摘要
采用Aspen HYSYS模拟软件对石蜡基原油的减压蜡油分别进行催化裂化、催化裂解、催化轻循环油加氢-催化裂解(HTMP)和加氢裂化(HCR)等加工方案的模拟,对比了不同加工方案下的柴汽比、主要产品收率等关键技术指标以及在不同原油价格(以布伦特原油80美元/桶为基准)下的经济效益。结果表明:在技术方面,HTMP加工方案的柴汽比最低(为0.18),氢耗和能耗居中,高价值产品收率和年生产总值最高,HCR加工方案氢耗、能耗、综合商品率和基本化工原料收率均高于其他加工方案;在经济效益方面,与其他加工方案相比,HTMP加工方案的净现值、内部收益率均最高,投资回收周期最短,投资回报率最高,抗风险能力最强。
Aspen-HYSYS software has been used to systematically investigate several typical processing schemes for paraffin-based vacuum gas oil(VGO), including fluid catalytic cracking, deep catalytic cracking, coupled hydrotreating-fluid catalytic cracking(HTMP), and hydrocracking.Economic benifits under different crude oil prices(based on the Brent Oil price 80 USD/bbl) have been compared over different processing routines focusing on differences of diesel to gasoline ratio, key products yield and etc.The results showed that in terms of technical performance,the HTMP process had the highest high value product yield and total annual output value and the lowest diesel-to-gasoline ratio. The hydrogen consumption, energy consumption of the HTMP process were in the middle. The hydrogen consumption, energy consumption, comprehensive commodity rate and basic chemical raw material yield of HCR processing scheme were higher than those of other processing schemes. As for economic performance, compared with other processing schemes, HTMP processing scheme had the highest net present value and internal rate of return, the shortest investment recovery cycle, the highest return on investment and the strongest anti risk ability.
作者
周鑫
赵辉
刘登峰
杨朝合
ZHOU Xin;ZHAO Hui;LIU Deng-feng;YANG Chao-he(State Key Laboratory of Heavy Oil Processing of China University of Petroleum,Qingdao 266580,China;East China Design Branch of CPECC,PetroChina,Qingdao 266071,China)
出处
《石化技术与应用》
CAS
2020年第2期137-141,共5页
Petrochemical Technology & Application
基金
国家自然科学基金资助项目(项目编号:21476263,U1462205)
中央高校基本科研业务费专项资金资助项目(项目编号:18CX06069A)。
关键词
石蜡基减压蜡油
加工方案
ASPEN
HYSYS软件
催化裂化
催化裂解
加氢裂化
技术经济
paraffin-based vacuum gas oil
processing scheme
Aspen HYSYS software
fluid catalytic cracking
deep catalytic cracking
hydrocracking
techno-economic