期刊文献+

基于连续热力学分析的塔河常压渣油戊烷溶剂脱沥青 被引量:2

Pentane Solvent Deasphalting of Tahe Atmospheric Residue Based on Continuous Thermodynamics Analysis
下载PDF
导出
摘要 针对塔河原油高金属、高沥青质、高酸值等特点,为避免加工过程中的高温腐蚀问题,将其经常压闪蒸后直接作为溶剂脱沥青工艺的原料进行加工。基于连续热力学分析,建立了溶剂脱沥青过程的相对分子质量分布模型,以所建模型考察了塔河常压闪蒸渣油戊烷溶剂脱沥青过程的操作条件对脱沥青油和脱油沥青的相对分子质量分布和产率的影响,并与中试装置所得结果进行对比,绝对误差小于5%。溶剂脱沥青中试实验的适宜操作条件为压力3.7MPa、温度175℃、剂/油比5.0,此时脱沥青油产率为75.2%,平均相对分子质量440,其性质满足催化裂化装置的进料要求,同时,脱油沥青可以作为沥青混合料添加剂。 Due to high content of metal, asphaltene and high acid value, Tahe atmospheric flashing residue was directly used as the feedstock of solvent deasphalting to avoid the high temperature corrosion in traditional process for Tahe crude oil. Based on continuous thermodynamics analysis, relative molecular mass distribution model for solvent deasphalting was established. The effects of different operating conditions of solvent deasphalting on the relative molecular mass distribution and yield of deasphalting oil and de-oil asphalt were investigated by the model. The absolute error between model calculated value and the medium experimental value was less than 5 %. The suitable conditions of medium solvent deasphalting process were the extraction temperature of 175℃, the extraction pressure of 3.7 MPa and the solvent/residue ratio of 5.0, under which the yield of deasphalted oil was 75.2% with the average relative molecular mass of 440, and its properties met the feed requirement for catalytic cracking unit. Meanwhile, de-oil asphalting can be used as asphalt mixture additive.
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2015年第2期487-496,共10页 Acta Petrolei Sinica(Petroleum Processing Section)
基金 国家自然科学基金项目(21476082) 中国石油化工股份有限公司合同项目(110104)资助
关键词 连续热力学 塔河原油 溶剂脱沥青 相对分子质量分布 continuous thermodynamics Tahe crude oil solvent deasphalting relative molecular mass distribution
  • 相关文献

参考文献12

  • 1KEHLEN, RATZSCH M T. Separate treatment of paraffins and aromatics in complex hydrocarbon mixtures by continuous thermodynamics [J]. Z Phys Chemic Leipzig, 1984, 265(6): 1049-1060.
  • 2KEHLEN, RATZSCH M T. Continuous thermodynamics of multicomponent systems[J]. AIChE, 1985, 31 (7) : 1136 1148.
  • 3江涛,杨光华.连续热力学及其在复杂混合物相平衡计算中的应用[J].石油大学学报(自然科学版),1992,16(2):115-120. 被引量:1
  • 4PARK J H, KIMH Y. Continuous thermodynamics of phase equilibria using the beta distribution function and an equation of state[J]. Korean J of Chem Eng, 1993, 10(2) : 71-77.
  • 5水恒福,沈本贤,高晋生,杨忠木.混合C_4溶剂脱沥青工艺研究-DAO与DOA影响因素考察[J].华东冶金学院学报,2000,17(1):15-19. 被引量:5
  • 6龙军,王子军,黄伟祁,祖德光.重溶剂脱沥青在含硫渣油加工中的应用[J].石油炼制与化工,2004,35(3):1-5. 被引量:36
  • 7段晓磊,王金刚,丁振君,任彦斌.塔河原油对常压设备腐蚀分析[J].化工装备技术,2009,30(1):49-52. 被引量:4
  • 8COTTERMAN R L, DIMITRELIS D, JOHN M P. Design of supercritical fluid extractionprocesses using continuous thermodynamics [ C ]//Supercritical Fluid Technology. Amsterdam: JML Penninger. 1985.
  • 9NASRIFAR K H. Application of an improved simplified perturbed hard chain theory equation of state for pure compounds and binary asymmetric mixtures [J]. Fluid Phase Equil, 2004, 216: 147 152.
  • 10PRAUSNITZ J M, LICHENTHAI.ER R N, AZEVEDO E G, et al. Molecular Thermodynamics of Fluid-Phase Equilibria [ M]. 2nd. Englewood Cliffs: Prentice Hall Inc. 1986.

二级参考文献10

  • 1柴志杰,李彬.一种新的塔河重质原油炼制工艺[J].炼油技术与工程,2006,36(6):35-37. 被引量:6
  • 2SH/T3096-2001.加工高硫原油重点装置主要设备设计选材导则[S].2001.
  • 3Sprague S B. How solvent selection affects extraction efficiency. NPRA Annual Meeting, 1986,AM-86-36
  • 4Hartnett C G. Some aspects of heavy oil processing. API 37th Midyear Meeting, New York, May 1982
  • 5Northup A H. Advance in solvent deasphalting technology.NPRA Annual Meeting, 1996, AM-96-55
  • 6Gillis D B. What 's new in solvent deasphalting. Foster Wheeler Heavy Oil Conference, June 1998.16
  • 7Ditman J G. Solvent deasphalitng-a versatile tool for the preparation of lube hytroitreating feed stocks. API 37th Midyear Meeting, New York, May 1982. 713-723
  • 8Wauquier J P. Separation Process Paris: Technip, 440-448
  • 9Biedermann J M. Solvahl: An attractive way to provide conversion units with high quality feedstock. NPRA Annual Meeting,1987, AM-87-41
  • 10中国石化设备管理协会.石油化工装置设备腐蚀与防护手册[M].北京:中国石化出版社.1996.565~567

共引文献41

同被引文献23

  • 1JunShi Tang, Qiang Song, BaiLei He,Qiang Yao.Oxidation behavior of a kind of carbon black[J].Science China(Technological Sciences),2009,52(6):1535-1542. 被引量:2
  • 2XUChun-ruing(徐春明),YANGChao-he(杨朝合).Petroleumrefiningengineering(石油炼制工程)[M].Beijing(北京):PetroleumIndustryPress(石油工业出版社),2009.
  • 3Speight J G. The chemistry and technology of petroleum [M]. New York: CRC Press, 2006.
  • 4van Grieken R, Coto B, Romero E, et aL Prediction of liquid-liquid equilibrium in the system furfural + heavy neutral distillate lubricating oil [J]. Industrial & Engineering Chemistry Research, 2005, 44(21): 8106-8112.
  • 5Coto B, van Grieken R, Pefia J, et al. A model to predict physical properties for light lubricating oils and its application to the extraction process by furfural [J]. Chemical Engineering Science, 2006, 61(13): 4381-4392.
  • 6Coto B, van Grieken R, Pefia J, et al. A generalized model to predict the liquid-liquid equilibrium in the systems furfural + lubricating oils [J]. Chemical Engineering Science, 2006, 61(24): 8028-8039.
  • 7Espada, J J, Coto B, Pena J L. Liquid-liquid equilibrium in the systems furfural + light lubricating oils using UNIFAC [J]. Fluid Phase Equilibria, 2007, 259 (2): 201-209.
  • 8de Lucas A, Rodriguez L, Sanchez P, et al. Extraction of aromatic compounds from heavy neutral distillate lubricating oils by using al [J]. Separation Science and Technology, 1993, 28(15-16): 2465-2477.
  • 9Eckert E, Vanek T. Improvements in the selection of real components forming a substitute mixture for petroleum fractions [J]. Chemical Papers, 2009, 63(4): 399-405.
  • 10Verstraete J J, Schnongs P, Dulot H, et al. Molecular reconstruction of heavy petroleum residue fractions [J]. Chemical Engineering Science, 2010, 65(1): 304-312.

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