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Sulfur Distribution during Hydrothermal Liquefaction of Lignite, Wheat Straw and Plastic Waste in Sub-Critical Water 被引量:1

Sulfur Distribution during Hydrothermal Liquefaction of Lignite, Wheat Straw and Plastic Waste in Sub-Critical Water
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摘要 The distribution and transformation of sulfur in products during hydrothermal liquefaction of lignite, wheat straw and plastic waste in sub-critical water were investigated in an autoclave. The influence of blending ratio, temperature, initial nitrogen pressure, residence time and additives on sulfur distribution was studied systematically. The results showed that most of sulfur existed as organic sulfur and transferred into the residue, and only a small part of sulfur transferred into oil and gas during hydrothermal liquefaction of lignite, wheat straw and plastic waste in sub-critical water. The results also showed that lower temperature(less than 300 ℃) was favorable for obtaining oil with low sulfur content. It can be also seen from the results that the best condition to obtain the oil with low sulfur content should be implemented at a lignite/wheat straw/plastic waste blending ratio of 5:4:1, an initial nitrogen pressure of 3 MPa and a residence time of 30 minutes. Furthermore, the results indicated that adding tourmaline during hydrothermal liquefaction of lignite, wheat straw and plastic waste was beneficial to production of oil with low sulfur content. The distribution and transformation of sulfur in products during hydrothermal liquefaction of lignite, wheat strawand plastic waste in sub-critical water were investigated in an autoclave. The influence of blending ratio, temperature, initialnitrogen pressure, residence time and additives on sulfur distribution was studied systematically. The results showed thatmost of sulfur existed as organic sulfur and transferred into the residue, and only a small part of sulfur transferred into oiland gas during hydrothermal liquefaction of lignite, wheat straw and plastic waste in sub-critical water. The results alsoshowed that lower temperature (less than 300 ℃) was favorable for obtaining oil with low sulfur content. It can be also seenfrom the results that the best condition to obtain the oil with low sulfur content should be implemented at a lignite/wheatstraw/plastic waste blending ratio of 5:4:1, an initial nitrogen pressure of 3 MPa and a residence time of 30 minutes. Furthermore,the results indicated that adding tourmaline during hydrothermal liquefaction of lignite, wheat straw and plasticwaste was beneficial to production of oil with low sulfur content.
出处 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2015年第1期24-30,共7页 中国炼油与石油化工(英文版)
基金 Financial support to this work provided by the Research Fund for the Doctoral Program of Higher Education for New Teachers of China (20091404120002) the Shanxi Province Science Foundation for the Youth of China (2011021008-1) the Soft Science Program of Shanxi Province (2011041015-01)was gratefully acknowledged
关键词 lignite WHEAT straw plastic waste HYDROTHERMAL liquefaction SULFUR lignite wheat straw plastic waste hydrothermal liquefaction sulfur
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参考文献22

  • 1Kannan P, Shoaibi A Al, Srinivasakannan C. Energy recov-ery from co-gasification of waste polyethylene and polyethyleneterephthalate blends [J]. Computers & Fluids, 2013,88: 38-42.
  • 2Wu Chunfei, Williams P T. Pyrolysis–gasification of postconsumermunicipal solid plastic waste for hydrogen production[J]. Int J Hydrogen Energy, 2010, 35 (3): 949-957.
  • 3Sharma S, Ghoshal A K. Study of kinetics of co-pyrolysisof coal and waste LDPE blends under argon atmosphere [J].Fuel, 2010, 89(12): 3943-3951.
  • 4Yang Tianhua, Kai Xingping, Sun Yang, et al. The effect ofcoal sulfur on the behavior of alkali metals during co-firingof biomass and coal [J]. Fuel, 2011, 90 (7): 2454-2460.
  • 5Montiano M G, Barriocanal C, Alvarez R. Effect of the additionof waste sawdust on thermoplastic properties of acoal [J]. Fuel, 2013, 106: 537-543.
  • 6Howaniec N, Smolinski A. Effect of fuel blend compositionon the efficiency of hydrogen-rich gas production inco-gasification of coal and biomass [J]. Fuel, 2014, 128:442-450.
  • 7Brebu M, Ucar S, Vasile C, et al. Co-pyrolysis of pine conewith synthetic polymers [J]. Fuel, 2010, 89 (8): 1911-1918.
  • 8Karaca F, Bolat E. Coprocessing of a Turkish lignite with acellulosic waste material: 1. The effect of coprocessing onliquefaction yields at different reaction temperatures [J].Fuel Process Technol, 2000, 64 (1/3): 47-55.
  • 9Pei Xiaokai, Yuan Xingzhong, Zeng Guangming, et al. Coliquefactionof microalgae and synthetic polymer mixturein sub- and supercritical ethanol [J]. Fuel Process Technol,2012, 93 (1): 35-44.
  • 10Haykiri-Acma H, Yaman S. Interaction between biomassand different rank coals during co-pyrolysis [J]. RenewableEnergy, 2010, 35 (1): 288-292.

同被引文献15

  • 1宋安太.塔河常压渣油结焦特性及焦化加工对策[J].炼油技术与工程,2004,34(7):6-9. 被引量:12
  • 2陈进荣,杨继涛,孙在春,范耀华.大庆渣油族组分非等温热反应的研究[J].燃料化学学报,1994,22(1):77-82. 被引量:7
  • 3周晓龙,陈绍洲,常可怡.减压渣油组成和结构的研究[J].华东理工大学学报(自然科学版),1995,21(6):649-653. 被引量:14
  • 4于承租.油样加氢脱硫催化剂级配方案工业应用与优化[D].东营:中国石油大学,2009.
  • 5李占武.我国重质原油的评价[J].石油炼制,1988,19(1):7-9.
  • 6张寿增,岳淑范,沈家珍,等.大庆、胜利及任丘渣油的组成研究[J].石油炼制,1982(1):24-33.
  • 7Chen Xiaoho,Li Teng,Liu Yibin,et al. Characterization of ni trogen compounds in vacuum residue and their structure com- parison with coker gas oil[J]. China Petroleum Processing and Petrochemical Technology, 2014,16(3) : 33-41.
  • 8SH/T0509-1992(1998版)石油沥青四组分[S].1998.
  • 9Sharp J H,Wentworth S A. Kinetic analysis of thermogravi metric data[J]. Anal Chem, 1969,41 (14) : 2060- 2067.
  • 10Martin H. Vis-breaking process has strong revival[J].Oil Gas J,1981,79(9) :109- 120.

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