发明公开
KR1020030051374A 중간 증류물 비등범위에서 외부 공급원료와 혼합되어마일드 수소첨가분해장치 및 감압경유 수소처리장치로부터고품질의 중간 증류물을 제조하는 방법
失效 - Ended
基本信息:
- 专利标题: 중간 증류물 비등범위에서 외부 공급원료와 혼합되어마일드 수소첨가분해장치 및 감압경유 수소처리장치로부터고품질의 중간 증류물을 제조하는 방법
- 专利标题(英):Process for the Production of High Quality Middle Distillates from Mild Hydrocrackers and Vacuum Gas Oil Hydrotreaters in Combination with External Feeds in the Middle Distillate Boiling Range
- 专利标题(中):使用外部材料在中等沸点范围内使用外部材料的微波加氢装置和从真空轻油加氢装置生产高质量中间馏分的方法
- 申请号:KR1020020080805 申请日:2002-12-17
- 公开(公告)号:KR1020030051374A 公开(公告)日:2003-06-25
- 发明人: 묵허지우잘쿠마르 , 루이웨이승더블유. , 달버그아더제이.
- 申请人: 셰브런 유.에스.에이.인크.
- 申请人地址: 미합중국 ***** 캘리포니아주 샌래몬 볼링거 캐년 로드 ****
- 专利权人: 셰브런 유.에스.에이.인크.
- 当前专利权人: 셰브런 유.에스.에이.인크.
- 当前专利权人地址: 미합중국 ***** 캘리포니아주 샌래몬 볼링거 캐년 로드 ****
- 代理人: 황주명
- 优先权: US10/025,411 2001-12-17
- 主分类号: C10G69/08
- IPC分类号: C10G69/08
摘要:
PURPOSE: Provided are a mild hydrocracking apparatus using external material in the boiling range of middle distillates and a method for producing high quality middle distillates from a vacuum light oil hydrotreating apparatus. CONSTITUTION: The method includes the steps of: (a) passing a hydrocarbonaceous feedstock to a first hydroprocessing zone having one or more beds containing hydroprocessing catalyst; (b) passing the effluent of step (a) directly to a hot high pressure separator; (c) passing the vapor stream from step (b) after cooling and partial condensation to a hot hydrogen stripper containing at least one bed of hydrotreating catalyst; (d) passing the overhead vapor stream from the hot hydrogen stripper of step (c), after cooling and contacting with water, to a first cold high pressure separator; (e) passing the liquid stream from the hot hydrogen stripper of step (c) to a bed of hydroprocessing catalyst in the second reactor stage; (f) passing the overhead from the cold high pressure separator of step (d) to an amine absorber; (g) passing the separator bottoms of step (b) to a second reaction stage; (h) passing the vapor stream of step (g) after cooling to a second cold high-pressure separator; (i) passing the liquid effluent of step (g) after cooling to the cold high-pressure separator of step (h) to separate hydrogen and light hydrocarbonaceous gases from the liquid effluent; (j) passing the vapor stream from steps (h) and (i) after further cooling and separation of condensate, to the make-up hydrogen compressor; (k) passing the compressed hydrogen from the make-up hydrogen compressor to the primary reactor loop; and (l) passing the liquid effluent from steps (h) and (i) to the fractionation system.
摘要(中):
目的:提供一种在中间馏分沸腾范围内使用外部材料的轻度加氢裂化装置,以及从真空轻油加氢处理装置生产高品质中间馏分的方法。 方法:该方法包括以下步骤:(a)将烃原料送至具有一个或多个含有加氢处理催化剂的床的第一加氢处理区; (b)将步骤(a)的流出物直接通入热高压分离器; (c)在冷却和部分冷凝之后使来自步骤(b)的蒸汽流通到含有至少一个加氢处理催化剂床的热氢汽提塔; (d)在冷却并与水接触之后,将来自步骤(c)的热氢汽提器的塔顶蒸气流送至第一冷高压分离器; (e)将来自步骤(c)的热氢汽提器的液流从第二反应器阶段通入加氢处理催化剂床; (f)将塔顶馏出物从步骤(d)的冷高压分离器送入胺吸收器; (g)将步骤(b)的分离器底部通入第二反应阶段; (h)冷却后将步骤(g)的蒸气流通入第二冷高压分离器; (i)冷却后将步骤(g)的液体流出物送入步骤(h)的冷高压分离器,以从液体流出物中分离氢气和轻质烃类气体; (j)在进一步冷却和分离冷凝物之后将来自步骤(h)和(i)的蒸气流送至补充氢气压缩机; (k)将压缩的氢气从补充氢压缩机传递到主反应器回路; 和(l)将来自步骤(h)和(i)的液体流出物送至分馏系统。