Oxygen-steam gasification of karanja press seed cake: Fixed bed experiments, ASPEN Plus process model development and benchmarking with saw dust, rice husk and sunflower husk

被引:65
作者
Dhanavath, Kotaiah Naik [2 ]
Shah, Kalpit [2 ]
Bhargava, Suresh K. [3 ]
Bankupalli, Satyavathi [1 ]
Parthasarathy, Rajarathinam [2 ]
机构
[1] Indian Inst Chem Technol, Chem Engn Div, Hyderabad 500007, Andhra Pradesh, India
[2] RMIT Univ, Sch Engn, Chem & Environm Engn, Melbourne, Vic 3001, Australia
[3] RMIT Univ, Sch Sci, Ctr Adv Mat & Ind Chem, Melbourne, Vic 3001, Australia
关键词
Fixed bed gasifier; Biomass; Karanja press seed cake; Aspen Plus simulation; Synthesis gas; BIOMASS GASIFICATION; BIO-OIL; GAS-PRODUCTION; PERFORMANCE ANALYSIS; SLOW PYROLYSIS; GASIFIER; SIMULATION; AIR; TEMPERATURE; REACTOR;
D O I
10.1016/j.jece.2018.04.046
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This article aims at investigating the oxygen-steam gasification of Karanja press seed cake using experimental and modeling studies and compare the results of these studies with those for other feedstocks such as rice husk, sawdust, and sunflower husk. The experimental work was conducted in a fixed bed reactor and the process simulation model was created in ASPEN Plus. Finally, validation and benchmarking exercise were conducted by validating the ASPEN Plus model using experimental results. A general agreement was found between the experimental results and ASPEN Plus process model results with a maximum variation of +/- 4%. Furthermore, sensitivity analyses were carried out to understand the effects of parameters such as gasification temperature, ER (equivalence ratio), and SBR (steam to biomass ratio) on synthesis gas composition, LHV (lower heating value) and CGE (cold gas efficiency). The optimal values of ER and SBR in this study were found to be 0.23 and 0.3, respectively. The CGE was found to increase with an increase in the temperature. Values of CGE and LHV were found to be as high as 95% and similar to 12 MJ/Nm(3), respectively at 1000 degrees C for all feedstocks. The optimum SBR value was found to vary from 0.3 to 0.7 for H-2/CO variation in the range of similar to 0.83-1.0.
引用
收藏
页码:3061 / 3069
页数:9
相关论文
共 53 条
[1]   Catalytic pyrolysis of rice husk for bio-oil production [J].
Abu Bakar, Muhammad S. ;
Titiloye, James O. .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2013, 103 :362-368
[2]  
[Anonymous], NUCLEUS
[3]  
[Anonymous], 2016, INT J RENEW ENERGY C
[4]   Performance Analysis of an Integrated Fixed Bed Gasifier Model for Different Biomass Feedstocks [J].
Begum, Sharmina ;
Rasul, Mohammad G. ;
Akbar, Delwar ;
Ramzan, Naveed .
ENERGIES, 2013, 6 (12) :6508-6524
[5]   Biomass gasification for decentralized power generation: The Indian perspective [J].
Buragohain, Buljit ;
Mahanta, Pinakeswar ;
Moholkar, Vijayanand S. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2010, 14 (01) :73-92
[6]   Biomass pyrolysis/gasification for product gas production: the overall investigation of parametric effects [J].
Chen, G ;
Andries, J ;
Luo, Z ;
Spliethoff, H .
ENERGY CONVERSION AND MANAGEMENT, 2003, 44 (11) :1875-1884
[7]   Energy efficient thermochemical conversion of very wet biomass to biofuels by integration of steam drying, steam electrolysis and gasification [J].
Clausen, Lasse R. .
ENERGY, 2017, 125 :327-336
[8]   Experimental investigations on entrained flow gasification of Torrefied Karanja Press Seed Cake [J].
Dhanavath, Kotaiah Naik ;
Shah, Kalpit ;
Islam, Md. Sakinul ;
Ronte, Anil ;
Parthasarathy, Rajarathinam ;
Bhargava, Suresh K. ;
Bankupalli, Satyavathi .
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2018, 6 (01) :1242-1249
[9]   Experimental investigations on the effect of pyrolytic bio-oil during the liquefaction of Karanja Press Seed Cake [J].
Dhanavath, Kotaiah Naik ;
Islam, Md. Sakinul ;
Bankupalli, Satyavathi ;
Bhargava, Suresh K. ;
Shah, Kalpit ;
Parthasarathy, Rajarathinam .
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2017, 5 (05) :4986-4993
[10]   Derivation of optimum operating conditions for the slow pyrolysis of Mahua press seed cake in a fixed bed batch reactor for bio-oil production [J].
Dhanavath, Kotaiah Naik ;
Shah, Kalpit ;
Bankupalli, Satyavathi ;
Bhargava, Suresh K. ;
Parthasarathy, Rajarathinam .
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2017, 5 (04) :4051-4063