Comparison study of activators performance for MDEA solution of acid gases capturing from natural gas: Simulation-based on a real plant

被引:37
作者
Abd, Ammar Ali [1 ,2 ]
Naji, Samah Zaki [2 ,3 ]
机构
[1] Al Qasim Green Univ, Water Resources Engn Coll, Babylon, Iraq
[2] Curtin Univ, Chem Engn Dept, Perth, WA, Australia
[3] Kerbala Univ, Petr Engn Dept, Kerbala, Iraq
关键词
CO2; H2S; Piperazine; Sulfolane; Active-methyldiethanolamine; Energy consumption; CARBON-DIOXIDE; N-METHYLDIETHANOLAMINE; SENSITIVITY-ANALYSIS; AQUEOUS-SOLUTION; CO2; CAPTURE; PLUS PIPERAZINE; SOLUBILITY; ABSORPTION; SULFOLANE; REMOVAL;
D O I
10.1016/j.eti.2019.100562
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Energy requirements and environmental regulations are the main limiting issues behind the continuous developments of amine absorption processes. Steady state simulation has been performed using the Aspen HYSYS program version 8.8 to determine the effects of adding various concentrations of activators up to 10% with maintaining the constancy of the entire amine strength of 45%. The present investigation addresses the performance of using piperazine/MDEA and sulfolane/MDEA on the absorption process in terms of energy consumption and acid gases loading. Four scenarios have been analyzed under the same operating conditions, 5% activator/ 40% MDEA has shown better performance superior to other scenarios regarding the balance between energy consumption and absorption capacity of acid gases. The results revealed that the addition of 5% piperazine improves the absorption of CO2 and H2S by 92.1% and 28.2% respectively. Correspondingly, 5% sulfolane enhances the absorption efficiency of CO2 and H2S by 80.48% and 48.18%. In terms of energy, the sulfolane system saved more reboiler energy compared to the piperazine system. Reboiler energy consumption was investigated by changing some effective parameters, namely sour gas temperature, lean amine temperature, reflux ratio, and rich amine temperature. Sulfolane promoter is more applicable for the study plant conditions due to its high absorption capacity for H2S and low reboiler duty requirements. (C) 2019 Elsevier B.V. All rights reserved.
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页数:11
相关论文
共 33 条
[1]   Comparison of amine solutions performance for gas sweetening [J].
Abkhiz, Vahid ;
Heydari, Isa .
ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2014, 9 (05) :656-662
[2]   Optimization and performance improvement of Lekhwair natural gas sweetening plant using Aspen HYSYS [J].
Al-Lagtah, Nasir M. A. ;
Al-Habsi, Sultan ;
Onaizi, Sagheer A. .
JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2015, 26 :367-381
[3]   Absorption of carbon dioxide in aqueous piperazine/methyldiethanolamine [J].
Bishnoi, S ;
Rochelle, GT .
AICHE JOURNAL, 2002, 48 (12) :2788-2799
[4]  
Dash S.K., 2015, COMPUT AIDED CHEM EN, V52, P1, DOI [10.1016/b978-0-444-63578-5.50082-7, DOI 10.1016/B978-0-444-63578-5.50082-7.]
[5]   Studies on the effect of addition of piperazine and sulfolane into aqueous solution of N-methyldiethanolamine for CO2 capture and VLE modelling using eNRTL equation [J].
Dash, Sukanta Kumar ;
Bandyopadhyay, Syamalendu S. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2016, 44 :227-237
[6]   Sensitivity analysis for selection of an optimum amine gas sweetening process with minimum cost requirement [J].
Dashti, Sajjad Sharif ;
Shariati, Ahmad ;
Nikou, Mohammad Reza Khosravi .
ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2015, 10 (05) :709-715
[7]   Using mixed tertiary amines for gas sweetening energy requirement reduction [J].
Fouad, Wael A. ;
Berrouk, Abdallah S. .
JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2013, 11 :12-17
[8]   Experimental research on the performance of CO2-loaded solutions of MEA and DEA at regeneration conditions [J].
Galindo, Paula ;
Schaeffer, Anke ;
Brechtel, Kevin ;
Unterberger, Sven ;
Scheffknecht, Guenter .
FUEL, 2012, 101 :2-8
[9]   Modeling the effect of piperazine on CO2 loading in MDEA/PZ mixture [J].
Ghalib, Lubna ;
Ali, Brahim Si ;
Ashri, Wan Mohd ;
Mazari, Shaukat ;
Saeed, Idris Mohamed .
FLUID PHASE EQUILIBRIA, 2017, 434 :233-243
[10]   Simultaneous measurement solubility of carbon dioxide plus hydrogen sulfide into aqueous blends of alkanolamines at high pressure [J].
Haghtalab, Ali ;
Izadi, Amin .
FLUID PHASE EQUILIBRIA, 2014, 375 :181-190