[1] 刘鹏飞. 半再生催化重整全流程模拟与优化[D]. 大连:大连理工大学,2015. LIU P F. The simulation and optimization of semi-regenerative catalytic[D]. Dalian:Dalian University of Technology,2015.
[2] 李睿,胡翔.化工流程模拟技术研究进展[J]. 化工进展,2014,33(sl):27-31. LI R,HU X. Research progress of chemical process simulation technology[J]. Chemical Industry and Engineering Process,2014,33(sl):27-31.
[3] 郭彦,龚燕,刘维康,等.连续重整装置节能潜力研究[J].山东化工,2014,43(3):147-149. GUO Y,GONG Y,LIU W K,et al. Study on energy saving potentiality of continuous catalytic reforming[J]. Shandong Chemical Industry,2014,43(3):147-149.
[4] 梁超. 催化重整反应器建模技术研究[D]. 杭州:浙江工业大学,2013. LIANG C. The study of continuous catalytic reforming reactor modeling[D]. Hangzhou:Zhejiang University of Technology, 2013.
[5] 张锋,成慧禹,姚松涛. 流程模拟软件在连续重整装置的应用与优化[J]. 炼油技术与工程,2013,43(3):56-60. ZHANG F,CHENG H Y,YAO S T,et al. Application of process simulation software in continuous catalytic reforming unit and optimization[J]. Petroleum Refinery Engineering,2013,43(3):56-60.
[6] 龚燕,张鸿山,王广河,等.催化重整装置节能增效优化方案研究[J].广东化工,2016,43(12):212-213. GONG Y,ZHANG H S,WANG G H,et al. Study on optimization projects of energy conservation and profit improvement for catalytic reforming unit[J]. Guangdong Chemical Industry,2016,43(12):212-213.
[7] 徐晓军. 塔河石化重整装置工艺过程模拟和研究[J]. 中外能源,2011,16(sl):34-38. XU X J. Process simulation and study for Sinopec Tahe company's reforming unit[J]. Sino-Global Energy,2011,16(sl):34-38.
[8] 汪宗麒. 镇海炼化连续重整装置流程模拟与优化[J]. 中外能源,2011,16(sl):39-43. WANG Z Q. Process simuIation and optimization for Sinopec Zhenhai refining and chemical company's continuous reforming unit[J]. Sino-Global Energy,2011,16(sl):39-43.
[9] 杨磊,刘建,王岩,等.催化重整装置原料优化对反应收率和能耗的影响研究[J]. 计算机与应用化学,2013,30(8):867-870. YANG L,LIU J,WANG Y,et al. Study on the reaction of feedstock optimization for the yield and energy consumption of catalytic reforming unit[J]. Computers and Applied Chemistry,2013,30(8):867-870. |