Predictions of equilibrium solubility and mass transfer coefficient for CO2 absorption into aqueous solutions of 4-diethylamino-2-butanol using artificial neural networks

被引:0
作者
Meesattham S. [1 ]
Charoensiritanasin P. [1 ]
Ongwattanakul S. [2 ]
Liang Z. [3 ]
Tontiwachwuthikul P. [4 ]
Sema T. [1 ]
机构
[1] Department of Chemical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom
[2] Department of Biomedical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom
[3] Capture and Storage (iCCS), College of Chemistry and Chemical Engineering, Hunan University, Changsha
[4] Clean Energy Technologies Research Institute (CETRi), Faculty of Engineering and Applied Science, University of Regina, Regina, S4S 0A2, SK
来源
Petroleum | 2020年 / 6卷 / 04期
关键词
Artificial neural network; CO[!sub]2[!/sub] absorption; Equilibrium solubility; Mass transfer coefficient;
D O I
10.1016/j.petlm.2018.09.005
中图分类号
学科分类号
摘要
In the present work, artificial neuron network (ANN) based models for predicting equilibrium solubility and mass transfer coefficient of CO2 absorption into aqueous solutions of high performance alternative 4-diethylamino-2-butanol (DEAB) solvent were successfully developed. The ANN models show an outstanding predictive performance over the predictive correlations proposed in the literature. In order to predict the equilibrium solubility, the ANN model were developed based on three input parameters of operating temperature, concentration of DEAB and partial pressure of CO2. An outstanding prediction performance of 2.4% average absolute deviation (AAD) can be obtained (comparing with 7.1–8.3% AAD from the literature). Additionally, a significant improvement on predicting mass transfer coefficient can also be achieved through the developed ANN model with 3.1% AAD (comparing with 14.5% AAD from the existing semi-empirical model). The mass transfer coefficient is considered to be a function of liquid flow rate, liquid inlet temperature, concentration of DEAB, inlet CO2 loading, outlet CO2 loading, concentration of CO2 along the height of the column. © 2020
引用
收藏
页码:385 / 391
页数:6
相关论文
共 41 条
  • [1] PLC B., BP Statistical Review of World Energy 2017, (2017)
  • [2] Chaudhuri U.R., Fundamentals of Natural Gas Processing, (2011)
  • [3] Kidnay A.J., K A.J., Parrish W.R., McCartney D.G., Fundamentals of Natural Gas Processing, (2011)
  • [4] Mokhatab S., Poe W.A., Mak J.Y., Chapter 1 - natural gas fundamentals, Handbook of Natural Gas Transmission and Processing, pp. 1-36, (2015)
  • [5] Oh S.-Y., Yun S., Kim J.-K., Process integration and design for maximizing energy efficiency of a coal-fired power plant integrated with amine-based CO2 capture process, Appl. Energy, 216, 100, pp. 311-322, (2018)
  • [6] Dutcher B., Fan M., Russell A.G., Amine-based CO2 capture technology development from the beginning of 2013: A Review, ACS Appl. Mater. Interfaces, 7, 4, pp. 2137-2148, (2015)
  • [7] El Hadri N., Et al., Aqueous amine solution characterization for post-combustion CO2 capture process, Appl. Energy, 185, pp. 1433-1449, (2017)
  • [8] Liang Z., Et al., Review on current advances, future challenges and consideration issues for post-combustion CO2 capture using amine-based absorbents, Chin. J. Chem. Eng., 24, 2, pp. 278-288, (2016)
  • [9] Kohl A.L., Nielsen R., Gas Purification, (1997)
  • [10] Liang Z.H., Et al., Recent progress and new developments in post-combustion carbon-capture technology with amine based solvents, Int. J. Greenhouse Gas Contr., 40, pp. 26-54, (2015)