Optimal slow pyrolysis of apple pomace reaction conditions for the generation of a feedstock gas for hydrogen production

被引:28
作者
Baray Guerrero, M. R. [1 ]
Salinas Gutierrez, J. M. [1 ]
Melendez Zaragoza, M. J. [1 ]
Lopez Ortiz, A. [1 ]
Collins-Martinez, V. [1 ]
机构
[1] Ctr Invest Mat Avanzados SC, Dept Ingn & Quim Mat, Miguel de Cervantes 120, Chihuahua 31136, Chih, Mexico
关键词
Pyrolysis; Apple pomace; Hydrogen production; CO2; capture; SUGAR-CANE BAGASSE; VACUUM PYROLYSIS; BIOMASS; GASIFICATION; KINETICS; CAPTURE; ENERGY; YIELD;
D O I
10.1016/j.ijhydene.2016.10.066
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This research explores optimal reaction conditions for the generation of gas products, through the slow pyrolysis of apple pomace, to be used as a feedstock for the production of H-2 by the absorption enhanced reforming of methane (AER). Pyrolysis was performed at 300-450 degrees C and heating rates 5-20 degrees C/min. Gases, tars and chars were quantified at different heating rates and isothermal conditions. Results indicate that at 400 degrees C a maximum of 71.5% W of non-condensable volatile matter (NCVM) can be obtained along with 25.4% W of condensable volatile matter (CVM), while only 3% W of residual matter (RM). At these conditions (NCVM) a gas composition of 49.8% CO, 26.8% CO2 and 23.4% CH4 (Vol) was generated. A thermodynamic analysis of this product gas was performed under AER through CO2 absorption by CaO. Calculations using a steam to methane ratio of 3.5 and 3.5 mol of CaO/mol of CH4 indicate that a maximum H-2 production is achieved at 715 degrees C containing 73.0% H-2, 19.1% CO, 5.3% CO2 and 2.5% CH4 with no carbon formation. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:23232 / 23237
页数:6
相关论文
共 29 条
[1]   The maximum capture efficiency of CO2 using a carbonation/calcination cycle of CaO/CaCO3 [J].
Abanades, JC .
CHEMICAL ENGINEERING JOURNAL, 2002, 90 (03) :303-306
[2]   A review on operating parameters for optimum liquid oil yield in biomass pyrolysis [J].
Akhtar, Javaid ;
Amin, NorAishah Saidina .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2012, 16 (07) :5101-5109
[3]  
Akinwale AO, 2012, THERMOCHIM ACTA, V530, P95
[4]  
[Anonymous], J CHINA U MINING TEC
[5]   Hydrogen from methane in a single-step process [J].
Balasubramanian, B ;
Ortiz, AL ;
Kaytakoglu, S ;
Harrison, DP .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (15-16) :3543-3552
[6]   Total condensable effluents yield in slow pyrolysis of bagasse briquettes [J].
Brossard, LE ;
Cortez, LAB ;
Penedo, M ;
Bezzon, G ;
Olivares, E .
ENERGY CONVERSION AND MANAGEMENT, 2000, 41 (03) :223-233
[7]  
BRUNTSEKHOVOI AR, 1986, P WORLD HYDR EN C, V2, P885
[8]   Comparison of slow and vacuum pyrolysis of sugar cane bagasse [J].
Carrier, Marion ;
Hugo, Thomas ;
Gorgens, Johann ;
Knoetze, Hansie .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2011, 90 (01) :18-26
[9]   Energy and exergy analyses of a biomass-based hydrogen production system [J].
Cohce, M. K. ;
Dincer, I. ;
Rosen, M. A. .
BIORESOURCE TECHNOLOGY, 2011, 102 (18) :8466-8474
[10]   A review of catalytic issues and process conditions for renewable hydrogen and alkanes by aqueous-phase reforming of oxygenated hydrocarbons over supported metal catalysts [J].
Davda, RR ;
Shabaker, JW ;
Huber, GW ;
Cortright, RD ;
Dumesic, JA .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 56 (1-2) :171-186