期刊文献+

超临界水中氨基乙酸的气化产氢特性 被引量:2

Glycine gasification in supercritical water for hydrogen production
下载PDF
导出
摘要 鉴于湿生物质如食品加工工业残余物和城市污泥中含有大量蛋白质的情况,以氨基乙酸作为蛋白质的模型化合物进行超临界水气化实验,研究了反应温度和反应时间耦合条件下Na2CO3的催化特性以及氨基乙酸气化产物特性。结果表明:添加Na2CO3会增大氨基乙酸的气化效率、氢气的体积分数和产率以及反应后液体化学需氧量(COD)的去除率,且添加质量分数为0.1%时的催化效果优于0.2%;Na2CO3主要是对H2产率产生影响,其催化机理与已有碱性化合物的催化机理不同,可能是通过促进氨基乙酸的水解产物(甲酸)的脱羧反应来提高H2的产率;氨基乙酸气化效率可达99.4%,生成物包括H2、CO2、N2、CH4和C2~C3气体,其中H2的体积分数可超过50%,产率可达1.8L.g-1,且超过一半的份额来源于水,反应后液体清澈透明,COD和pH值指标均可以达到《生活杂用水水质标准》,可以进行回收利用。 Because wet biomass such as residues from food industry or sewage sludge usually contains plenty of protein, the experiments of glycine gasification in supercritical water were conducted, in which glycine was used as the model compound of protein. The catalytic mechanism of sodium carbonate, product characteristics of glycine gasification were investigated with coupled relation between reaction temperature and reaction time. The results showed that sodium carbonate could increase gasification efficiency of glycine, the yield and volume fraction of hydrogen, and the removal efficiency of chemical oxygen demand (COD) of liquid products. The catalytic effect of addition amount of 0.1% mass concentration was better than that of 0.2%. And the effect of sodium carbonate on hydrogen yield was greater than that on volume fraction. The catalytic mechanism of sodium carbonate for glycine gasification was different from that of alkali compounds which has been reported before. Sodium carbonate increased the hydrogen yield probably by accelerating the decarboxylation reaction of formic acid, which was a glycine hydrolysate. Glycine could almost be gasified completely. The gas products include H2, CO2, N2, CH4, C2--C3, in which hydrogen volume fraction could be higher than 50%, hydrogen yield could be up to 1.8 L· g^-1, and more than half of hydrogen came from water. The liquid after reaction could be reused not only because it was clear and transparent but also because both the COD and pH values were met the quality standard of domestic water for miscellaneous use.
出处 《化工学报》 EI CAS CSCD 北大核心 2008年第3期735-742,共8页 CIESC Journal
基金 国家重点基础研究发展计划项目(2003CB214502) 国家高技术研究发展计划项目(2006AA06Z313)~~
关键词 超临界水 氨基乙酸 气化 氢气 supercritical water glycine gasification hydrogen
  • 相关文献

参考文献34

  • 1Calzavara Y, Joussot D C, Boissonnet G, Sarrade S. Evaluation of biomass gasification in supercritical water process for hydrogen production. Energy Conversion and Management, 2005, 46:615-631
  • 2Matsumura Y. Evaluation of supercritical water gasification and biornethanation for wet biomass utilization in Japan. Energy Conversion and Management, 2002, 43:1301-1310
  • 3Bridgewater A. The technical feasibility of biomass gasification for power generation. Fuel, 1997, 74: 631-653
  • 4Demirbas A. Hydrogen-rich gas from fruit shells via supercritieal water extraction. International Journal of Hydrogen Energy, 2004, 29:1237-1243
  • 5Yoshida Y, Dowaki K, MatsumuraY, Matsuhashi R, Li D, Ishitani H, Komiyama H. Comprehensive comparison of efficiency and CO2 emissions between biomass energy conversion technologies- position of supercritieal water gasification in biomass technologies.Biomass and Bioenergy, 2003, 25 (3): 257-272
  • 6Sehmieder H, Abeln J, Boukis N, Dinjus E, Kruse A, Kluth M, Petrich G, Sadri E, Schacht M. Hydrothermal gasification of biomass and organic wastes. Journal of Supercritical Fluids, 2000, 17:145-153
  • 7Yan Q H, Guo I. J, Lu Y J. hydrogen production from Thermodynamic analysis of biomass gasification in supercritical water. Energy Conversion and Management 2006, 47:1515-1528
  • 8Watanabe M, Aizawa Y, Iida T, Levy C, Taku M, Aida T M, Inoraata H. Glucose reactions within the heating period and the effect of heating rate on the reactions in hot compressed water. Carbohydrate Research, 2005, 340: 1931-1939
  • 9Hao X H, Guo L J, Mao X, Zhang X M, Chen X J. Hydrogen production from glucose used as a model compound of biomass gasified in supercritical water. International Journal of Hydrogen Energy, 2003, 28: 55-64
  • 10Watanabe M, Inomata H, Arai K. Catalytic hydrogen generation from biomass (glucose and cellulose) with ZrO2 in supercritical water. Biomass and Bioenergy, 2002, 22: 405-410

二级参考文献44

  • 1吴川,张华民,衣宝廉.化学制氢技术研究进展[J].化学进展,2005,17(3):423-429. 被引量:65
  • 2[1]Modell M.Reforming of glucose and wood at the critical condition of water[C]//ASME Intersociety Conference on Environmental Systems.San Francisco,1977:8-13.
  • 3[3]Antal M J,Leesonboom T,Mok W S,et al.Mechanism of formation of 2-furaldehyde from D-xylose[J].Carbohydrate Research,1991,217:71-85.
  • 4[4]Kabyemela B M,Adschiri T,Malaluan R M,et al.Glucose and fructose decomposition in subcritical and supercritical water:Detailed reaction pathway,mechanisms,and kinetics[J].Industrial and Engineering Chemistry Research,1999,38:2888-2895.
  • 5[5]Kabyemela B M,Adschiri T,Malaluan R M,et al.Kinetics of glucose epimerization and decomposition in subcritical and supercritical water[J].Industrial and Engineering Chemistry Research,1997,36:1552-1558.
  • 6[6]Holgate H R,Meyer J C,Tester J W.Glucose hydrolysis and oxidation in supercritical water[J].AIChE Journal,1995,41:637-648.
  • 7[7]Kabyemela B M,Takigawa M,Adschiri T,et al.Mechanism and kinetics of cellobiose decomposition in sub-and supercritical water[J].Industrial and Engineering Chemistry Research,1998,37:357-361.
  • 8[8]Kabyemela B M,Adschiri T,Malaluan R,et al.Degradation kinetics of dihydroxyacetone and glyceraldehydes in subcritical and supercritical water[J].Industrial and Engineering Chemistry Research,1997,36:2025-2030.
  • 9[9]Bobleter O.Hydrothermal degradation of polymers derived from plants[J].Progress in Polymer Science,1994,19:797-841.
  • 10[10]Schmieder H,Abeln J,Boukis N,et al.Hydrothermal gasification of biomass and organic wastes[J].Journal of Supercritical Fluids,2000,17:145-153.

共引文献4

同被引文献42

引证文献2

二级引证文献5

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部