Document kDR75a3VbExRVwrp0xmJyj9pn
Synthesis of dipropylene glycol: Optimization of operating condition through a statistical
technique
Liang Lu Yuzhi Xiang Daohong Xia Yulu Zhou
College of Chemistry and Chemical Engineering, China University of Petroleum, Dong Ying, 266555, China
Introduction
The dipropylene glycol (DPG) is one kind of fine chemicals that was used to synthesize the plasticizers dipropylene glycol dibenzoate (DPGDB) [1] and widely used as solvent due to its ether bond and hydroxyl group, respectively [2]. Moreover, it is a component of many widely used commercial products such as antifreeze, air fresheners, cosmetic products, chemical intermediates and plastics [3].
The mostly convenient and industrial feasible method for synthesis DPG is through the reaction called O-alkylation [4] of propylene oxide (PO) with 1, 2-propanediol (1, 2-PDO) over catalysts [5, 6]. Unfortunately, the main source of DPG is as the by-product in the process of producing 1, 2-PDO, and few studies have reported about the synthesis of DPG.
In this paper, a secondary amine [3] was selected as the catalyst for the synthesis of DPG and the effects of five operating parameters (reaction time, pressure, temperature, mol ratio of material and the amount of catalysts) were studied using orthogonal design experiment to find the optimal condition.
Experimental
Materials and Apparatus
1,2-propanediol, propylene oxide and organic amine, analytical grade pure, purchased from Shanghai chemical regents company, were dried by magnesium sulfate before use.
High pressure kettle and temperature controller were used in the process. The qualitative analysis and quantitative analysis were carried out by Agilent 6820 gas chromatograph.
Orthogonal experiment
Based on our previous work, an orthogonal array experiment with variation of five experimental parameters is constructed without considering their mutual interactions. Each parameter has four selected levels and the level covered a broad range (Table 1). In Table 1, A, B, C , D, E indicate the Reaction Temperature (K), the Reaction Pressure (gauge pressure/ atm), the Reaction Time (min), the Mol ratio of
material (n mol = NPDO / NPO), and the Amount of Catalysts (n' mol=N Cat /N PO), respectively.
Table 1 Experimental variables: factors and levels
Level
Factors
A:T(K)
B:
C:
D:
E:
Pressure Time Material Catalysts
(atm) (min) ratio
dose
(n mol)
(n' mol)
1 330
1.0 50 2.0
0.01
2 350
2.0 70 1.5
0.04
3 370
3.0 90 1.0
0.07
4 370
4.0 110 0.5
0.10
Table 2 Design matrix and measured response of each
designed experiment
Run no.
A
B
C
D
E
Yield Selectivity (%) (%)
1 1 1 1 1 1 1.58 70.16
2 1 2 2 2 2 2.57 80.11
3 1 3 3 3 3 2.51 82.40
4 1 4 4 4 4 9.63 86.03
5 2 1 2 3 4 23.16 85.93
6 2 2 1 4 3 16.66 86.32
7 2 3 4 1 2 19.84 85.53
8 2 4 3 2 1 7.13 84.05
9 3 1 3 4 2 33.85 86.59
10 3 2 4 3 1 4.85 84.92
11 3 3 1 2 4 32.26 85.75
12 3 4 2 1 3 37.66 85.82
13 4 1 4 2 3 33.17 85.64
14 4 2 3 1 4 35.97 85.42
15 4 3 2 4 1 15.13 84.34
16 4 4 1 3 2 21.20 84.89
Results and Discussion
Analysis of experimental data
Each variable (each factor) was tested at four levels and the level covered a broad range (Table 1). The factorial design led to a total of 16 experimental runs listed in Table 2, which comprised of five columns and sixteen rows constructed. From the Analysis of Range (Table 3), we can get the information as followings: 1) the order of the factor's effect on DPG yield and selectivity were A> E> D> B> C and A >E >D > C> B, respectively. 2) the optimal levels of design parameters about DPG yield and selectivity were A3, B4, C3, D1, E4 and A3, B4, C4, D4, E4, respectively.
Prepr. Pap.-Am. Chem. Soc., Div. Petr. Chem. 2009, 54 (1), 39
Table 3 Results of the DPG Range Analysis Yield (%)
ABCDE
K 1
4.072
12.940 17.925 23.762
7.173
K 2
16.697
15.012
19.630
18.782
19.365
K 3
27.155
17.435
19.865
12.930
22.500
K 4
26.367
18.905
16.873
12.817
25.255
R 23.083 7.928 2.992 10.832 18.082
Selectivity (%)
ABCDE
K 1
79.675
82.080
81.780
81.733
80.868
K 2
85.457
84.193
84.050
83.888
84.280
K 3
85.770
84.505
84.615
84.535
85.045
K 4
85.073
85.197
85.530
85.820
85.783
R 6.095 3.117 3.750 4.087 4.915
Analysis of variance
The test result difference caused by the changes of factor levels or by the mutual interactions and the erroneous fluctuation can't be separated out by range analysis, through the analysis of variance, from it the information about which process parameter is statistically significant can be got, was introduced.
Table 4 The results of Variance Analysis about DPG yield
Symbol
Paramete
r
SS
d. f.
F0.05 (3, 3)
Signi FI f-
icant
A
T (K)
1392.748
3
57.099 9.280
*
B
P (atm)
132.612
3
5.437 9.280
C
Time (min)
24.392
3 1.000 9.280
Mate
D -rial 235.512 3 9.655 9.280 *
ratio
Catal
E -ysts 762.676 3 31.267 9.280 *
dose
Error
24.39
3
Table 5 The results of Variance Analysis about DPG
selectivity
Symbol
Paramete
r
SS
d. f.
F0.05 (3,3)
Signi FI f-
icant
A
T ( 100. ) 452
3
4.640
9.28 0
B
P 21.6 (atm) 49
3
1.000
9.28 0
C
Time 30.5 (min) 99
3
1.413
9.28 0
D
Mate -rial ratio
35.0 11
3
1.617
9.28 0
E
Catal -ysts dose
56.6 41
3
2.616
9.28 0
Error
21.6 5
3
Conclusion
From the laboratory scale production, the factors on the synthesis of the DPG were studied using the orthogonal experiment design and some conclusions can be drawn as following: 1. The optimal condition for the synthesis of dipropylene
glycol is: 370K, 1atm, 90min, 1:1 mol ratio of PDO to PO, addition 0.06 mol catalyst to PO. 2. The order of importance for the several factors studied on dipropylene glycol yield and selectivity are T (K)> n'cat > nmol > P (atm)> T (min) and T (K) > n'cat > nmol > T (min)> P(atm), respectively. 3. The parameters that reaction temperature, mol ratio of material and the amount of catalysts gave more significant on dipropylene glycol yield, and all parameters had in significant effect on dipropylene glycol selectivity.
Reference
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(2) Opdyke, D.L. (1978). Fragrance rawmaterials monographs: Dipropylene Glycol, Food Cosmet Toxicol, 16, 729730.
(3) Staples, C. A. Davis, J. W. (2002). An examination of the physical properties, fate, ecotoxicity and potential environmental risks for a series of propylene glycol ethers, Chemosphere, 49, 61-73.
(4) Zhou, Q. F. Ma, H. Z. Wang, B. Fan, F. (2007). Degradation of methylene blue: Optimization of operating condition through a statistical technique and environmental estimate of the treated wastewater. J. Hazard. Mater, 153,44-51.
(5) Zhang, X. H. Zhang, W. Y. Li, J. P. Zhao, N. Wei, W. Sun, Y. H. (2007). Synthesis of propylene glycol methyl ether over amine modified porous silica by ultrasonic technique, Catal. Commun., 8, 437-441.
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(6) SEXTON, A.R. BRITTON, E.C. (1953). Synthesis and Identification of Dipropylene Glycol Isomers, Org. Syntheses, 4357-4358.
Prepr. Pap.-Am. Chem. Soc., Div. Petr. Chem. 2009, 54 (1), 41