Effects of integrating a bioethanol production process to a kraft pulp mill

被引:12
作者
Kautto, Jesse [1 ]
Henricson, Kaj [2 ]
Sixta, Herbert [3 ]
Trogen, Mikaela [3 ]
Alen, Raimo [4 ]
机构
[1] Lappeenranta Univ Technol, Technol Business Res Ctr, FI-53851 Lappeenranta, Finland
[2] Lappeenranta Univ Technol, Dept Chem Technol, FI-53851 Lappeenranta, Finland
[3] Aalto Univ, Dept Forest Prod Technol, FI-02015 Espoo, Finland
[4] Univ Jyvaskyla, Dept Chem, FI-40014 Jyvaskyla, Finland
关键词
Kraft pulp mill; Hemicellulose extraction; Water prehydrolysis; Biorefinery; Bioethanol; EUCALYPTUS-GLOBULUS WOOD; PRE-EXTRACTION; SOUTHERN PINE; AUTOHYDROLYSIS; PREHYDROLYSIS; ETHANOL;
D O I
10.3183/npprj-2010-25-02-p233-242
中图分类号
TB3 [工程材料学]; TS [轻工业、手工业、生活服务业];
学科分类号
0805 ; 080502 ; 0822 ;
摘要
The integration of an ethanol production process based on prehydrolysis of softwood chips to a kraft pulp mill is discussed. A simulation model of this biorefinery has been created with WinGEMS simulation software to calculate the mass and energy balances of the biorefinery and to examine the effects of the integration on the operation of the pulp mill. Integrating the prehydrolysis process to the modeled pulp mill producing 1000 Adt/day of pine pulp would increase the wood consumption by 16%. With the increased wood consumption, 40 t/day of ethanol could be produced, and the excess power production could be increased by 460 MWh/day. The integration of the ethanol production process to a pulp mill would have considerable effects on the operation of the pulp mill. The coupling of hydrolyzate evaporation with black liquor evaporation would require major modifications in the evaporation plant. Due to the burning of organic residue from the ethanol process and to the increase in the heating value of black liquor, the load on the recovery boiler would increase by 31%.
引用
收藏
页码:233 / 242
页数:10
相关论文
共 22 条
[1]  
Al-Dajani WW, 2008, TAPPI J, V7, P3
[2]  
[Anonymous], GUARDIAN 0704
[3]  
CASEBIER RL, 1969, TAPPI, V52, P2369
[4]  
FOGELHOLM CJ, 2000, CHEM PULPING PAPERMA, P303
[5]   Co-production of ethanol and cellulose fiber from Southern Pine: A technical and economic assessment [J].
Frederick, W. J., Jr. ;
Lien, S. J. ;
Courchene, C. E. ;
DeMartini, N. A. ;
Ragauskas, A. J. ;
Iisa, K. .
BIOMASS & BIOENERGY, 2008, 32 (12) :1293-1302
[6]   Non-isothermal autohydrolysis of Eucalyptus wood [J].
Garrote, G ;
Parajó, JC .
WOOD SCIENCE AND TECHNOLOGY, 2002, 36 (02) :111-123
[7]   Generation of xylose solutions from Eucalyptus globulus wood by auto hydrolysis-posthydrolysis processes:: Posthydrolysis kinetics [J].
Garrote, G ;
Dominguez, H ;
Parajó, JC .
BIORESOURCE TECHNOLOGY, 2001, 79 (02) :155-164
[8]   Ethanol from lignocellulosic biomass: techno-economic performance in short-, middle- and long-term [J].
Hamelinck, CN ;
van Hooijdonk, G ;
Faaij, APC .
BIOMASS & BIOENERGY, 2005, 28 (04) :384-410
[9]   Process Modeling of Comprehensive Integrated Forest Biorefinery-An Integrated Approach [J].
Huang, Hua-Jiang ;
Lin, Weilu ;
Ramaswamy, Shri ;
Tschirner, Ulrike .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2009, 154 (1-3) :205-216
[10]  
LEHTINEN M, 2001, AEL METSKO SEM MARCH