[1] 杨光福.典型石油加工工艺过程中结焦形态及其危害[J].安全,2011,10:19-21. [2] SHELL D,HAYWARD C,EDWARD C.Phosphorous ester antifoulants in crude oil refining:US4024050[P].1977-05-17. [3] SHELL D,HAYWARD C,EDWARD C.Using an antifoulant in a crude oil heating process:US4024051[P].1977-05-17. [4] KINNEY R,CROWLEY D.Pyrolysis of C2 and C3 hydrocarbons[J].I&EC,1954,46(2):258-264. [5] ALBRIGHT L F,MAREK J C.Coke formation during pyrolysis:roles of residence time,reactor geometry and time of operation[J].I&EC,1988,27(5):743-751. [6] CRYNES L,CRYNES B.Coke formation on polished and unpo-lished incoloy 800 coupons during pyrolysis of light hydrocarbons[J].I&EC,1987,26(10):2139-2144. [7] ALBRIGHT L,MAREK J.Analysis of coke produced in ethylene furnaces:insights on process improvements[J].I&EC,1988,27(5):751-755. [8] ALBRIGHT L,MAREK J.Mechanistic model for formation of coke in pyrolysis units producing ethylene[J].I&EC,1988,27(5):755-759. [9] REYNIERS G C,FROMENT G F,KOPINKE F D,et al.Coke formation in the thermal cracking of hydrocarbons 4 modeling of coke formation in naphtha cracking[J].I&EC,1994,11(33):2584-2590. [10] GUISNET M,MAGNOUX P.Organic chemistry of coke forma-tion[J].App.Catal.A-Gen,2001,212(23):83-96. [11] APPLEBY W,GIBSON J,GOOD G.Coke formation in catalytic cracking[J].I&EC,1962,1(2):102-110. [12] DEROUANE E,LEMOS F,NACCACHE C,et al.Zeolite mic-roporous solids:synthesis,structure and reactivity[J].NATO ASI Ser,Ser C,1992,352(27):95-102. [13] MAGNOUX P,MACHADO F,GUISNET M,et al.New frontiers in catalysis:Proceeding of the 10th International Congress on Catalysis[C].Studies in Surface Science and Catalysis,Budapest,1992. [14] MILLS G,BOEDEKER E,OBLAD A.Chemical characterization of catalysts.I.Poisoning of cracking catalysts by nitrogen compounds and potassium ion[J].JACS,1950,72(4):1554-1560. [15] 马名杰,张胜局,闫燕,等.焦炭结构的研究进展[J].中国煤炭,2006,32(8):54-60. [16] BROOKS J,TAYLOR G.The formation of graphitizing carbons from the liquid phase[J].Carbon,1965,3(2):185-193. [17] 李生华,刘晨光,阙国和,等.渣油热反应体系中第二液相的存在性I渣油热反应体系中的相分离[J].燃料化学学报,1996,24(6):473-478. [18] 李生华,刘晨光,阙国和,等.渣油热反应体系中第二液相的存在性II第二液相及其表征[J].燃料化学学报,1997,25(1):1-6. [19] 查庆芳,李学军.针状焦形成的基本原理[C].北京:中国金属学会炭素材料分会2007年年会,2007. [20] 王安华,寇亮,晁可绳.影响延迟焦化装置加热炉长周期运行的因素[J].石化技术,2009,16(3):63-67. [21] 刘淑芳.原料劣质化对延迟焦化炉管结焦的影响[J].广州化工,2012,40(16):171-173. [22] 张龙力,杨国华,张庆轩,等.渣油胶体稳定性与热反应生焦性能的关系[J].石油化工高等学校学报,2005,15(1):4-6. [23] 郭爱军.饱和烃促进渣油热反应初期生焦的考察[J].燃料化学学报,2001,29(5):408-412. [24] 李星,李丹,杨学远,等.石脑油中氧含量高对预加氢系统的影响及应对措施[J].石化技术,2013,20(1):58-60. [25] 张建明,王新平,谢鹏,等.渣油FCC改性Y沸石研究[J].燃料化学学报,2006,34(3):319-323. [26] 车春霞,颉伟,谭都平,等.碱土金属镁对乙炔前加氢催化剂性能的影响[J].工业催化,2010,18(12):42-44. [27] 王继乾,李明,李庶峰,等.碳质颗粒添加物对渣油热反应生焦的影响[J].燃料化学学报,2006,34(1):36-41. [28] 李明,王继乾,邓文安,等.Fe/炭黑、Ni/炭黑催化剂对渣油加氢反应的影响[J].燃料化学学报,2007,35(5):558-562. [29] 曹江林,吴冰.甘油为供氢剂水热轻质化重油的基础研究[J/OL].中国科技论文在线,2013-02-27.http://www.paper.edu.cn/html/releasepaper/2013/02/485/. [30] 郏景省,王申祥,王红霞,等.硅铬复合氧化物抗结焦涂层的制备及其性能[J].石油化工,2014,43(4):364-368. [31] 王宗贤,耿亚平,郭爱军,等.馏分循环对延迟焦化加热炉管结焦规律影响的实验研究[J].石油炼制与化工,2010,41(9):65-71. [32] 胡敏,刘为民.催化裂化装置沉降器结焦与防治对策[J].炼油技术与工,2013,43(6):26-33. |