Experimental methods in chemical engineering: Process simulation

被引:15
作者
De Tommaso, Jacopo [1 ]
Rossi, Francesco [2 ]
Moradi, Nooshin [3 ]
Pirola, Carlo [4 ]
Patience, Gregory S. [1 ]
Galli, Federico [1 ]
机构
[1] Polytech Montreal, Chem Engn, CP 6079, Montreal, PQ H3C 3A7, Canada
[2] Purdue Univ, Davidson Sch Chem Engn, Forney Hall Chem Engn, Sch Chem Engn, W Lafayette, IN 47907 USA
[3] Shiraz Univ, Sch Chem & Petr Engn, Shiraz, Iran
[4] Univ Milan, Dipartimento Chim, Milan, Italy
关键词
cost estimation; design; optimization; process simulation; thermodynamics; INTENSIFICATION EDUCATION CONTRIBUTES; HEAT-EXCHANGER NETWORKS; VAPOR-LIQUID-EQUILIBRIA; DYNAMIC SIMULATION; P-XYLENE; DESIGN; DISTILLATION; SEPARATION; ENERGY; MULTICOMPONENT;
D O I
10.1002/cjce.23857
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Process simulation software designs equipment, simulates operations, optimizes a plant's configuration (heat exchangers network, for example), estimates operating and capital expenses, and serves as an educational tool. However, mastering the theoretical background minimizes common mistakes such as applying an incorrect thermodynamic method, selecting improper algorithms in the case of tear systems, and setting irrational system specifications. Engineers and researchers will exploit this tool more often in the future as constant advancements in simulation science as well as new models are released continually. Process simulators make it easier to build digital twins and thus will facilitate the implementation of the industry 4.0 guidelines. We highlight the mathematical and technical features of process simulators, as well as the capabilities and the fields of application. A bibliometric map of keywords from articles citing Aspen+, Aspen plus, Hysys, and Pro/II indexed byWeb of Sciencebetween 2017 and 2020 identified the main research clusters, such as design, optimization, energy or exergy, biomass; H(2)and CO(2)capture, thermodynamics; and separations and techno-economic analysis.
引用
收藏
页码:2301 / 2320
页数:20
相关论文
共 121 条
[1]   STATISTICAL THERMODYNAMICS OF LIQUID-MIXTURES - NEW EXPRESSION FOR EXCESS GIBBS ENERGY OF PARTLY OR COMPLETELY MISCIBLE SYSTEMS [J].
ABRAMS, DS ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1975, 21 (01) :116-128
[2]  
[Anonymous], 2007, EVOLUTIONARY ALGORIT
[3]  
[Anonymous], 1947, CHEM ENG
[4]  
Aspen Plus, 2004, 1 GETTING STARTED US
[5]   Clean hydrogen generation and storage strategies via CO2 utilization into chemicals and fuels: A review [J].
Bahari, Nurazni Amat ;
Isahak, Wan Nor Roslam Wan ;
Masdar, Mohd Shahbudin ;
Yaakob, Zahira .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2019, 43 (10) :5128-5150
[6]   Hydrogenation to convert CO2 to C1 chemicals: Technical comparison of different alternatives by process simulation [J].
Barbera, Elena ;
Mantoan, Fabio ;
Bertucco, Alberto ;
Bezzo, Fabrizio .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2020, 98 (09) :1893-1906
[7]  
Barkley R., 1972, Chem. Eng. J, V3, P265, DOI [10.1016/0300-9467(72)85030-5, DOI 10.1016/0300-9467(72)85030-5]
[8]  
Biegler LT, 2010, MOS-SIAM SER OPTIMIZ, V10, pXIII, DOI 10.1137/1.9780898719383
[9]   Simulator-based learning in the teaching of chemical engineering [J].
Borreguero, Ana M. ;
Valverde, Jose L. ;
Garcia-Vargas, Jesus M. ;
Sanchez-Silva, Luz .
COMPUTER APPLICATIONS IN ENGINEERING EDUCATION, 2019, 27 (05) :1267-1276
[10]   NEW CLASS OF SOLUTION METHODS FOR MULTICOMPONENT, MULTISTAGE SEPARATION PROCESSES [J].
BOSTON, JF ;
SULLIVAN, SL .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1974, 52 (01) :52-63