Energetic, exergetic and economic assessment of oxygen production from two columns cryogenic air separation unit

Energy

Volumn 90, Issue , 2015, Pages 1298-1316

  Ebrahimi, Armin ^a   Meratizaman, Mousa ^a   Reyhani, Hamed Akbarpour ^a   Pourali, Omid ^a   Amidpour, Majid ^a  

^a K N TOOSI UNIVERSITY OF TECHNOLOGY   (Iran)

Author keywords

Annualized cost of system; Energy analysis; Exergy analysis; Two columns cryogenic air separation unit

Indexed keywords

CHEMICAL ANALYSIS; COST BENEFIT ANALYSIS; COST EFFECTIVENESS; CRYOGENICS; DISTILLATION; DISTILLATION EQUIPMENT; DISTILLERIES; ECONOMIC ANALYSIS; EXERGY; INDUSTRIAL WATER TREATMENT; OXYGEN; SENSITIVITY ANALYSIS;

ANNUALIZED COST OF SYSTEM; CRYOGENIC AIR SEPARATION; ECONOMIC ASSESSMENTS; ENERGY ANALYSIS; EXERGY ANALYSIS; EXERGY DESTRUCTIONS; INDUSTRIAL OPERATIONS; INDUSTRIAL PROCESSS;

COSTS;

AIR SAMPLING; CHEMICAL REACTION; COMBUSTION; COST ANALYSIS; DISTILLATION; EXERGY; NITROGEN; OXYGEN; SENSITIVITY ANALYSIS;

EID: 84959368275     PISSN: 03605442     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.energy.2015.06.083     Document Type: Article

References (31)

1. Linde to build six major air separation units in China. Available online at: http://www.linde-gas.nl/en/news_and_media/press_releases/news_130311.html. Last access [5.8.2015].
2. Iora P, Chiesa P. High efficiency process for the production of pure oxygen based on solid oxide fuel cellesolid oxide electrolyzer technology. J Power Sources 2009;190:408-16.
3. Cornelissen RL, Hirs GG. Exergy analysis of cryogenic air separation. Energy Convers Manage 1998;39:1821-6.
4. Smith AR, Klosek J. A review of air separation technologies and their integration with energy conversion processes. Fuel Process Tech 2001;70:115-34.
5. Meratizaman M, Monadizadeh S, Ebrahimi A, Akbarpour H, Amidpour M. Scenario analysis of gasification process application in electrical energyfreshwater generation from heavy fuel oil, thermodynamic, economic and environmental assessment. Int J Hydrogen Energy 2015;40:2578-600.
6. Van der Ham LV, Kjelstrup S. Exergy analysis of two cryogenic air separation processes. Energy 2010;35:4731-9.
7. 2 capture. Fuel Process Tech 2011;92:1685-95.
8. Querol E, Gonzalez-Regueral B, Ramos A, Perez-Benedito JL. Novel application for exergy and thermoeconomic analysis of processes simulated with aspen plus. Energy 2011;36:964-74.
9. Fu C, Gundersen T. Using exergy analysis to reduce power consumption in air separation units for oxy-combustion processes. Energy 2012;44:60-8.
10. Hu Y, Li X, Li H, Yan J. Peak and off-peak operations of the air separation unit in oxy-coal combustion power generation systems. Appl Energy 2013;112: 747-54.
11. Kotowicz J, Balicki A. Enhancing the overall efficiency of a lignite-fired oxyfuel power plant with CFB boiler and membrane-based air separation unit. Energy Convers Manage 2014;80:20-31.
12. Bhattacharya A, Das A, Datta A. Exergy based performance analysis of hydrogen production from rice straw using oxygen blown gasification. Energy 2014;69:525-33.
13. Kaichen G, Vassilios SV. Limitations in using Euler's formula in the design of heat exchanger networks with Pinch technology. Comput Chem Eng 2014;68: 123-7.
14. LinnhoffB, Hindmarsh E. The pinch design method for heat exchanger networks. Chem Eng Sci 1983;38:745-63.
15. LinnhoffB, Mason DR, Wardle I. Understanding heat exchanger networks. Comput Chem Eng 1979;3(1):295-302.
16. Fu C, Gundersen T. Recuperative vapor recompression heat pumps in cryogenic air separation processes. Energy 2013;59:708-18.
17. Rao CS, Barik K. Modeling, simulation and control of middle vessel batch distillation column. Procedia Eng 2012;38:2383-97.
18. Eckert E, Kubicek M. Dynamic simulation of a distillation column with multiple liquid phase. Comput Chem Eng 1995;19:393-8.
19. Zhu Y, Legg S, Laird CD. Optimal operation of cryogenic air separation systems with demand uncertainty and contractual obligations. Chem Eng Sci 2011;66: 953-63.
20. Liu ZY, Jobson M. Retrofit design for increasing the processing capacity of distillation columns, a hydraulic performance indicator. Chem Eng Res Des 2004;82:3-9.
21. Chemical engineering design. 2nd ed. Elsevier Ltd; 2013. http://dx.doi.org/10.1016/B978-0-08-096659-5.00017-1.
22. Chan SH, Low CF, Ding OL. Energy and exergy analysis of simple solid oxide fuel cell power system. J Power Sources 2002;103:188-200.
23. Meratizaman M, Amidpour M, Jazayeri SA, Naghizadeh K. Energy and exergy analyses of urban waste incineration cycle coupled with a cycle of changing LNG to pipeline gas. J Nat Gas Sci Eng 2010;2:217-21.
24. Statistics which published by Central Bank of the Islamic Republic of Iran. June, 2014.
25. Rahimi S, Meratizaman M, Monadizadeh S, Amidpour M. Techno-economic analysis of wind turbine-PEM (polymer electrolyte membrane) fuel cell hybrid system in standalone area. Energy 2014;67:381-96.
26. Sayyaadi H, Mehrabipour R. Efficiency enhancement of a gas turbine cycle using an optimized tubular recuperative heat exchanger. Energy 2012;38: 362-75.
27. Khoshgoftar Manesh MH, Ghalami H, Amidpour M, Hamedi MH. Optimal coupling of site utility steam network with MED-RO desalination through total site analysis and exergoeconomic optimization. Desalination 2013;316: 42-52.
28. Galanti L, Massardo AF. Micro gas turbine thermodynamic and economic analysis up to 500 kWe size. Appl Energy 2011;88:4795-802.
29. Wei Z, Zhang B, Wu S, Chen Q, Tsatsaronis G. Energy-use analysis and evaluation of distillation systems through avoidable exergy destruction and investment costs. Energy 2012;42:424-33.
30. 2 emission dimethyl ether (DME) plant based on gasification of torrefied biomass. Energy 2010;35:4831-42.
31. Rivarolo M, Magistri L, Massardo AF. Hydrogen and methane generation from large hydraulic plant: thermo-economic multi-level time-dependent optimization. Appl Energy 2014;113:1737-45.