[1] 李大东.四大技术系列拓宽炼油业未来发展空间[J].中国石油企业, 2018, (Z1):27-30</br>[2]宋明超,张俊晓,雷亮,等.延迟焦化装置防结焦技术改造[J].山东化工, 2019, 48(15):130-131</br>[3]傅钢强.焦化装置油气携带大量泡沫焦的原因分析和对策[J].炼油技术与工程, 2015, 45(10):13-16</br>[4]胡尧良.焦炭塔油气携带泡沫焦的分析及抑制措施[J].炼油技术与工程, 2010, 40(3):1-5</br>[5] 杨军卫, 王兰娟, 肖家治, 等.焦化原料起泡性能评价[C]//山东石油学会炼制委员会.山东石油学会炼制委员会2009年技术交流会论文集.山东石油学会炼制委员会:山东省科学技术协会,2009:41-45.</br>[6] Pugh, R.J..Foaming, foam films, antifoaming and defoaming[J].Advances in Colloid and Interface Science, 1996, 64:69-142</br>[7] Colton, J.S, Suh, N. P..Nucleation of Microcellular Foam: Theory and Practice[J].Polymer Engineering and Science, 1987, 27(7):500-503</br>[8] OOLMAN, T.O., BLANCH, H. W.. Bubble coalescence in stagnant liquids[J].Chemical Engineering communications, 1986, 43(4):237-261</br>[9] Chan, D. Y. C., Klaseboer, E., Manica, R..Theory of non-equilibrium force measurements involving deformable drops and bubbles[J].Advances in Colloid and Interface Science, 2011, 165(2):70-90</br>[10] Lemlich, R..Prediction of Changes in Bubble Size Distribution Due to Interbubble Gas Diffusion in Foam[J].Industrial & Engineering Chemistry Fundamentals, 1978, 17(2):89-93</br>[11] 孙汉华.稠油焦化泡沫抑制机制研究与抑制剂开发[D].中国石油大学(华东),2013.</br>[12]Asprino, O.J.,Elliott,JA. W.,McCaffrey,W. C.,et al. Fluid Properties of Asphaltenes at 310?530 °C[J].Energy & Fuels, 2005, 19(5):2026-2033</br>[13]Bauget, F.Langevin,D,Lenormand,R.. Dynamic Surface Properties of Asphaltenes and Resins at the Oil-Air Interface[J].Colloid and Interface Science, 2001, 239(2):501-508</br>[14]Kilpatrick, P.K.. Water-in-Crude Oil Emulsion Stabilization: Review and Unanswered Questions[J].Energy & Fuels, 2012, 26(7):4017-4026</br>[15]Blázquez, C, Dalmazzone, C., Emond, E., et al. .Crude oil foams Crude oil foams. Part 1 – A novel methodology for studying non-aqueous foams formed by depressurization[J].Fuel, 2016, 171:224-237</br>[16]陶春风.延迟焦化装置长周期生产中存在的问题及解决措施[J].石油炼制与化工, 2000, 31(2):17-22</br>[17]程玉桥.胜利油田单家寺油区稠油物理化学性质研究[D].浙江:浙江大学,2002.</br>[18]孙利, 沈本贤.射线衍射法研究石油焦碳化过程的微晶变化[J].石油学报(石油加工), 2004, 20(2):53-56</br>[19]Binks, B.P.,Rocher,A,Kirkland,M.. Oil foams stabilised solely by particles[J].Soft Matter, 2011, 7(5):1800-1808</br>[20]马宝岐,孙风顺.三相泡沫特性的研究[J].油田化学, 1992, 9(3):238-242</br>[21]瞿国华.延迟焦化工艺与工程[M].第二版.北京:中国石化出版社,2017:421-425+256.</br>[22]郭小安,张德龙,龚文武,等.延迟焦化装置焦炭塔挥发线结焦原因及预防措施[J].石油与天然气化工, 2011, 40(5):451-455</br>[23]颜峰,谢崇亮,董罡,等.延迟焦化装置掺炼催化裂化油浆的影响及优化设计[J].石油炼制与化工, 2014, 45(8):49-53</br>[24]王洪彬,韩海波,江莉,等.循环比对塔河常压渣油延迟焦化工艺过程的影响[J].石油炼制与化工, 2016, 47(1):58-61</br>[25]Aminu, M.O.,Elliott,JA.W.,McCaffrey,W. C.,et al. Fluid Properties at Coking Process Conditions[J].Industrial & Engineering Chemistry Research, 2004, 43(12):2929-2935</br>[26]黄新龙,王宝石,李晋楼,等.降低焦炭塔操作压力对焦化过程的影响[J].石油炼制与化工, 2019, 50(4):16-19</br>[27]王玉章,李云龙,李锐,等.延迟焦化消泡剂的应用[J].石油炼制与化工, 2001, 32(4):17-19</br>[28]杨楠.消泡剂在延迟焦化过程中的应用[J].扬子石油化工, 2007, 22(1):5-8</br>[29]王鑫,孙鹏,刘纾言,等.延迟焦化消泡剂消泡性能及硅污染的研究[J].橡塑技术与装备, 2016, 42(14):15-17</br>[30]刘公召,霍巍.延迟焦化无硅消泡剂的研制与工业应用[J].炼油技术与工程, 2006, 36(1):56-58</br>[31]赵蓓蓓,杨超,张喜文,等.延迟焦化低硅消泡剂的研制[J].石油炼制与化工, 2012, 43(9):25-28</br> |