selecting pour depressants for diesel fuels
TRANSCRIPT
309
____________________________________________________________________________________________________
Shanghai Institute of Technology; Research China Shenhua Coal to Liquid and Chemical Shanghai Research
Institute. Dalian Polytechnic University, Shanghai Hiri Lubricants R&D Centre, PR of China. Translated from
Khimiya i Tekhnologiya Topliv i Masel, No. 5, pp. 18 – 24, September – October , 2010.
0009-3092/10/4605–0309 © 2010 Springer Science+Business Media, Inc.
Chemistry and Technology of Fuels and Oils, Vol. 46, No.5, 2010
SELECTING POUR DEPRESSANTS FOR DIESEL FUELS
Sheng Han, Kui Zeng, Hualin Lin, and Peng Wang
The correlation between effectiveness and composition was investigated to choose the most effective
pour depressant from the multitude on the market. Samples of pour depressants from the main
manufacturers were collected and their ability to improve the low-temperature properties of diesel fuels
was evaluated. The composition and structure of the additives with the best results and their solvents
after separation by crystallization were investigated by Fourier-transform infrared spectroscopy, proton
nuclear magnetic resonance spectroscopy, and chromatography-mass spectrometry. It was shown that
copolymers of ethylene and vinyl acetate are the most effective pour depressant additives. Their solvents
contain aromatic compounds.
The pour depressants added to diesel fuel to improve its low-temperature properties modify crystallization
of waxes [1-5]. They basically contain polymers [6-14] such as copolymers of ethylene and vinyl acetate, polyalkyl
methacrylate, maleic anhydride, alkylnaphthalenes, nitrogen-containing, and other polymers. These compounds
are usually soluble in crude oil and have very complex compositions [15, 16].
Diesel fuel, with additive Decrease, deg
LFT ts
A-1 10 25
Haote 11 25
KT8804 13 27
T803 3 18
V-385 3 20
10-320 1 13
10-330 2 22
ACLUBE148 2 14
ACLUBE134 3 20
CS 8 21
Table 1
310
The manufacturers of pour depressants market them under different trade marks without revealing the
composition. For this reason, the assortment of products of similar composition on the market is very wide.
However, there are few effective additives among them [17], which makes it difficult for the consumer to select
them since selection should be based on a significant number of screening experiments, and this will result in
losses of time, feedstock, and consequently increased costs.
The composition of the basic pour depressants must be characterized for selecting the best products.
Pour depressants f rom the fo l lowing manufac turers were se lec ted for the s tudy: Haote (Bei j ing
Haote), A-1 (Tianyu Petroleum Additives), KT8804 (Shanghai Boda Chemical), CS (Jinan Three Metallurgical
Fig. 1. IR spectra of pour depressants: a) A-1; b) Haote; c) KT8804.
Wavenumber, cm-1
Tran
smis
sion
, % b
a
c
311
Table 2Pe
ak n
umbe
r in
sp
ectr
um
(s
ee F
ig. 3
c)
Ret
entio
n tim
e,
min
Component Structural formula
Accuracy, %
Are
a of
pea
k, %
1 2 3 4 5 6
1 9.96 1-Methyl-2-ethylbenzene
95 1.24
2 10.46 1,4-Dimethyl-2-ethylbenzene
94 1.35
3 10.90 1,2,4,5-Tetramethylbenzene
91 2.20
4 11.03 1,3-Dimethyl-2-ethylbenzene 87 3.40
5 11.28 4,7-Methanoindene
98 9.87
6 11.36 Undecane 87 2.42
7 11.65 1,2,3,4-Tetramethylbenzene 97 4.41
8 11.71 1,2,3,5-tetramethylbenzene
97 4.78
9 12.13 Indene
94 2.14
10 12.24 1-Methyl-4-isopropylbenzene
91 3.18
11 1..51 1-Methyl-4-propylbenzene
95 9.66
12 12.60 Ethylcyclohexane
89 4.01
13 12.93 Naphthalene
93 7.77
14 13.16 Dodecane
97 4.20
312
Table 2 (continued)
Fig. 2. 1H NMR spectra of pour depressants: a) A-1; b) Haote; c) KT8804.
δ, ppm
1 2 3 4 5 6
15 13.36 6-Methyldodecane
94 2.75
16 14.30 2,6-Dimethyloctadecane 90 2.77
17 14.76 1-Methylnaphthalene 91 2.88
18 14.99 2-Methylnaphthalene 90 1.01
19 15.60 1,2,3,4-Tetrahydronaphthalene
95 0.71
20 16.02 1,4-Dimethylnaphthalene
98 0.65
313
Fig. 3. Results of chromatography-mass spectrometry of solvents in additives; a) A-1;
b) Haote; c) KT8804.
Time, min-1
a
b
c
314
Table 3P
eak
num
ber
in
spec
trum
(see
Fig
. 3c)
Ret
entio
n ti
me,
m
in
Component Structural formula
Accuracy, %
Are
a of
pea
k, %
1 2 3 4 5 6
1 6.58 Nonane 95 1.04
2 7.58 3-Methylnonane 90 1.97
3 8.83 1-Methyl-2-propylcyclohexane 92 2.89
4 9.06 1,2,4-Trimethylbenzene 91 4.98
5 9.25 Decane 91 3.79
6 9.66 1,2,3-Trimethylbenzene 98 4.66
7 9.95 Propylbenzene 90 2.82
8 10.26 1,4-Diethylbenzene 90 2.00
9 10.49 1-Ethyl-3,5-dimethylbenzene 94 4.06
11 10.77 3-Methyldecane 93 2.15
11 10.85 1,2-Dimethyl-4-ethylbenzene
95 3.49
12 10.90 1-Ethyl-2,4-dimethylbenzene
94 4.27
13 11.03 2-Ethyl-1,4-dimethylbenzene
97 7.38
14 11.38 Undecane
90 8.05
315
Chemical), V-385 (Xian Qichuang Chemical), 10-320 and 10-330 (Rohmax), ACLUBE148 and ACLUBE134 (Sanyo
Chemical Industries, Japan). The efficacy of these additives was assessed by the improvement in the
low-temperature properties of diesel fuel No. 0 supplied by Lanzhou Petroleum Refining Co.
Most pour depressants are viscous polymers, so that a solvent is added to them to increase solubility in
petroleum products. The solvent must be separated to analyze the additive. Separation is conducted by
crystallization, which is based on the different solubility of the components at different temperatures and
precipitation of the additive at low temperatures. The necessary amount of additive in the solvent was cooled in
a SYP1022-2 ins t rument . When the t empera ture became lower than the l imi t ing f i l t e rab i l i ty
temperature (3°C), the additive begin to precipitate into sediment. The supernatant liquid was collected as the
solvent.
The compos i t ion and s t ruc ture o f the add i t ives were de te rmined by Four ie r- t rans form
infrared (IR) spectroscopy and proton nuclear magnetic resonance spectroscopy (1H NMR). A small amount of
the polymer granulated with KBr was analyzed in an American Nicolet IR 100/200 IR spectrometer, and
a smal l amount o f po lymer d i sso lved in deu te ra ted ch loroform (CDCl3) was ana lyzed in
a Varian VNS-400 NMR spectrometer.
The composition of the solvents separated from the additives was determined by chromatography–mass
spectrometry. An Agilent 5975 GC-MS with a HP-5 capillary column (30 m × 0.32 mm × 0.5 μm) was used for
the analysis. The analysis was conducted in the following conditions: the temperature in the column was increased
from 40 to 280°C at the rate of 10°/min, the interface temperature was 280°C, the injector temperature
was 300°C, and the sample volume was 0.1 μl.
The viscosity at low temperatures, solid point, and limiting filterability temperature (LFT) of diesel fuel
with additives in the concentration of 1000 ppm were determined on a Shanghai Boli SYP1022-2 multifunctional
instrument [17, 18]. The results of determination of the solid point ts and LFT are reported in Table 1.
T803, ACLUBE148, ACLUBE134, V-385, 10-320, and 10-330 pour depressants decreased the solid point
by 13-22°, but the decrease in the LTF was a total of 1-3°. With A-1, Haote, KT8804, and CS additives, both the
Table 3 (continued)
1 2 3 4 5 6
15 11.66 1,2,4,5-tetramethylbenzene
97 6.96
16 11.73 1-Methyl-4-isopropylbenzene
87 6.62
17 12.08 2,3-Dihydro-5-methylindene
89 2.11
18 12.23 1-Methylindene
95 1.87
19 12.29 1,2,3,5-Tetramethylbenzene
91 2.74
20 12.92 Naphthalene
94 3.60
316
Pea
k nu
mbe
r in
sp
ectr
um (
see
Fig
. 3c
)
Ret
enti
on ti
me,
m
in
Component Structural formula
Accuracy, %
Are
a of
pea
k, %
1 2 3 4 5 6
1 9.66 Toluene
89 0.56
2 9.98 1-Methyl-2-ethylbenzene
90 4.32
3 10.26 1,3-Dimethylbenzene
91 1.19
4 10.34 1-Methyl-2-propylbenzene
92 0.97
5 10.45 1,2,3-Trimethylbenzene
86 2.99
6 10.86 3-Ethyl-1,3-dimethylbenzene
95 0.87
7 11.08 4-Ethylstyrene
90 4.07
8 11.35 4,7-Methanoindene
96 19.56
9 11.69 Dodecane
90 2.28
10 12.05 2,3-Dihydro-4-methylindene
95 3.45
11 12.12 2,4-Dimethylstyrene
93 8.14
12 12.27 2-Ethyl-1,3-dimethylbenzene
94 6.13
13 12.59 1,2,3,4-Tetrahydronaphthalene
89 17.73
14 12.96 Naphthalene
97 7.02
Table 4
317
solid point and the LFT of the diesel fuel decreased. Most of the additives thus decreased the solid point with a
comparatively small decrease in the LFT.
The three most effective pour depressants were selected for further investigation based on the results of
the tests: A-1, Haote, and KT8804. Their IR spectra are shown in Fig. 1a-c. The IR spectra of the additives are
very similar. The absorption bands in the 2948 and 2830 cm-1 regions correspond to stretching vibrations of
methylene and methyl groups, and the absorption bands in the 1738 and 1457 cm-1 regions correspond to stretching
vibrations of C=O and C–O groups. The absorption bands in the 1241 cm-1 region correspond to deformation
vibrations of the methylene group, while the bands in the 1036 cm-1 region correspond to stretching vibrations of
the O–C=O group. The absolution band in the 733 cm-1 region indicate rocking vibrations of (CH2)
n groups
for n > 4. The analysis of these spectra showed their similarity to the spectra of the copolymer of ethylene and
vinyl acetate. As a consequence, these pour depressants can be assigned to additives of this type.
The 1H NMR spectra of additives A-1, Haote, and KT8804PPD are shown in Fig. 2a-c. The peak in
the 0.89 ppm region indicates the presence of a CH3 group in a long hydrocarbon chain [14]. The peak
at 1.25 ppm relates to protons in the long –(CH2)
n– chain and the peak at 1.50 ppm belongs to a methylene group
bound with CH2O–. The peak at 2.04 ppm characterizes the CH
2O– group, and the one at 4.87 ppm characterizes
a –CH2OCO– group. The results obtained also confirm that these additives are the copolymer of ethylene and
vinyl acetate. However, the structure and composition of the copolymer in the investigated samples differ.
As noted previously, the additives consist of polymers and solvents. The latter affect the efficacy of the
our depressants differently, so that it was necessary to analyze the composition of the solvents. The solvents
separated from A-1, Haote, and KT8804 additives were analyzed by gas chromatography–mass spectrometry.
The spectra obtained are shown in Fig. 3a-c, and the results of their analysis are reported in Tables 2-4.
As Tables 2 and 3 show, derivatives of benzene, cyclohexane, naphthalene, indene, and paraffins with
long hydrocarbon chains are the basic components of the solvents in A-1 and KT8804.
Table 4 (continued)
1 2 3 4 5 6
15 13.33 Cyclohexane
86 1.64
16 13.85 Tetradecane
93 1.22
17 14.05 Phenol
87 1.04
18 14.26 Propylcyclohexane
83 0.56
19 15.95 3,4-Dihydronaphthalene
97 0.64
20 15.95 1-Methylnaphthalene
97 0.64
x
318
The basic components of the solvent in the Haote additive (see Table 4) include derivatives of benzene,
naphthalene, indene, and long-chain paraffins. The basic components of the solvents in the A-1 and Haote additives
are aromatic hydrocarbons (approximately 58%) and long-chain paraffins (approximately 17%).
In view of the earlier studies in [20] which showed the similarity of this composition to the composition
of the naphtha cut, we can conclude that the naphtha cut is the solvent in pour depressants A-1 and Haote.
The solvent in additive KT8804 primarily consists of aromatic hydrocarbons (of the order of 80%), and
the content of paraffins is only 3.5%. Based on the previous studies [21], we can thus conclude that aromatic
petroleum oil is the solvent in this additive. Since the aromatic hydrocarbon content in all three solvents is
significant, we can conclude that aromatic solvents cause both the good solubility and dispersion of the additive
and consequently increase its efficacy in improving the low-temperature properties.
The research was conducted with the support of Shanghai Leading Academic Discipline Project (Project
No. J51503), National Natural Science Foundation of China (Project No. 20976105), Science and Technology
Commission of Shanghai Municipality (Project No. 09QT1400600), and Innovation Program of Shanghai
Municipal Education Commission (Project No. 09YZ387).
REFERENCES
1. US Patent No. 2001/0034410A1 (2001).
2. A. Jukic, M. Rogosic, and Z. Janovic, Eur. Polym. J., No. 42, 1105-1112 (2006).
3. Yang Xin-hua and Jie Cheng-xi, Study on the Synthesis and Properties of Copolymers as Low-temperature
Flow Improvers [D], Xinjing University, Xinjing (2006).
4. J. A. Coutinho, C. Dauphin, and J. L. Daridon, Fuel, No. 79, 607-616 (2000).
5. Huang Ying-xiong, Shandong Chem. Ind., No. 37, 20-22 (2008).
6. US Patent No. 6017370 (2000).
7. W. H. Chen, X. D. Zhang, Z. C. Zhao, et al., Fluid Phase Equil., No. 280, 9-15 (2009).
8. Wu Chuanjie, Zhang Jinli, Want Yiping, et al., Fuel Proc. Technol., No. 87, 585-590 (2006).
9. Rafael A. Soldi, Angelo R. S. Oliveira, Ronilson V. Barbosa, et al., Eur. Polym. J., No. 43, 3671-3678
(2007).
10. Sheng Han, Yuping Song, and Tianhui Ren, Energy Fuels, No. 23, 2576-2580 (2009).
11. US Patent 6017370 (2000).
12. A. L. C. Machado, E. F. Lucas, et al., J. Petrol. Sci. Eng., No. 32, 159-165 (2001).
13. Y. P. Song, T. H. Ren, X. S. Fu, et al., Fuel Proc. Technol., No. 86, 641-650 (2005).
14. J. X. Li, N. N. Xu, and G. D. Yin, Anal. Chim. Acta, No. 373, 73-81 (1998).
15. Xi Xiao-li, Qi Pan-lun, and Wang Xi, Petrochem. Technology & Application, 26, No. 3, 250-253 (2008).
16. K. S. Pedersen and H. P. Ronningsen, Energy Fuels, No. 17, 321-328 (2003).
17. M. Kan, M. Djabourov, J. L. Volle, et al., Fuel, No. 82, 127-135 (2003).
18. Cai Zhi, Huang Wei-qiu, and Li Wei-ming, Oil Blending Technology [M], China Petrochemical Press,
Beijing (2005), pp. 20-23.
19. Zhang Jin-li, Wu Chuanjie, Li Wei, et al., Fuel, No. 82, 1419-1426 (2003).
20. Yan Jian-hua, Gao Ya-li, and Chi Yong, J. Fuel Chem. Technol., 32, No. 2, 165-170 (2004).
21. Zhang Hong-xi, Xie Chen-xi, and Chen Zhao-hui, J. Xinjiang Univ. (Natural Science Edition), 21, No. 3,
282-284 (2004).