Pervaporation technology for regeneration of diethylene glycol at Russian complex gas treatment plants with the use of ceramic membranes HybSi

被引:8
作者
Akberov, Roald R. [1 ,2 ]
Fazlyev, Azat R. [2 ,3 ]
Klinov, Alexander V. [3 ]
Malygin, Alexander V. [3 ]
Farakhov, Mansur I. [2 ,3 ]
Maryakhina, Vera A. [2 ,3 ]
机构
[1] Kazan Natl Res Technol Univ, Dept Ind Safety, Kazan 420015, Russia
[2] LLC Engn Promot Ctr Inzhekhim, Kazan 420049, Russia
[3] Kazan Natl Res Technol Univ, Dept Chem Engn, Kazan 420015, Russia
关键词
Complex gas treatment plant; Russian Northern gas fields; Natural gas dehydration; DEG regeneration; Pervaporation; HybSi membrane; ETHYLENE-GLYCOL; DEHYDRATION; SEPARATION; WATER; PERFORMANCE; MIXTURES; PVA;
D O I
10.1016/j.jngse.2015.07.006
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Conventional methods of regeneration of diethylene glycol used as an absorbent for natural gas dehydration at complex gas treatment plants in the Russian gas fields are analyzed. An alternative method of regeneration by pervaporation using tubular ceramic membranes coated on the inside with the HybSi material is proposed. Experimental study of pervaporation dehydration of diethylene glycol in concentration ranges 97-99.5 wt% and 93.5-99.5 wt% corresponding to saturation levels 2.5 wt% and 6.0 wt%, respectively, is carried out in the temperature range 70-90 degrees C and vacuum pressure range 5-30 mm Hg. Increase in saturation level from 2.5 wt% to 6.0 wt% leads to inessential increase in the required surface area of HybSi membranes. Results of the experimental study are compared with experimental results obtained by other researchers for SepraTek hollow-fiber polymer membranes. Losses of diethylene glycol through HybSi membranes are shown not to exceed losses at conventional stripping and to be lower by two orders of magnitude than losses through SepraTek membranes. Use of pervaporation instead of stripping for diethylene glycol regeneration leads to more than two-fold energy saving. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:670 / 682
页数:13
相关论文
共 43 条
[1]   Dehydration of diethylene glycol by pervaporation using HybSi ceramic membranes [J].
Akberov, R. R. ;
Fazlyev, A. R. ;
Klinov, A. V. ;
Malygin, A. V. ;
Farakhov, M. I. ;
Maryakhina, V. A. ;
Kirichenko, S. M. .
THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2014, 48 (05) :650-655
[2]  
Andreev O.P., 2010, REMOVING MECH ADMIXT
[3]  
Bekirov T. M., 1999, Gas and condensate processing technology
[4]   Dehydration of ethylene glycol by pervaporation using hydrophilic IPNs of PVA, PAA and PAAM membranes [J].
Burshe, MC ;
Sawant, SB ;
Joshi, JB ;
Pangarkar, VG .
SEPARATION AND PURIFICATION TECHNOLOGY, 1998, 13 (01) :47-56
[5]   High-performance hybrid pervaporation membranes with superior hydrothermal and acid stability [J].
Castricum, Hessel L. ;
Kreiter, Robert ;
van Veen, Henk M. ;
Blank, Dave H. A. ;
Vente, Jaap F. ;
ten Elshof, Johan E. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 324 (1-2) :111-118
[6]   Chitosan coated zeolite filled regenerated cellulose membrane for dehydration of ethylene glycol/water mixtures by pervaporation [J].
Dogan, Hacer ;
Hilmioglu, Nilufer Durmaz .
DESALINATION, 2010, 258 (1-3) :120-127
[7]   Dehydration of ethylene glycol by pervaporation using poly(N,N-dimethylaminoethyl methacrylate)/polysulfone composite membranes [J].
Du, Jennifer Runhong ;
Chakma, Amit ;
Feng, X. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 64 (01) :63-70
[8]  
Dyment O.N., 1976, Glycols and other Derivatives of Ethylene and Propylene Oxides
[9]  
Elistratov A.V., 2004, THESIS
[10]   Pervaporation with chitosan membranes .1. Separation of water from ethylene glycol by a chitosan/polysulfone composite membrane [J].
Feng, XS ;
Huang, RYM .
JOURNAL OF MEMBRANE SCIENCE, 1996, 116 (01) :67-76