electrical supporting information

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Electrical Supporting information One-pot integrated biofuel production using low-cost biocompatible protic ionic liquids Jian Sun 1,2 , N.V.S.N. Murthy Konda 1,3# , Ramakrishnan Parthasarathi 1,2# , Tanmoy Dutta 1,2 , Marat Valiev 4 , Feng Xu 1,2 , Blake A. Simmons 1,3 , and Seema Singh 1,2* 1 Deconstruction Division, Joint BioEnergy Institute, Emeryville, CA, USA. 2 Biomass Science and Conversion Technology Department, Sandia National Laboratories, Livermore, CA, USA. 3 Biological Systems and Engineering Division, Lawrence Berkeley National Laboratory, Berkeley, CA, USA. 4 Environmental Molecular Sciences Laboratory, Pacific Northwest National Laboratory, Richland, WA, USA. *Corresponding author: E-mail: [email protected] # Equal contribution as the co-second author 1 Electronic Supplementary Material (ESI) for Green Chemistry. This journal is © The Royal Society of Chemistry 2017

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Page 1: Electrical Supporting information

Electrical Supporting information

One-pot integrated biofuel production using low-cost

biocompatible protic ionic liquids

Jian Sun1,2, N.V.S.N. Murthy Konda1,3#, Ramakrishnan Parthasarathi1,2#, Tanmoy Dutta1,2,

Marat Valiev4, Feng Xu1,2, Blake A. Simmons1,3, and Seema Singh1,2*

1 Deconstruction Division, Joint BioEnergy Institute, Emeryville, CA, USA.2 Biomass Science and Conversion Technology Department, Sandia National Laboratories,

Livermore, CA, USA.3 Biological Systems and Engineering Division, Lawrence Berkeley National Laboratory,

Berkeley, CA, USA.4 Environmental Molecular Sciences Laboratory, Pacific Northwest National Laboratory,

Richland, WA, USA.

*Corresponding author: E-mail: [email protected]# Equal contribution as the co-second author

1

Electronic Supplementary Material (ESI) for Green Chemistry.This journal is © The Royal Society of Chemistry 2017

Page 2: Electrical Supporting information

Table S1. Compositional analysis of major components in the switchgrass before and

after pretreated and solid recovered after pretreatment.[a]

Solvent Solid recovery/% Glucan/% Xylan/% Lignin/%

/ / 32.9±0.1 20.4±0.1 22.2±0.1

HOAC 79.5 37.9±0.1 15.5±0.2 25.5±0.5

EOA 59.0 53.1±0.1 22.4±0.2 5.7±0.3[a] Method is described in the main text.

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Page 3: Electrical Supporting information

Computational details for IL Screening

The geometry optimizations of ethanolamine (EOA), diethanolamine (DEOA), triethanolamine (TEOA), and triethylamine (TEA), with acetic acid, lactic acid, sulfuric acid, formic acid and hydrochloric acid (Fig. 2), were performed using density functional theory (DFT) with the M06-2X hybrid exchange-correlation functional and the 6-311++G(d, p) basis set. Frequency calculations were carried out to verify that the computed structures corresponded to energy minima. In the present study, density functional theory (DFT) based global reactivity descriptors, such as chemical hardness, chemical potential, and electrophilicity were calculated. Quantum chemical reactivity descriptors predicted acidity, basicity and net basicity, and showed good correlation with experimentally observed values for [C2C1Im][OAc]. These results provide a basis to describe the observed experimental delignification trend for a set of ILs. These descriptors were used to derive the molecular basicity, acidity, and net basicity values for the novel ILs. According to the DFT, the chemical potential (), and chemical hardness () are defined as,

and )(2

1)(2

12

2

rvNrvNE rr

(2)

where E is the total energy of the system, N is the number of electrons in the system and is the external potential. is identified as the negative of the electronegativity ( ). )(rv r

By applying finite difference approximation to Eqs. (2) and (3) we get the operational definition for and as,

2)( EAIP (3)

2EAIP (4)

Chemical potential and chemical hardness can be rewritten using Koopmans’ theorem in terms of the vertical ionization potential (IP) and electron affinity (EA) as,

2HOMOLUMO EE (5)

2HOMOLUMO EE (6)

3

)(rvNE r (1)

Page 4: Electrical Supporting information

where ELUMO is the lowest unoccupied molecular orbital’s energy and EHOMO is the highest occupied molecular orbital’s energy. Upon formation of a hydrogen bond, electron density is transferred from the hydrogen bond acceptor towards the hydrogen bond donor. In the light of Hard Soft Acids Base (HSAB) concept the propensity of molecule to donate the electron density depends inversely on the electronegativity and hydrogen atom-attracting sites are formed through the interaction of intramolecular sites of different electronegativity. Hence, we define the hydrogen bonding basicity BIL of an IL using simple working equation based on DFT based descriptors as follows

BIL =2 (7)An increased electrostatic component and the high electronegativity of a molecule influence the hydrogen bonding ability. In the case of basicity, electronegativity is very important for hydrogen bonding. Therefore, molecular acidity dependence on the reduced orbital electronegativity of the molecule is considered. The formula for the acidity is written as follows

AIL =22 (8)IL net basicity values were reported as a difference in BIL - AIL. All quantum chemical calculations were performed using the Gaussian 09 suite of programs.

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Page 5: Electrical Supporting information

[EOA][OAc] [DEOA][OAc] [TEOA][OAc]

[EOA]Cl [EOA][HSO4] [EOA][La]

[EOA]F [DEOA]F [TEOA]F

[TEA][HSO4] [C2C1Im][OAc] [Ch][OAc]

Figure S1. Optimized geometries of ILs screened in this study.

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Page 6: Electrical Supporting information

NMR OF ILS SYNTHESIZED, 1HNMR (UP) AND 13CNMR (BOTTOM)

Figure S2. 1HNMR and 13CNMR spectrums of [EOA][OAc]

6

~ ~

*

*

NH3HO

O

O

1

1

1

2 3

2 3

3

2

4

4

5

5

δ (ppm)

δ (ppm)

Page 7: Electrical Supporting information

H3N H O

OOH

1 1

2 2 3

3

4 4 5

~ ~

1 2

5

*

*

Figure S3. 1HNMR and 13CNMR spectrums of [EOA]F

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Page 8: Electrical Supporting information

*

1

2 3 1 2

3

NH3HO

Cl

*

1 2

Figure S4. 1HNMR and 13CNMR spectrums of [EOA]Cl

8

Page 9: Electrical Supporting information

*

1

3

2 4 51

23

4

~~*

1

23

5

Figure S5. 1HNMR and 13CNMR spectrums of [DEOA][OAc]

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Page 10: Electrical Supporting information

NH2HO

OH

H O

O

3 2 4

1

5

1 2

4 3 *

*

1 2 5

Figure S6. 1HNMR and 13CNMR spectrums of [DEOA]F

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Page 11: Electrical Supporting information

NH

HSO4

1

2

1

2

*

*

Figure S7. 1HNMR and 13CNMR spectrums of [TEA][HSO4]

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Page 12: Electrical Supporting information

NH

O

O1

1

2 2

3

3 4

4

~ ~

*

*

Figure S8. 1HNMR and 13CNMR spectrums of [TEA][OAc]

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Page 13: Electrical Supporting information

1 2

3

NH

H O

O

HO

OH

OH

1

2 3

4

4

*

* 1

2

5

5

Figure S9. 1HNMR and 13CNMR spectrums of [TEOA]F

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Page 14: Electrical Supporting information

H2N

OHH

OH

O

O

*

1 1

2

3 4

2 3

4 5

5 6

*

1 2 3 4 6

Figure S10. 1HNMR and 13CNMR spectrums of [EOA][La]

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Page 15: Electrical Supporting information

*

*

NOH

HO

HO

H

O

O1

1 5

2 3

4

2 3

1

2 3

5

Figure S11. 1HNMR and 13CNMR spectrums of [TEOA][OAc]

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Page 16: Electrical Supporting information

Figure S12. SEC chromatograms of extracted lignin streams from switchgrass

pretreatment with (a) [EOA]-based; (b) [OAc]-based; (c) [HSO4]-based; (d) [F]-based ILs

along with EMAL lignin for comparison.

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7 9 11 13 15 17 19 21 23 25

[EOA][OAc]

[EOA][HSO4]

[EOA][F]

[EOA][La]

[EOA][Cl]

[EOA][H2PO4]

EMAL

A

Retention time (min)

Inte

nsity

(a.u

)

7 9 11 13 15 17 19 21 23 25

[EOA][OAc]

[DEOA][OAc]

[C2C1Im][OAc]

[TEOA][OAc]

[Ch][OAc]

EMAL

Inte

nsity

(a.u

)

Retention time (min)

B

7 9 11 13 15 17 19 21 23 25

EMAL

[TEA][HSO4]

[EOA][HSO4]

Retention time (min)

Inte

nsity

(a.u

)

C

7 9 11 13 15 17 19 21 23 25

EMAL

[TEOA][F]

[DEOA][F]

[EOA][F]

Retention time (min)

Inte

nsity

(a.u

)

D

Page 17: Electrical Supporting information

Biomass

Pretreat

ILrecycle

Enzyme

SSF Pre-Hydrolysis

Pervapora on

S/L separa on (Centrifuga on)

Ethanol

Water (to WWT)

Ultrafiltra on Solids (to boiler)

Solids (to boiler)

Dis lla on

Conentra on (mul -effect evaporator)

Water (recycle)

ILmake-up

Figure S13. A simplified representation of the PIL based biorefinery process.

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Page 18: Electrical Supporting information

Table S2. Key process and cost parameters in the scenarios studied.

Scenario S0 S1 S2 S3

Switchgrass processed (dry MT/day) 2000 2000 2000 2000

Feedstock price ($/dry ton, delivered at plant-gate) 80 80 80 80

Pretreatment

Pure IL price ($/kg)* 2 2 2 2

IL purity (wt% in H2O) ~100 ~100 ~25 ~25

Biomass loading (wt%) 40 40 20 20

IL recovery (%) 99 99 99 99

SSF

Enzyme loading (mg/g biomass) 20 20 20 7

Enzyme price ($/kg protein)** 5 5 5 5

IL concentration during SSF (wt%) 5 20 20 20

Pre-hydrolysis time (hr) 24 24 24 24

SSF time (hr) 72 72 72 72

Co-utilization of glucose and xylose Yes Yes Yes Yes

Overall ethanol yield (gal/dry ton switchgrass) 72 72 72 72

* Price of ILs is assumed to reflect on the fact that the hydroxyl ammonium based ILs such as [EOA][OAc] use cheaper raw materials and require simpler synthesis methods. For instance, according to the information available in the open literature (e.g., www.alibaba.com), ethanolamine and acetic acid (i.e., the primary raw materials used to synthesize [EOA][OAc]) can be purchased for about $800-$1500/MT and $300-$700/MT (depending on the supplier, quality and order quantity). Therefore, a price of $2/kg of [EOA][OAc] is a reasonable estimate in this preliminary TEA. ** The enzyme was estimated based on a design report from NREL (Humbird et al., 2011, see Ref. 46). The effective enzyme price obtained based on this report was ~ $4.3/kg which was reported in 2007$. Since our analysis is based on more recent year (2015), we estimated the enzyme price to be $5/kg with an average inflation rate of around 2%.

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