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1. 发明授权

US08696887B2 Catalytic conversion process 有权
标题翻译：催化转化过程
公开(公告)号：US08696887B2
公开(公告)日：2014-04-15
申请号：US12672666
申请日：2008-08-07
申请人： Youhao Xu , Lishun Dai , Longsheng Tian , Shouye Cui , Jianhong Gong , Chaogang Xie , Jiushun Zhang , Jun Long , Zhijian Da , Hong Nie , Jinbiao Guo , Zhigang Zhang
发明人： Youhao Xu , Lishun Dai , Longsheng Tian , Shouye Cui , Jianhong Gong , Chaogang Xie , Jiushun Zhang , Jun Long , Zhijian Da , Hong Nie , Jinbiao Guo , Zhigang Zhang
IPC分类号： C10G11/00
CPC分类号： B01J29/084 , B01J29/46 , B01J29/80 , B01J29/90 , B01J37/0045 , B01J38/30 , B01J2229/42 , C10G11/05 , C10G11/18 , C10G2300/104 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4018 , C10G2300/4025 , C10G2300/4093 , C10G2400/02 , C10G2400/06 , C10G2400/20
摘要： A catalytic conversion process which comprises catalytic cracking reaction of a hydrocarbon feedstock contacting with a medium pore size zeolite enriched catalyst in a reactor, characterized in that reaction temperature, weight hourly space velocity and catalyst/feedstock ratio by weight are sufficient to achieve a yield of fluid catalytic cracking gas oil between 12% and 60% by weight of said feedstock, wherein said weight hourly space velocity is between 25 h−1 and 100 h−1, said reaction temperature is between 450° C. and 600° C., and said catalyst/feedstock ratio by weight is between 1 and 30. This invention relates to a catalytic conversion process, especially for heavy feedstock oil to produce higher octane gasoline and an enhanced yield of propylene. More particularly, the invention relates to a process to utilize petroleum oil resources efficiently for decreasing the yield of dry gas and coke significantly.
摘要翻译：催化转化方法，其包括在反应器中与中等孔径的沸石富集催化剂接触的烃原料的催化裂化反应，其特征在于反应温度，重量时空速和催化剂/原料重量比足以实现流化催化裂化瓦斯油在所述原料的12重量％至60重量％之间，其中所述重时空速在25h -1和100h -1之间，所述反应温度在450℃和600℃之间，并且所述催化剂/原料的重量比在1和30之间。本发明涉及催化转化方法，特别是用于重质原料油生产高辛烷值汽油和提高丙烯收率的方法。更具体地说，本发明涉及一种利用石油资源有效降低干燥气体和焦炭产率的方法。

2. 发明申请

US20100213102A1 CATALYTIC CONVERSION PROCESS 有权
标题翻译：催化转化过程
公开(公告)号：US20100213102A1
公开(公告)日：2010-08-26
申请号：US12672666
申请日：2008-08-07
申请人： Youhao Xu , Lishun Dai , Longsheng Tian , Shouye Cui , Jianhong Gong , Chaogang Xie , Jiushun Zhang , Jun Long , Zhijian Da , Hong Nie , Jinbiao Guo , Zhigang Zhang
发明人： Youhao Xu , Lishun Dai , Longsheng Tian , Shouye Cui , Jianhong Gong , Chaogang Xie , Jiushun Zhang , Jun Long , Zhijian Da , Hong Nie , Jinbiao Guo , Zhigang Zhang
IPC分类号： C10G57/00 , C10G11/05
CPC分类号： B01J29/084 , B01J29/46 , B01J29/80 , B01J29/90 , B01J37/0045 , B01J38/30 , B01J2229/42 , C10G11/05 , C10G11/18 , C10G2300/104 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4018 , C10G2300/4025 , C10G2300/4093 , C10G2400/02 , C10G2400/06 , C10G2400/20
摘要： A catalytic conversion process which comprises catalytic cracking reaction of a hydrocarbon feedstock contacting with a medium pore size zeolite enriched catalyst in a reactor, characterized in that reaction temperature, weight hourly space velocity and catalyst/feedstock ratio by weight are sufficient to achieve a yield of fluid catalytic cracking gas oil between 12% and 60% by weight of said feedstock, wherein said weight hourly space velocity is between 25 h−1 and 100 h−1, said reaction temperature is between 450° C. and 600° C., and said catalyst/feedstock ratio by weight is between 1 and 30. This invention relates to a catalytic conversion process, especially for heavy feedstock oil to produce higher octane gasoline and an enhanced yield of propylene. More particularly, the invention relates to a process to utilize petroleum oil resources efficiently for decreasing the yield of dry gas and coke significantly.
摘要翻译：催化转化方法，其包括在反应器中与中等孔径的沸石富集催化剂接触的烃原料的催化裂化反应，其特征在于反应温度，重量时空速和催化剂/原料重量比足以实现流化催化裂化瓦斯油在所述原料的12重量％至60重量％之间，其中所述重时空速在25h -1和100h -1之间，所述反应温度在450℃和600℃之间，并且所述催化剂/原料的重量比在1和30之间。本发明涉及催化转化方法，特别是用于重质原料油生产高辛烷值汽油和提高丙烯收率的方法。更具体地说，本发明涉及一种利用石油资源有效降低干燥气体和焦炭产率的方法。

3. 发明授权

US08597500B2 Process for converting inferior feedstock to high quality fuel oil 有权
标题翻译：将劣质原料转化为优质燃料油的方法
公开(公告)号：US08597500B2
公开(公告)日：2013-12-03
申请号：US12921436
申请日：2009-03-13
申请人： Youhao Xu , Lishun Dai , Zhigang Zhang , Shouye Cui , Jianhong Gong , Chaogang Xie , Jun Long , Hong Nie , Zhijian Da , Jiushun Zhang , Tao Liu , Anguo Mao
发明人： Youhao Xu , Lishun Dai , Zhigang Zhang , Shouye Cui , Jianhong Gong , Chaogang Xie , Jun Long , Hong Nie , Zhijian Da , Jiushun Zhang , Tao Liu , Anguo Mao
IPC分类号： C10G11/00
CPC分类号： C10G55/06 , C10G11/18 , C10G67/0409 , C10G69/04 , C10G2300/1033 , C10G2300/104 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1077 , C10G2300/203 , C10G2300/205 , C10G2300/308 , C10G2300/4018 , C10G2300/4025 , C10G2300/4093 , C10G2300/44 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/28
摘要： A catalytic conversion process to convert inferior feedstock to high quality fuel oil and propylene is disclosed. Inferior feedstock is introduced into first and second reactor zone, wherein first step and second step reactions occur by contacting with catalytic conversion catalyst. Product vapors include fluid catalytic cracking gas oil (FGO) which is introduced into a hydrotreating unit and/or extraction unit to obtain hydrotreated FGO and/or extracted FGO. Hydrotreated FGO and/or extracted FGO returns to the first reactor zone and/or another catalytic cracking unit to obtain propylene and gasoline. The extracted oil of said FGO is rich in double ring aromatics and the raffinate of said FGO is rich in chain alkane and cycloalkane. More particularly, the invention utilizes petroleum oil resources efficiently for decreasing the yield of dry gas and coke significantly.
摘要翻译：公开了将劣质原料转化为高质量燃料油和丙烯的催化转化方法。将不良原料引入第一和第二反应器区，其中通过与催化转化催化剂接触进行第一步和第二步反应。产物蒸气包括流化催化裂化瓦斯油（FGO），其被引入加氢处理单元和/或提取单元以获得加氢处理的FGO和/或提取的FGO。加氢处理的FGO和/或提取的FGO返回到第一反应器区和/或另一个催化裂化单元以获得丙烯和汽油。所述FGO的提取油富含双环芳族化合物，所述FGO的残油富含链烷烃和环烷烃。更具体地说，本发明有效地利用石油资源，显着降低干气和焦炭的产率。

4. 发明申请

US20110000818A1 PROCESS FOR CONVERTING INFERIOR FEEDSTOCK TO HIGH QUALITY FUEL OIL 有权
标题翻译：将惰性饲料转化为高品质燃油的方法
公开(公告)号：US20110000818A1
公开(公告)日：2011-01-06
申请号：US12921436
申请日：2009-03-13
申请人： Youhao Xu , Lishun Dai , Zhigang Zhang , Shouye Cui , Jianhong Gong , Chaogang Xie , Jun Long , Hong Nie , Zhijian Da , Jiushun Zhang , Tao Liu , Anguo Mao
发明人： Youhao Xu , Lishun Dai , Zhigang Zhang , Shouye Cui , Jianhong Gong , Chaogang Xie , Jun Long , Hong Nie , Zhijian Da , Jiushun Zhang , Tao Liu , Anguo Mao
IPC分类号： C10G57/00
CPC分类号： C10G55/06 , C10G11/18 , C10G67/0409 , C10G69/04 , C10G2300/1033 , C10G2300/104 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1077 , C10G2300/203 , C10G2300/205 , C10G2300/308 , C10G2300/4018 , C10G2300/4025 , C10G2300/4093 , C10G2300/44 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/28
摘要： A catalytic conversion process can convert inferior feedstock to high quality fuel oil and propylene. A inferior feedstock is introduced into first and second reactor zone, wherein the feedstock carry out first step and second step reactions by contacting with catalytic conversion catalyst. Product vapors separate from spent catalyst by gas-solid separation. The spent catalyst is stripped, regenerated by burning off coke and then returns to reactor. The product vapors are introduced into separation system to obtain propylene, gasoline, diesel, fluid catalytic cracking gas oil (FGO) and other products. The FGO is introduced into hydrotreating unit and/or extraction unit to obtain hydrotreated FGO and/or extracted FGO. Said hyrotreated FGO and/or extracted FGO return to the first reactor zone and/or another catalytic cracking unit to obtain propylene and gasoline. The extracted oil of said FGO is rich in double ring aromatics which are good chemical materials. The raffinate of said FGO is rich in chain alkane and cycloalkane which are suitable for catalytic cracking. More particularly, the invention relates to a process to utilize petroleum oil resources efficiently for decreasing the yield of dry gas and coke significantly.
摘要翻译：催化转化过程可以将劣质原料转化为高质量的燃料油和丙烯。将劣质原料引入第一和第二反应器区，其中原料通过与催化转化催化剂接触进行第一步和第二步反应。产物蒸气通过气 - 固分离与废催化剂分离。废弃的催化剂被汽提，通过燃烧焦炭再生，然后返回反应器。将产品蒸气引入分离系统中，得到丙烯，汽油，柴油，流化催化裂化瓦斯油（FGO）等产品。将FGO引入加氢处理单元和/或提取单元以获得加氢处理的FGO和/或提取的FGO。所述经处理的FGO和/或提取的FGO返回到第一反应器区和/或另一个催化裂化装置以获得丙烯和汽油。所述FGO的提取油富含双环芳族化合物，其为良好的化学物质。所述FGO的萃余液富含链烷烃和环烷烃，适用于催化裂化。更具体地说，本发明涉及一种利用石油资源有效降低干燥气体和焦炭产率的方法。

5. 发明授权

US09309467B2 Integrated process for hydrogenation and catalytic cracking of hydrocarbon oil 有权
标题翻译：碳氢化合物氢化和催化裂解的综合工艺
公开(公告)号：US09309467B2
公开(公告)日：2016-04-12
申请号：US12809516
申请日：2008-12-19
申请人： Yongcan Gao , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
发明人： Yongcan Gao , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
IPC分类号： C10G11/18 , C10G51/06 , C10G69/04
CPC分类号： C10G11/18 , C10G11/182 , C10G51/06 , C10G69/04 , C10G2300/1037 , C10G2300/107 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/70 , C10G2300/807 , C10G2400/02 , C10G2400/04 , C10G2400/28
摘要： Disclosed is a combination process for improved hydrotreating and catalytic cracking of hydrocarbon oils, including: contacting residual oil, catalytic cracking cycle oil, and optional distillate oil with a hydrotreating catalyst under hydrotreating conditions in the presence of hydrogen followed by separation of the reaction products to obtain gas, hydrogenated naphtha, hydrogenated diesel oil, and hydrogenated tail oil; contacting the hydrogenated tail oil and optional normal catalytic cracking feedstock oil with a cracking catalyst under catalytic cracking conditions followed by separation of the reaction products to obtain dry gas, hydrogenated naphtha, liquefied petroleum gas, catalytic cracked gasoline, catalytic cracked diesel oil, and catalytic cracking cycle oil; wherein the hydrogenated tail oil and/or normal catalytic cracking feedstock oil are separated into at least two fractions, the light and the heavy fractions or normal catalytic cracking heavy feedstock oil and normal catalytic cracking light feedstock oil, prior to contacting the hydrogenated tail oil and/or normal catalytic cracking feedstock oil with the cracking catalyst. The process according to the present invention is especially suitable for conversion of hydrocarbon oils to produce more products of gasoline or diesel oil.
摘要翻译：公开了用于改进烃油的加氢处理和催化裂化的组合方法，包括：在加氢处理条件下在氢气存在下，用加氢处理催化剂将残油，催化裂化循环油和任选的馏出油接触，然后将反应产物分离获得气体，氢化石脑油，氢化柴油和氢化尾油; 在催化裂化条件下使氢化尾油和任选的常规催化裂化原料油与裂化催化剂接触，然后分离反应产物，得到干燥气体，氢化石脑油，液化石油气，催化裂化汽油，催化裂化柴油和催化剂开裂循环油; 其中所述氢化尾油和/或常规催化裂化原料油在将氢化尾油与氢化尾油接触之前分离成至少两个馏分，轻馏分或重馏分或正常催化裂化重原料油和常规催化裂化轻原料油， /或正常催化裂化原料油与裂化催化剂。根据本发明的方法特别适用于烃油的转化以产生更多的汽油或柴油的产物。

6. 发明授权

US09260667B2 Combined process of hydrotreating and catalytic cracking of hydrocarbon oils 有权
标题翻译：烃油的加氢处理和催化裂化的组合方法
公开(公告)号：US09260667B2
公开(公告)日：2016-02-16
申请号：US13618759
申请日：2012-09-14
申请人： Yongcan Gao , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
发明人： Yongcan Gao , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
IPC分类号： C10G11/00 , C10G11/18 , C10G51/06 , C10G69/04
CPC分类号： C10G11/18 , C10G11/182 , C10G51/06 , C10G69/04 , C10G2300/1037 , C10G2300/107 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/70 , C10G2300/807 , C10G2400/02 , C10G2400/04 , C10G2400/28
摘要： Disclosed is a combination process for improved hydrotreating and catalytic cracking of hydrocarbon oils, including: contacting residual oil, catalytic cracking cycle oil, and optional distillate oil with a hydrotreating catalyst under hydrotreating conditions in the presence of hydrogen followed by separation of the reaction products to obtain hydrogenated tail oil and other products; contacting the hydrogenated tail oil and optional normal catalytic cracking feedstock oil with a cracking catalyst under catalytic cracking conditions followed by separation of the reaction products; wherein the hydrogenated tail oil and/or normal catalytic cracking feedstock oil are separated into at least two fractions prior to contacting the hydrogenated tail oil and/or normal catalytic cracking feedstock oil with the cracking catalyst.
摘要翻译：公开了用于改进烃油的加氢处理和催化裂化的组合方法，包括：在加氢处理条件下在氢气存在下，用加氢处理催化剂将残油，催化裂化循环油和任选的馏出油接触，然后将反应产物分离获得氢化尾油等产品; 在催化裂化条件下使氢化尾油和任选的常规催化裂化原料油与裂化催化剂接触，然后分离反应产物; 其中在将氢化尾油和/或常规催化裂化原料油与裂化催化剂接触之前，将氢化尾油和/或常规催化裂化原料油分离成至少两个馏分。

7. 发明申请

US20130062250A1 COMBINED PROCESS OF HYDROTREATING AND CATALYTIC CRACKING OF HYDROCARBON OILS 审中-公开
标题翻译：碳氢化合物加氢和催化裂化的组合工艺
公开(公告)号：US20130062250A1
公开(公告)日：2013-03-14
申请号：US13618759
申请日：2012-09-14
申请人： Yongcan GAO , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
发明人： Yongcan GAO , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
IPC分类号： C10G69/04
CPC分类号： C10G11/18 , C10G11/182 , C10G51/06 , C10G69/04 , C10G2300/1037 , C10G2300/107 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/70 , C10G2300/807 , C10G2400/02 , C10G2400/04 , C10G2400/28
摘要： Disclosed is a combination process for improved hydrotreating and catalytic cracking of hydrocarbon oils, including: contacting residual oil, catalytic cracking cycle oil, and optional distillate oil with a hydrotreating catalyst under hydrotreating conditions in the presence of hydrogen followed by separation of the reaction products to obtain hydrogenated tail oil and other products; contacting the hydrogenated tail oil and optional normal catalytic cracking feedstock oil with a cracking catalyst under catalytic cracking conditions followed by separation of the reaction products; wherein the hydrogenated tail oil and/or normal catalytic cracking feedstock oil are separated into at least two fractions prior to contacting the hydrogenated tail oil and/or normal catalytic cracking feedstock oil with the cracking catalyst.
摘要翻译：公开了用于改进烃油的加氢处理和催化裂化的组合方法，包括：在加氢处理条件下在氢气存在下，用加氢处理催化剂将残油，催化裂化循环油和任选的馏出油接触，然后将反应产物分离获得氢化尾油等产品; 在催化裂化条件下使氢化尾油和任选的常规催化裂化原料油与裂化催化剂接触，然后分离反应产物; 其中在将氢化尾油和/或常规催化裂化原料油与裂化催化剂接触之前，将氢化尾油和/或常规催化裂化原料油分离成至少两个馏分。

8. 发明申请

US20110062054A1 IMPROVED INTEGRATED PROCESS FOR HYDROGENATION AND CATALYTIC CRACKING OF HYDROCARBON OIL 有权
标题翻译：油气加氢催化裂化改进综合工艺
公开(公告)号：US20110062054A1
公开(公告)日：2011-03-17
申请号：US12809516
申请日：2008-12-19
申请人： Yongcan Gao , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
发明人： Yongcan Gao , Chaogang Xie , Chuanfeng Niu , Jiushun Zhang , Lishun Dai , Hong Nie , Dadong Li , Jun Long , Jianguo Ma , Yan Cui
IPC分类号： C10G69/04
CPC分类号： C10G11/18 , C10G11/182 , C10G51/06 , C10G69/04 , C10G2300/1037 , C10G2300/107 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/70 , C10G2300/807 , C10G2400/02 , C10G2400/04 , C10G2400/28
摘要： Disclosed is a combination process for improved hydrotreating and catalytic cracking of hydrocarbon oils, including: contacting residual oil, catalytic cracking cycle oil, and optional distillate oil with a hydrotreating catalyst under hydrotreating conditions in the presence of hydrogen followed by separation of the reaction products to obtain gas, hydrogenated naphtha, hydrogenated diesel oil, and hydrogenated tail oil; contacting the hydrogenated tail oil and optional normal catalytic cracking feedstock oil with a cracking catalyst under catalytic cracking conditions followed by separation of the reaction products to obtain dry gas, hydrogenated naphtha, liquefied petroleum gas, catalytic cracked gasoline, catalytic cracked diesel oil, and catalytic cracking cycle oil; wherein the hydrogenated tail oil and/or normal catalytic cracking feedstock oil are separated into at least two fractions, the light and the heavy fractions or normal catalytic cracking heavy feedstock oil and normal catalytic cracking light feedstock oil, prior to contacting the hydrogenated tail oil and/or normal catalytic cracking feedstock oil with the cracking catalyst. The process according to the present invention is especially suitable for conversion of hydrocarbon oils to produce more products of gasoline or diesel oil.
摘要翻译：公开了用于改进烃油的加氢处理和催化裂化的组合方法，包括：在加氢处理条件下在氢气存在下，用加氢处理催化剂将残油，催化裂化循环油和任选的馏出油接触，然后将反应产物分离获得气体，氢化石脑油，氢化柴油和氢化尾油; 在催化裂化条件下使氢化尾油和任选的常规催化裂化原料油与裂化催化剂接触，然后分离反应产物，得到干燥气体，氢化石脑油，液化石油气，催化裂化汽油，催化裂化柴油和催化裂化柴油开裂循环油; 其中所述氢化尾油和/或常规催化裂化原料油在将氢化尾油与氢化尾油接触之前分离成至少两个馏分，轻馏分或重馏分或正常催化裂化重原料油和常规催化裂化轻原料油， /或正常催化裂化原料油与裂化催化剂。根据本发明的方法特别适用于烃油的转化以产生更多的汽油或柴油的产物。

9. 发明授权

US08529753B2 Combined process for hydrotreating and catalytic cracking of residue 有权
标题翻译：渣油加氢处理和催化裂化的综合工艺
公开(公告)号：US08529753B2
公开(公告)日：2013-09-10
申请号：US12521346
申请日：2007-12-27
申请人： Chuanfeng Niu , Lishun Dai , Yongcan Gao , Dadong Li , Yahua Shi , Hong Nie , Qinghe Yang
发明人： Chuanfeng Niu , Lishun Dai , Yongcan Gao , Dadong Li , Yahua Shi , Hong Nie , Qinghe Yang
IPC分类号： C10G69/04
CPC分类号： C10G69/04
摘要： Disclosed is a combined process for hydrotreating and catalytic cracking of residue, wherein the residue, catalytic cracking heavy cycle oil with acidic solid impurity being removed, optional distillate oil and adistillate of catalytic cracking slurry oil from which the acidic solid impurity is removed are fed into residue hydrotreating unit, the hydrogenated residue obtained and optional vacuum gas oil are fed into catalytic cracking unit to obtain various products; the catalytic cracking heavy cycle oil from which the acidic solid impurity is removed is circulated to the residue hydrotreating unit; the catalytic cracking slurry oil is separated by distilling, the distillate of the catalytic cracking slurry oil after removing off the acidic solid impurity is circulated to the residue hydrotreating unit. This process makes the residue hydrotreating and catalytic cracking being combined together more effectively such that it is not only able to improve product quality of the residue hydrotreating, elongate operation cycle of the residue hydrotreating unit, but also increases the yield of the hydrogenated diesel oil and catalytic cracking light oil, and decreases coking quantity of the catalytic cracking.
摘要翻译：公开了一种用于残余物加氢处理和催化裂化的组合方法，其中除去残留物，除去酸性固体杂质的催化裂解重质循环油，任选的馏出油和除去酸性固体杂质的催化裂化浆料油馏出物进入残渣加氢处理装置，将得到的氢化残渣和任选的减压瓦斯油加入催化裂化装置中得到各种产物; 去除酸性固体杂质的催化裂解重质循环油循环至残渣加氢处理装置; 通过蒸馏分离催化裂化浆料油，除去酸性固体杂质后的催化裂化浆料油的馏出物循环至残渣加氢处理装置。该方法使残渣加氢处理和催化裂化更有效地结合在一起，使得不仅能够提高残余物加氢处理装置的残余物加氢处理，延长操作循环的产品质量，而且还提高氢化柴油的产率，催化裂解轻油，降低催化裂化的焦化量。

10. 发明申请

US20100314287A1 COMBINED PROCESS FOR HYDROTREATING AND CATALYTIC CRACKING OF RESIDUE 有权
标题翻译：用于加氢和催化裂化的残留物的组合方法
公开(公告)号：US20100314287A1
公开(公告)日：2010-12-16
申请号：US12521346
申请日：2007-12-27
申请人： Chuanfeng Niu , Lishun Dai , Yongcan Gao , Dadong Li , Yahua Shi , Hong Nie , Qinghe Yang
发明人： Chuanfeng Niu , Lishun Dai , Yongcan Gao , Dadong Li , Yahua Shi , Hong Nie , Qinghe Yang
IPC分类号： C10G69/04
CPC分类号： C10G69/04
摘要： Disclosed is a combined process for hydrotreating and catalytic cracking of residue, wherein the residue, catalytic cracking heavy cycle oil with acidic solid impurity being removed, optional distillate oil and adistillate of catalytic cracking slurry oil from which the acidic solid impurity is removed are fed into residue hydrotreating unit, the hydrogenated residue obtained and optional vacuum gas oil are fed into catalytic cracking unit to obtain various products; the catalytic cracking heavy cycle oil from which the acidic solid impurity is removed is circulated to the residue hydrotreating unit; the catalytic cracking slurry oil is separated by distilling, the distillate of the catalytic cracking slurry oil after removing off the acidic solid impurity is circulated to the residue hydrotreating unit. This process makes the residue hydrotreating and catalytic cracking being combined together more effectively such that it is not only able to improve product quality of the residue hydrotreating, elongate operation cycle of the residue hydrotreating unit, but also increases the yield of the hydrogenated diesel oil and catalytic cracking light oil, and decreases coking quantity of the catalytic cracking.
摘要翻译：公开了一种用于残余物加氢处理和催化裂化的组合方法，其中除去残留物，除去酸性固体杂质的催化裂解重质循环油，任选的馏出油和除去酸性固体杂质的催化裂化浆料油馏出物进入残渣加氢处理装置，将得到的氢化残渣和任选的减压瓦斯油加入催化裂化装置中得到各种产物; 去除酸性固体杂质的催化裂解重质循环油循环至残渣加氢处理装置; 通过蒸馏分离催化裂化浆料油，除去酸性固体杂质后的催化裂化浆料油的馏出物循环至残渣加氢处理装置。该方法使残渣加氢处理和催化裂化更有效地结合在一起，使得不仅能够提高残余物加氢处理装置的残余物加氢处理，延长操作循环的产物质量，而且还可以提高氢化柴油的产率，催化裂解轻油，降低催化裂化的焦化量。

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