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1. 发明授权

US08303804B2 Process to improve jet fuels 有权
标题翻译：改善喷气燃料的工艺
公开(公告)号：US08303804B2
公开(公告)日：2012-11-06
申请号：US12287079
申请日：2008-10-06
申请人： Terry E. Helton , William J. Tracy, III , Michael T. Grove , Dennis H. Hoskin , Philip J. Angevine , David A. Pappal
发明人： Terry E. Helton , William J. Tracy, III , Michael T. Grove , Dennis H. Hoskin , Philip J. Angevine , David A. Pappal
IPC分类号： C10G69/02
CPC分类号： C10G3/00 , B01J29/74 , C10G45/04 , C10G47/18 , C10G65/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/301 , C10G2300/4018 , C10G2400/08 , C10L1/04 , Y02P30/20
摘要： This invention relates to a process for improving the yield and properties of jet fuel from a kerosene feed. More particularly, a kerosene feedstock is hydrotreated and dewaxed using a ZSM-48 catalyst to produce a jet fuel in improved yield and having improved properties.
摘要翻译：本发明涉及一种提高煤油进料的喷气燃料的产率和性能的方法。更具体地，使用ZSM-48催化剂对煤油原料进行加氢处理和脱蜡以产生具有改进的性能的喷射燃料。

2. 发明申请

US20100084313A1 Process to improve jet fuels 有权
标题翻译：改善喷气燃料的工艺
公开(公告)号：US20100084313A1
公开(公告)日：2010-04-08
申请号：US12287079
申请日：2008-10-06
申请人： Terry E. Helton , William J. Tracy, III , Michael T. Grove , Dennis H. Hoskin , Philip J. Angevine , David A. Pappal
发明人： Terry E. Helton , William J. Tracy, III , Michael T. Grove , Dennis H. Hoskin , Philip J. Angevine , David A. Pappal
IPC分类号： C10G69/02
CPC分类号： C10G3/00 , B01J29/74 , C10G45/04 , C10G47/18 , C10G65/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/301 , C10G2300/4018 , C10G2400/08 , C10L1/04 , Y02P30/20
摘要： This invention relates to a process for improving the yield and properties of jet fuel from a kerosene feed. More particularly, a kerosene feedstock is hydrotreated and dewaxed using a ZSM-48 catalyst to produce a jet fuel in improved yield and having improved properties.
摘要翻译：本发明涉及一种提高煤油进料的喷气燃料的产率和性能的方法。更具体地，使用ZSM-48催化剂对煤油原料进行加氢处理和脱蜡以产生具有改进的性能的喷射燃料。

3. 发明申请

US20110132803A1 TWO STAGE HYDROPROCESSING WITH DIVIDED WALL COLUMN FRACTIONATOR 有权
标题翻译：两阶段水力分离与分段墙柱分段
公开(公告)号：US20110132803A1
公开(公告)日：2011-06-09
申请号：US12946353
申请日：2010-11-15
申请人： Benjamin S. Umansky , Berne K. Stober , Carlos N. Lopez , Stuart S. Shih , Timothy L. Hilbert , Andre T. Sims , William J. Tracy, III , Akira Murata , Paul W. Kamienski
发明人： Benjamin S. Umansky , Berne K. Stober , Carlos N. Lopez , Stuart S. Shih , Timothy L. Hilbert , Andre T. Sims , William J. Tracy, III , Akira Murata , Paul W. Kamienski
IPC分类号： C10G65/02 , C10G67/02
CPC分类号： C10G45/02 , B01D3/141 , C10G7/00 , C10G47/00 , C10G65/043 , C10G65/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/202 , C10G2300/304 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/04 , Y02P30/20
摘要： A divided wall column allows for fractionation of multiple streams while maintaining separate product qualities. Effluents from multiple stages of a reaction system can be processed in a single divided wall column. The divided wall column can produce multiple cuts from each separated area, as well as at least one output from a common area.
摘要翻译：分隔壁柱允许分离多个流，同时保持单独的产品质量。来自反应体系的多个阶段的流出物可以在单个分隔壁塔中进行处理。分隔壁柱可以从每个分离的区域产生多个切割，以及从公共区域产生至少一个输出。

4. 发明授权

US09447339B2 Hydroprocessing of biodiesel fuels and blends 有权
标题翻译：生物柴油和混合物的加氢处理
公开(公告)号：US09447339B2
公开(公告)日：2016-09-20
申请号：US13127875
申请日：2008-11-06
申请人： William J. Novak , Zhiguo Hou , William J. Tracy, III , Patrick L. Hanks , Timothy L Hilbert
发明人： William J. Novak , Zhiguo Hou , William J. Tracy, III , Patrick L. Hanks , Timothy L Hilbert
IPC分类号： C10L1/10 , C10L1/00 , C10L1/18 , C10L1/02 , C10G45/64
CPC分类号： C10L1/08 , C10G45/64 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/307 , C10G2300/4018 , C10G2400/04 , C10L1/026 , C10L2200/0469 , C10L2270/026 , C10L2290/06 , C10L2290/54 , Y02E50/13 , Y02P30/20
摘要： A method for producing diesel fuel from biocomponent feeds includes hydrotreating the feed followed by catalytic dewaxing with a ZSM-48 containing catalyst. The hydrotreated feed may be cascaded directly to the dewaxing step, or the hydrotreated feed can undergo intermediate separation. The diesel fuel resulting from processing of the biocomponent feed exhibits superior cetane values.
摘要翻译：从生物组分进料生产柴油燃料的方法包括用含ZSM-48的催化剂加氢处理进料，然后进行催化脱蜡。加氢处理的进料可以直接级联到脱蜡步骤，或加氢处理的进料可以进行中间分离。由生物组分进料加工产生的柴油表现出优异的十六烷值。

5. 发明申请

US20120156111A1 CATALYST BED PLATFORM WITH CENTER SUPPORT PIPE 有权
标题翻译：催化床平台与中心支撑管
公开(公告)号：US20120156111A1
公开(公告)日：2012-06-21
申请号：US13325148
申请日：2011-12-14
申请人： Antonio O. Ramos , Benjamin S. Umansky , William J. Tracy, III , Ramesh X. Gandhi , Hans G. Korsten , Enrique Feliz
发明人： Antonio O. Ramos , Benjamin S. Umansky , William J. Tracy, III , Ramesh X. Gandhi , Hans G. Korsten , Enrique Feliz
IPC分类号： B01J8/44 , B23P11/00
CPC分类号： B01J8/008 , B01J8/0015 , B01J8/003 , B01J8/0035 , B01J8/02 , B01J8/025 , B01J8/0453 , B01J2208/00884 , B01J2208/00938 , B01J2219/00024 , B01J2219/185 , Y10T29/49826
摘要： A structure and method are provided for adding a catalyst bed platform to an existing reactor without welding to the structural portion of the reactor walls. The structure is constructed from components that can be passed through an existing opening in a reactor. The structure allows a catalyst bed in an existing reactor to be divided into catalyst beds with a reduced length to diameter ratio.
摘要翻译：提供了一种用于将催化剂床平台添加到现有反应器而不与反应器壁的结构部分焊接的结构和方法。该结构由可以通过反应器中的现有开口的部件构成。该结构允许将现有反应器中的催化剂床分成具有减小的长径比的催化剂床。

6. 发明授权

US07713407B2 Production of low sulfur fuels using improved hydrocracker post-treatment catalyst 有权
标题翻译：使用改进的加氢裂化器后处理催化剂生产低硫燃料
公开(公告)号：US07713407B2
公开(公告)日：2010-05-11
申请号：US11446251
申请日：2006-06-02
申请人： William J. Tracy, III , Chuansheng Bai , Robert A. Bradway , William E. Lewis , Randolph J. Smiley
发明人： William J. Tracy, III , Chuansheng Bai , Robert A. Bradway , William E. Lewis , Randolph J. Smiley
IPC分类号： C10G65/00 , C10G69/00
CPC分类号： C10G65/12 , B01J23/883 , B01J23/8885 , B01J31/10 , C10G45/08
摘要： A hydrocracking process for converting a petroleum feedstock to higher gravity, lower sulfur products, especially ultra low sulfur road diesel fuel. The process may be operated as a single-stage or two-stage hydrocracking. In each case, a hydrocracking step is followed directly by a post-treat hydrodesulfurization zone using a bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals with a ratio of Group VIB metal to Group VIII non-noble metal is from about 10:1 to about 1:10. In the two-stage option with interstage ammonia removal, the initial hydrocracking step may be followed by hydrodesulfurization using the bulk multimetallic catalyst prior to the ammonia removal which is followed by the second hydrocracking step. A final hydrodesulfurization over the bulk multimetallic catalyst may follow. The hydrodesulfurization over the bulk multimetallic catalyst is carried out at a pressure of at least 25 barg and preferably at least 40 barg.
摘要翻译：用于将石油原料转化为更高重力，较低硫产物，特别是超低硫道路柴油的加氢裂化方法。该方法可以作为单级或两级加氢裂化来操作。在每种情况下，加氢裂化步骤直接通过后处理加氢脱硫区，使用由至少一种VIII族非贵金属和至少两种VIB族金属与VIII族的VIB族金属组成的本体多金属催化剂非贵金属为约10:1至约1:10。在阶段氨除去的两阶段选择中，初始加氢裂化步骤之后可以在除氨之前使用大量多金属催化剂进行加氢脱硫，其后是第二加氢裂化步骤。可以遵循大量多金属催化剂的最终加氢脱硫。本体多金属催化剂上的加氢脱硫在至少25barg，优选至少40barg的压力下进行。

7. 发明授权

US09126168B2 Catalyst bed platform with center support pipe 有权
标题翻译：催化床平台与中心支撑管
公开(公告)号：US09126168B2
公开(公告)日：2015-09-08
申请号：US13325148
申请日：2011-12-14
申请人： Antonio O. Ramos , Benjamin S. Umansky , William J. Tracy, III , Ramesh X. Gandhi , Hans G. Korsten , Enrique Feliz
发明人： Antonio O. Ramos , Benjamin S. Umansky , William J. Tracy, III , Ramesh X. Gandhi , Hans G. Korsten , Enrique Feliz
IPC分类号： B01J8/02 , B01J8/00 , B01J8/04
CPC分类号： B01J8/008 , B01J8/0015 , B01J8/003 , B01J8/0035 , B01J8/02 , B01J8/025 , B01J8/0453 , B01J2208/00884 , B01J2208/00938 , B01J2219/00024 , B01J2219/185 , Y10T29/49826
摘要： A structure and method are provided for adding a catalyst bed platform to an existing reactor without welding to the structural portion of the reactor walls. The structure is constructed from components that can be passed through an existing opening in a reactor. The structure allows a catalyst bed in an existing reactor to be divided into catalyst beds with a reduced length to diameter ratio.
摘要翻译：提供了一种用于将催化剂床平台添加到现有反应器而不与反应器壁的结构部分焊接的结构和方法。该结构由可以通过反应器中的现有开口的部件构成。该结构允许将现有反应器中的催化剂床分成具有减小的长径比的催化剂床。

8. 发明授权

US5009767A Recycle of oily refinery wastes 失效
标题翻译：回收油性炼油废物
公开(公告)号：US5009767A
公开(公告)日：1991-04-23
申请号：US410434
申请日：1989-09-21
申请人： Mark P. Bartilucci , Grant G. Karsner , William J. Tracy, III
发明人： Mark P. Bartilucci , Grant G. Karsner , William J. Tracy, III
IPC分类号： C10B57/04 , C10B39/06 , C10B55/00 , C10G9/00
CPC分类号： C10B39/06 , C10B55/00
摘要： Petroleum refinery waste stream sludges are recycled by segregating the sludges according to their oil content. Sludges of high oil content are developed and then injected into a delayed coking unit during the coking phase so that they are converted to coke and liquid coking products. High water content sludges are used to quench the coke during the quench phase of the coking cycle, with minimal increases in coke volatile matter. The process increases the capacity of the delayed coking unit to process and recycle refinery waste sludges and produce a coke of lower volatile content.
摘要翻译：石油炼厂废物流淤泥根据其含油量分离污泥进行回收利用。开发高含油量的污泥，然后在焦化阶段将其注入延迟焦化装置，使其转化为焦炭和液体焦化产物。高含水量的污泥用于在焦化循环的淬火阶段淬火焦炭，焦炭挥发物质的增加最少。该过程增加了延迟焦化装置处理和回收炼油废物污泥并产生低挥发物含量的焦炭的能力。

9. 发明授权

US4786401A Liquid sludge disposal process 失效
标题翻译：液体污泥处理过程
公开(公告)号：US4786401A
公开(公告)日：1988-11-22
申请号：US101092
申请日：1987-09-25
申请人： Solomon M. Jacob , Grant G. Karsner , William J. Tracy, III
发明人： Solomon M. Jacob , Grant G. Karsner , William J. Tracy, III
IPC分类号： C10G11/18 , C10L1/32 , C10G17/00 , C10G55/06
CPC分类号： C10L1/322 , C10G11/18
摘要： Hydrocarbon-containing liquid waste sludges from refinery waste streams can be disposed of by blending with the feedstock being passed to a fluid catalytic cracking unit. Preferably, the sludge is premixed with a hydrocarbon, such as a light oil, prior to mixing with the feed.

10. 发明授权

US4780193A Process for hydrotreating catalytic cracking feedstocks 失效
标题翻译：加氢处理催化裂化原料的方法
公开(公告)号：US4780193A
公开(公告)日：1988-10-25
申请号：US945254
申请日：1986-12-22
申请人： W. Rodman Derr, Jr. , Robert E. Holland , Stephen J. McGovern , William J. Tracy, III
发明人： W. Rodman Derr, Jr. , Robert E. Holland , Stephen J. McGovern , William J. Tracy, III
IPC分类号： C10G69/04
CPC分类号： C10G69/04
摘要： Catalytic cracking of hydrocarbon feedstocks is improved by hydrotreating the cracking feed under conditions of relatively low temperature, typically below 390.degree. C. for start-of-cycle, and high pressure, typically above 10,000 kPa, preferably above 12,000 kPa. The use of these conditions favors aromatics saturation to produce a cracking feed of improved crackability so that higher conversion is achieved in the cracking step at constant cracking conditions with production of naphtha of good octane quality. At the same time, desulfurization is achieved to maintain cracker SO.sub.x emissions at required levels; the advantages of high pressure operation are more notable at high denitrogenation severities while still achieving a low catalyst aging rate.

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