na+, NH4

+, and K

+. Operating conditions

as in Figure 4-4.

Figure 4-6 shows the effect of retention time of inorganic monovalent cations

as a function of the copper sulfate concentration in the eluent. The longer retention time

of each cation was found with decreasing concentration of eluent, which indicates that

the separation mechanism of the cations on the SPMP-co-EDMA monolith column

involved cation-exchange and copper ion is a carrying ion.

0 5 10 15

0.02 Abs

Time (min)

Na+

NH4+

K+

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Chapter 4

64

Fig. 4-6. Effect of retention of inorganic monovalent cations as a function of

CuSO4 concentration in the eluent. Operating conditions as in

Figure 4-4.

4.3.3. Separations at high flow rate

The merits of the monolithic column such as the good mechanical strength of

the construction and low flow resistance make it possible to operate at high flow rate

and provide the high speed of separations. Figure 4-7 shows chromatograms separation

of Na+, NH4

+ and K

+ at different flow rates. As expected, the elution time was decreased

with increasing flow rate. The effect of height equivalent to a theoretical plate (HETP)

to a different flow rate of the mobile phase is described in Figure 4-8. It can be seen that

HETP increases with increasing flow rate. In other word, HETP increased ~10 times

higher, when the flow rate was raised from 2 to 15 µL/min.

0 2 4 6 8 10 122

4

6

8

10

[CuSO4] (mM)

Ret

enti

on t

ime

(min

)

Na+

NH4+

K+

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Chapter 4

65

Fig. 4-7. Separation of common cations at different flow rates of (A) 2, (B) 4,

(C) 6, (D) 8, (E) 15 µL/min. Sample, 1 mM each of Na+, NH4

+ and K

+.

Operating conditions as in Figure 4-4.

Fig. 4-8. Effect of flow rate on height equivalent to a theoretical plate of K+.

Operating condition as in Figure 4-4.

0 5 10 15 20 25 30

Na+

NH4+

K+

(A)

(B)

(C)

(D)

(E)

0.1 Abs

Time (min)

0 5 10 15 200

1

2

3

Flow rate (μL/min)

HE

TP

(m

m)

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Chapter 4

66

4.4. Conclusions

Strong cation-exchange monolith columns were produced by single step

thermally treatment procedure involving the polymerization of 3-sulfopropyl

methacrylate potassium salt as functional monomer which introduced sulfonate groups

with ethylene dimethacrylate (EDMA). SPMP-co-EDMA monolith column has great

selectivity and strong retention for separation of monovalent cations by indirectly

detected with UV absorption at 210 nm and copper (II) sulfate as eluent. The present

monolithic column has great mechanical stability which could be operated at high flow

rates.

4.5. References

[1] S. Hjertén, J. L. Liao, and R. Zhang, J. Chromatogr., 473, (1989), 273–275.

[2] E. Vlakh and T. Tennikova, J. Sep. Sci., 30, (2007), 2801-2813.

[3] M. R. Buchmeiser, Polymer, 48, (2007,) 2187-2198.

[4] A. Hanora, I. Savina, F. M. Plieva, V. A. Izumrudov, B. Mattiasson, and I. Y.

Galaev, J. Biotech., 123, (2006), 343–355.

[5] S. Xie, F. Svec, and J. M.J. Fréchet , J. Chromatogr. A, 775, (1997), 65–72.

[6] J. Krenkova, N. A. Lacher, and F. Svec, J. Chromatogr. A, 1216, (2009),

3252-3259.

[7] Y. Ueki, T. Umemura, J. X. Li, T. Odake, and K. Tsunoda, Anal. Chem. 76,

(2004), 7007-7012.

[8] H. Yu, H. Ai, and Q. Chen, Chromatographia, 70, (2009), 1017–1022.

[9] Y. Li, B. Gu, H. D.Tolley, and M. L. Lee, J. Chromatogr. A, 1216, (2009),

5525-5532.

[10] M. Wang, J. Xu, X. Zhou, and T. Tan, J. Chromatogr. A, 1147, (2007), 24–29.

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Chapter 4

67

[11] X. Chen, H. D. Tolley, and M. L. Lee, J. Sep. Sci., 32, (2009), 2565 – 2573.

[12] B. Gu, Z. Chen, C. D. Thulin, and M. L. Lee. Anal. Chem., 78, (2006), 3509–

3518.

[13] Q. Xu, M. Mori, K. Tanaka, M. Ikedo, and W. Hu, J. Chromatogr. A, 1026,

(2004), 191–194.

[14] Z. Zhanga, F. Wanga, B. Xua, H. Qina, M. Yea, and H. Zoua, J. Chromatogr. A,

1256, (2012), 136– 143.

[15] H. Yang, Y. Chen, Y. Liu, L. Nie, and S. Yao, Electrophoresis, 34, (2013),

510-517.

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Chapter 5

68

Chapter 5

Conclusions and future perspective

5.1. Conclusions

In the present study, monolithic column stationary phases as one of the

alternative to achieve the satisfaction in analysis, simple preparation, rapid and great

separation of inorganic cations and anions have been developed. The polymeric

monolith column as well as silica organic-inorganic hybrid monolith column have been

successfully fabricated and applied to rapid analysis of the inorganic compound in the

environment.

1. The simple and rapid method with poly(ethylene glycol) monolithic column by

thermal in situ polymerization for analyzing 5 anions has been reported. The

chromatographic experiments were shown that PEG monolith can be an alternative

for short determination of anions. Introduction of PEG-groups could improve

theoretical plates of the monolith compared without any PEG-groups. The PEG

groups also have satisfaction in mechanical stability that was proved by the fact that

there is no significant swelling and shrinkage of the PEG monolith and it could be

worked on different polarities at the high flow rate. The present method allows

determination of anions contained in the seawater sample without any pretreatment

before analyzing. The bromide in seawater Padang beach and nitrate in public

drinking water in Padang City Indonesia have been determined by this method to be

44 ppm and 1.9 ppm, respectively.

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Chapter 5

69

2. An AS-hybrid monolithic capillary column with strong cation-exchange moieties

was successfully fabricated for the simultaneous separation of common inorganic

cations in ion-exchange chromatographic mode. The simple and easy preparation

with incorporation of sodium allylsulfonate into the silica monolith matrix was

carried out by single-step thermal-treatment one-pot manner. Nine common

inorganic cations (Li+, Na

+, NH4

+, K

+, Rb

+, Cs

+, Mg

2+, Ca

2+ and Sr

2+) could be

satisfactorily separated with sufficient relative standard deviations and low limits of

detection. The satisfactions of AS-hybrid monolith columns in mechanical stability

were proved by the fact that no significant swelling or shrinkage occurred in the

columns and it could also work in solutions with different polarities at high flow

rates. This method showed the elution of cations within 15 min with the pressure

drop of only ca. 0.2 MPa, which has better performance in terms of speed and the

pressure drop than the particle-packed capillary column. Based on the results in our

work and compared to other literatures, we found a novel application of an

AS-hybrid monolithic column for rapid and simultaneous determination of both

common monovalent and divalent inorganic cations in ion-exchange

chromatography mode.

3. A strong cation-exchange monolith columns were produced by single step thermal

treatment procedure involving the polymerization of 3-sulfopropyl methacrylate

potassium salt as functional monomer which introduced sulfonate groups with

ethylene dimethacrylate (EDMA). SPMP-co-EDMA monolith column has great

selectivity and strong retention for separation of monovalent cations by indirectly

detected with UV absorption at 210 nm and copper (II) sulfate as eluent. The present

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Chapter 5

70

monolithic column has great mechanical stability which could be operated at high

flow rates.

5.2. Future Perspective

With the enormous development of separation technique in analytical

chemistry, the interesting analytes can be straightly determined. Liquid chromatography

(LC) still plays an important role in offering the great results. Because the users of LC

still tend to choose the method with the higher column efficiency, rapid analysis, and

excellent selectivity, stationary phases have been developed due to offer of the

satisfaction in analyzing. It has been taken many decades with numerous efforts for the

expansion from large to smaller particle of packing material of column [1-2]. Since

appeared in the late 1980s with development of the continuous bed [3], monolithic

columns offer highly permeability and were available as one of the choice due to

achievement of the user targets.

The trend of the method with the higher column efficiency, rapid analysis, and

excellent selectivity can be achieved by availability of monolithic columns with

sophisticated property such as high porosity, great uniform skeletal structure and also

versatility for any kind of analysis. Currently, because biological samples are still a

trend to be analyzed, the monolithic columns by introducing suitable functional groups

as active sites in separation of samples are preferred. Thus, due to consideration of that

reason, polymeric monolith column can be developed and promising results were

satisfactory because it has micro-pores existing at the polymer surface which are

strongly recognized to negatively affect column efficiency and peak symmetry during

the separation of biological samples.

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Chapter 5

71

The second perspective concerns in versatility of monolithic column in ion

chromatography. The selection of appropriate system for analyzing inorganic analytes

can be worked by choosing type of detection that has a higher sensitivity. Conductivity

detector offers higher sensitivity detections. Although in certain conditions, especially

separation of anions using eluent with high background conductivity, the suppressor

column which provides cation-exchange site is required. Polymeric-based and hybrid

monolithic column contained sulfonate groups (chapter 3 and 4) can be applied for

above suppressor.

5.3. References

[1] Y. M. Li, J. L. Liao, K. Nakazato, J. Mohammad, L. Terenius, and S. Hjertén.

Anal. Biochem, 223, (1994), 153-158.

[2] L. A. Colon, J. M. Cintron, J. A. Anspach, A. M. Fermier, and K. A. Swinney,

Analysist, 129, (2004), 503-504.

[3] S. Hjertén, J. L. Liao, and R. Zhang, J. Chromatogr., 473, (1989), 273–275.

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List of figures

72

List of figures

Chapter 2

Fig. 2-1. Scanning electron microscope images of PEG-monolithic column.

Monomer:porogen=40/60 (A), 30/70 (B), 20/80 (C) and 10/90 (D).

Fig.2-2. Schematic diagram of the expected reaction for the preparation of

PEG-monolithic column.

Fig. 2-3. Separation of inorganic anions on the stationary phase with and without PEG

groups. Operating conditions: Analytes, 1 mM of each iodate (1), bromate (2),

nitrite (3), bromide (4) and nitrate (5); PEG-monolith M2 column (100 x 0.32

mm i.d.); 100 mM of sodium chloride eluent; 4 µL/min flow rate; 210 nm

wavelength of UV detection and 0.2 µL injection volume.

Fig. 2-4. Effect of modification condition for separation of inorganic anions (4 to 6 h

reaction time). Operating condition is in Figure 2-3.

Fig. 2-5. Effect of modification condition for separation of inorganic anions (7 and 8 h

reaction time). Operating condition is in Figure 2-3.

Fig. 2-6. Chromatograms of inorganic anions with various chloride eluents. Operating

conditions: Analytes, 1 mM each of iodate (1), bromate (2), nitrite (3),

bromide (4) and nitrate (5); PEG-monolith M2 column (100 x 0.32 mm i.d.);

100 mM aqueous solution of various chloride eluent, as indicated; 4 µL/min

flow rate; 210 nm wavelength of UV detection and 0.2 µL injection volume.

Fig. 2-7. Effect of potassium chloride concentration (log [KCl]) on retention (log k) of

inorganic anions. Operation conditions as in Figure 2-3.

Fig. 2-8. Back pressure of M2 as a function of flow rate of water, methanol and THF.

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73

Fig. 2-9. Separation of anions contained in seawater sample. Operating conditions as in

Figure 2-3.

Fig. 2-10. Separation of anions contained in public drinking water sample. Operating

conditions as in Figure 2-3.

Chapter 3

Fig. 3-1. Schematic of expected reaction for the preparation of AS-hybrid monolithic

column.

Fig. 3-2. The relationship of preparation time and the amount of sulfonate groups

(denoted as cation-exchange capacity) of the AS-hybrid monolith.

Fig. 3-3. Separation of inorganic cations on the AS-hybrid monolith. Operating

conditions: Analytes, 1 mM each of Li+ (1), Na

+ (2), NH4

+ (3), K

+ (4), Rb

+ (5),

Cs+ (6), Mg

2+ (7), Ca

2+ (8), and Sr

2+ (9); AS-hybrid monolith column (100 x

0.32 mm i.d.); 5 mM of CuSO4 eluent; 2 µL/min flow rate; 210 nm

wavelength of UV detection and 0.2-µL injection volume.

Fig. 3-4. Effect of copper (II) sulfate concentration (log [CuSO4]) on retention (log k) of

inorganic cations. The symbols in the figure represent as (●) Li+, (△) Na

+,

(▲) NH4+, (□) K

+, (▼) Rb

+, (■) Cs

+, (+) Mg

2+, (×) Ca

2+, (◯) Sr

2+.

Operating conditions as in Figure 3.

Fig.3-5. Separation of inorganic cations on a cation-exchange packed capillary column.

Packing material, IC cation SW (5µm) packed into 100 x 0.32 mm i.d.

Operating conditions as in Figure 3.3

Fig.3-6. Scanning Electron Microscope images of AS-hybrid monolith Magnification =

320x (A), 600x (B), and 3000x (C)

Fig.3-7. Back pressure of column B as a function of flow rate of (◇ )water,

(▲)methanol, (□)acetonitrile, and (●)THF.

Fig.3-8. Separation of cations contained in groundwater sample. Operating conditions

as in Figure 3-3.

Fig.3-9. Separation of anions contained in the effluent onsite domestic wastewater

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74

treatment system sample. Operating conditions as in Figure 3-3.

Chapter 4

Fig. 4-1. Effect of the mixture ratio of monomer and porogen of SPMP-co-EDMA

monolithic column on cation-exchange capacity. The polymerization

temperature was kept at 60 ºC.

Fig. 4-2. Effect of the mixture ratio of monomer and porogen of SPMP-co-EDMA

monolithic column on pressure drop. The column (100 x 0.32 mm i.d.), flow

rate was kept at 4 µL/min, 10 mM CuSO4 eluent.

Fig. 4-3. Effect of polymerization time of SPMP-co-EDMA monolithic column on

cation-exchange capacity. The polymerization temperature was kept at 60 ºC.

Fig. 4-4. Separation of cation on SPMP4 monolith column. Operating conditions:

Analytes, 1 mM each of NH4+, and Mg

2+. Column (100 x 0.32 mm i.d.); 5

mM of Copper (II) sulfate eluent; 4 µL/min flow rate; 210 nm wavelength of

UV detection and 0.2 µL injection volume.

Fig. 4-5. Separation of monovalent cation on SPMP4 monolith column. Analytes, 1 mM

each of Na+, NH4

+, and K

+. Operating conditions as in Figure 4-4.

Fig. 4-6. Effect of retention of inorganic monovalent cations as a function of copper (II)

sulfate concentration in the eluent. Operating conditions as in Figure 4-4.

Fig. 4-7. Separation of common cations at different flow rates of (A) 2, (B) 4, (C) 6, (D)

8, (E) 15 µL/min. Sample, 1 mM each of Na+, NH4

+ and K

+. Operating

conditions as in Figure 4-4.

Fig. 4-8. Effect of flow rate on height equivalent to a theoretical plate of K+. Operating

condition as in Figure 4-4.

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List of table

75

List of tables

Chapter 1

Table 1-1. Classification of chromatography.

Chapter 2

Table 2-1. Various polymerization conditions.

Table 2-2. Resolution of the analytes for various total monomer to porogen ratios.

Table 2-3. Relative standard deviation of retention time, peak height and peak area for

five anions under optimum operating condition as in Figure 2-3.

Chapter 3

Table 3-1. Effects of preparation parameters on the fabrication of AS-hybrid monolith

column.

Table3-2. Summarized data for the retention time (tR), relative standard deviations

(RSDs), limits of detection (LODs) of common inorganic cations. Operation

condition as in Figure 3-3.

Chapter 4

Table 4-1. Various polymerization conditions.

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List of publications

76

List of publications

1. A. Rahayu, L. W. Lim, T. Takeuchi

“Polymer monolithic methacrylate base modified with tosylated-polyethylene glycol

monomethyl ether as a stationary phase for capillary liquid chromatography”

Talanta, 134 (2015) 232-238.

2. A. Rahayu, L. W. Lim, T. Takeuchi

“Preparation of hybrid monolithic stationary phase with allylsulfonate for the rapid

and simultaneous separation of cations in capillary ion chromatography”

Journal of Separation Science, (Accepted on January 5th

, 2015)

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List of presentations

77

List of presentations

1. A. Rahayu, L. W. Lim, T. Takeuchi

“Organic-Inorganic-Silica Hybrid Monolithic Column with Allylsulfonate as Strong

Cation Exchanger for Capillary Liquid Chromatography”, the 6th

Asia-Pasific

Symposium on Ion Analysis, Padang, Indonesia, September 26-28th

2012 (Oral

Presentation).

2. A. Rahayu, L. W. Lim, T. Takeuchi

“Tosylated-polyethylene glycol monomethyl ether-bonded polymeric monolith as a

stationary phase for capillary liquid chromatography”, 日本分析化学会有機微量

分析研究懇談会創立60周年記念大会シンポジウム, Gifu, Japan, May 30-31st

2013 (Poster Presentation).

3. A. Rahayu, L. W. Lim, T. Takeuchi

“Organic-Inorganic-Silica Hybrid Monolithic Column with Allylsulfonate as Strong

Cation Exchanger for Capillary Liquid Chromatography”, the 7th

Asia-Pasific

Symposium on Ion Analysis, Jeju, South Korea, November 3-6th

2013 (Oral

Presentation)

4. A. Rahayu, L. W. Lim, T. Takeuchi

“Organic-Inorganic-Silica Hybrid Monolithic Column with Allylsulfonate as Strong

Cation Exchanger for Capillary Liquid Chromatography”, The 30th

Ion

Chromatography Symposium, TOYOTA, Japan, November 28-29th

2013 (Poster

Presentation).

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List of presentations

78

5. A. Rahayu, L. W. Lim, T. Takeuchi

“Preparation of “One-pot” Approach Silica Hybrid Monolithic Column for Ion

Exchange and Hydrophilic Interaction Capillary Liquid Chromatography”, The 21st

Chromatography Symposium, Nagoya, Japan, June 4-6th

2014 (Poster Presentation)

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Curriculum vitae

79

Curriculum vitae

Aster Rahayu

Born on July 26th

, 1986 in Bukittinggi, West Sumatera, Indonesia

Married with Joni Aldilla Fajri

Mother of Fadhlurrahman Fathih Asshiddiq

2001 – 2004 : Senior High School at SMU Negeri 3 Padang, West Sumatera,

Indonesia.

2004 – 2008 : Bachelor at Department of Chemistry, Mathematic and Natural

Science Faculty, Andalas University, Padang, Indonesia.

2009 : Research student at Graduated School of Environmental Science,

Hokkaido University, Sapporo, Japan.

2011 : Research student at Toyohide Takeuchi’s Laboratory, Faculty of

Engineering, Gifu University, Gifu, Japan.

2009 – 2011 : Master Degree at Post Graduate Program, Andalas University,

Padang, Indonesia

2012 – 2014 : Doctoral Degree at Material Engineering Division, Graduated

School of Engineering, Gifu University, Gifu, Japan.

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Acknowledgements

80

Acknowledgements

Foremost, thank and praise to God (Allah Almighty), the most merciful and

gracious, for the greatest opportunities and blessing me in my Ph.D degree.

I would like to express my sincerest gratitude and appreciate to my advisor

Professor Toyohide Takeuchi, for his greatest support, thoughtful guidance, wide

knowledge, patience, comment and understanding to me during my study. His

encouragement and precious suggestion helped me in all the time of research and

writing this dissertation.

I would like to express my heartfelt gratitude to Associate Professor Lee Wah

Lim for supportive, insightful inspirations discussions and helped me during the whole

period my study, and especially for her admirable advises and patience in all time of

research and writing this dissertation.

I would like to express my grateful and warn thanks to Professor Fuseng Li

(River Basin Research Center, Gifu University) for the kind measurements of surface

area and pores size distribution of the monoliths.

My grateful and sincere thanks to all the member of Takeuchi’ s Laboratory

for their kind support, and also providing greater atmosphere of research and study. The

deep gratitude and thanks to all friends in Indonesia Student Association of Gifu

(PPI-Gifu) for being family and the great friendship, during I stayed in Gifu.

I would like to express my warm thank and appreciate my father Yuharlis,

mother Nellita, my parents in law Nasrhul Siddiq and Nurana Khazim, my sister Suci

Nivlaharmy and sisters in law Yuri Febriani, Sri Rahmi Utami for their support and all

the respect for me during my study. My warmly and deepest thank to my beloved

husband, Joni Aldilla Fajri, for your greatest love, deep patience, excellent support, and

outstanding understanding and my little prince Fadhlurrahman Fathih Asshiddiq, for

your cheers up every single little time with your cute smile.

Japan, March 2015

Aster Rahayu