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1. 发明授权

US09776160B2 Catalyst recovery system, hydrocarbon synthesis reaction apparatus, hydrocarbon synthesis reaction system, and catalyst recovery process 有权
公开(公告)号：US09776160B2
公开(公告)日：2017-10-03
申请号：US13978772
申请日：2012-01-13
申请人： Toshiyuki Shibata , Hidekatsu Honda , Akira Kawamura
发明人： Toshiyuki Shibata , Hidekatsu Honda , Akira Kawamura
IPC分类号： B01J8/00 , B01J20/34 , B01J19/06 , C10G2/00 , B01J38/00 , B01D21/00
CPC分类号： B01J19/06 , B01D21/0045 , B01D21/0048 , B01J8/0045 , B01J38/00 , B01J2219/0077 , B01J2219/185 , B01J2219/1943 , B01J2219/1946 , C10G2/32 , C10G2/342 , C10G2/343 , C10G2300/4081 , C10G2300/70
摘要： A catalyst recovery system that includes a concentrated slurry production unit that concentrates a slurry extracted from a reactor main unit and continuously produces a concentrated slurry, a first discharge unit that discharges the concentrated slurry from the concentrated slurry production unit, a solidified slurry production unit that cools the concentrated slurry discharged from the concentrated slurry production unit, thereby solidifying the liquid medium within the concentrated slurry and producing a solidified slurry, and a recovery mechanism that recovers the solidified slurry from the solidified slurry production unit.

2. 发明申请

US20140004011A1 CATALYST RECOVERY SYSTEM, HYDROCARBON SYNTHESIS REACTION APPARATUS, HYDROCARBON SYNTHESIS REACTION SYSTEM, AND CATALYST RECOVERY PROCESS 有权
标题翻译：催化回收系统，烃合成反应装置，烃合成反应系统和催化剂回收方法
公开(公告)号：US20140004011A1
公开(公告)日：2014-01-02
申请号：US13978772
申请日：2012-01-13
申请人： Toshiyuki Shibata , Hidekatsu Honda , Akira Kawamura
发明人： Toshiyuki Shibata , Hidekatsu Honda , Akira Kawamura
IPC分类号： B01J19/06
CPC分类号： B01J19/06 , B01D21/0045 , B01D21/0048 , B01J8/0045 , B01J38/00 , B01J2219/0077 , B01J2219/185 , B01J2219/1943 , B01J2219/1946 , C10G2/32 , C10G2/342 , C10G2/343 , C10G2300/4081 , C10G2300/70
摘要： A catalyst recovery system that includes a concentrated slurry production unit that concentrates a slurry extracted from a reactor main unit and continuously produces a concentrated slurry, a first discharge unit that discharges the concentrated slurry from the concentrated slurry production unit, a solidified slurry production unit that cools the concentrated slurry discharged from the concentrated slurry production unit, thereby solidifying the liquid medium within the concentrated slurry and producing a solidified slurry, and a recovery mechanism that recovers the solidified slurry from the solidified slurry production unit.
摘要翻译： 1.一种催化剂回收系统，其特征在于，包括浓缩从反应器主体提取的浆料的浓缩浆料生成装置，并连续地生成浓缩浆料，从浓缩浆料生成装置排出浓缩浆料的第一排出单元，固化浆料生成单元，冷却从浓缩浆料生成单元排出的浓缩浆料，使浓缩浆液内的液体介质固化，生成固化浆料，以及从固化浆料生成单元回收固化浆料的回收机构。

3. 发明授权

US08951408B2 Method for starting-up naphtha fraction hydrotreating reactor 有权
$Method for starting-up naphtha fraction hydrotreating reactor$
标题翻译：启动石脑油馏分加氢处理反应器的方法
公开(公告)号：US08951408B2
公开(公告)日：2015-02-10
申请号：US12998198
申请日：2009-09-25
申请人： Yuichi Tanaka , Hidekatsu Honda
发明人： Yuichi Tanaka , Hidekatsu Honda
IPC分类号： C07C5/02 , C07C5/09 , C07C5/10 , C07C5/11 , C10G45/02 , C10G45/00 , C10G59/02
CPC分类号： C10G45/02 , C10G45/00 , C10G59/02 , C10G2300/1022 , C10G2300/1044 , C10G2300/4031 , C10G2300/44 , C10G2400/02
摘要： A method for starting-up a naphtha fraction hydrotreating reactor which subjects a naphtha fraction obtained in a fractionator by fractional distillation of hydrocarbon compounds produced by a Fischer-Tropsch synthesis reaction to hydrotreating, the method comprising: charging in advance an inactive hydrocarbon compound corresponding to the naphtha fraction into a vapor-liquid separator to which hydrogenated naphtha, which has been subjected to hydrotreating in the naphtha fraction hydrotreating reactor, is transferred; mixing the inactive hydrocarbon compound drawn from the vapor-liquid separator and the naphtha fractions being transferred from the fractionator to the naphtha fraction hydrotreating reactor, and supplying a mixture of the naphtha fractions and the inactive hydrocarbon compound to the naphtha fraction hydrotreating reactor.
摘要翻译：一种用于启动石脑油馏分加氢处理反应器的方法，该方法包括：将通过费 - 托合成反应生产的烃化合物通过分馏在分馏塔中获得的石脑油馏分进行加氢处理，所述方法包括：预先将对应于石脑油馏分转移到已经在石脑油馏分加氢处理反应器中进行加氢处理的氢化石脑油的气液分离器中; 将从气液分离器抽取的惰性烃化合物和从分馏塔转移到石脑油馏分加氢处理反应器的石脑油馏分混合，并将石脑油馏分和非活性烃化合物的混合物供给石脑油馏分加氢处理反应器。

4. 发明授权

US07112311B2 Cooling method of hydrotreating plant and cooling unit therefor 有权
标题翻译：加氢处理装置冷却方式及冷却装置
公开(公告)号：US07112311B2
公开(公告)日：2006-09-26
申请号：US09984967
申请日：2001-10-31
申请人： Yuji Yoshizumi , Hidekatsu Honda , Masayuki Shoji , Toshihiko Nasu , Katsuhiko Kawakami , Junichi Takano
发明人： Yuji Yoshizumi , Hidekatsu Honda , Masayuki Shoji , Toshihiko Nasu , Katsuhiko Kawakami , Junichi Takano
IPC分类号： B01J8/00 , C10G45/00
CPC分类号： C10G45/02 , B01D53/1468 , B01J2219/00006
摘要： A cooling method of a hydrotreating plant having a desulfurization section (1) including a furnace (12) for heating liquid to be processed, reactors (14, 15) for hydrotreating sulfur to generate hydrogen sulfide, a hydrogen sulfide absorber (19) for absorbing the hydrogen sulfide generated in the reactors (14, 15), and a compressor (21) for compressing and transferring fluid from the hydrogen sulfide absorber (19) toward the reactors (14, 15), the cooling method comprising the steps of gradually depressurizing the hydrotreating plant at the desulfurization section (1) to a pressure level at which reactor material does not embrittle and gas does not leak due to difference of mechanical thermal expansion in the plant after stopping supply of the liquid to be processed, operating the compressor (21) approximately at the maximum rotation number, and completely extinguishing burners (12A, 12B) in the furnace (12) during plant shutdown operation.
摘要翻译：具有脱硫部（1）的加氢处理装置的冷却方法，所述脱硫部（1）包括用于加热待处理液体的炉（12），用于加氢处理硫以产生硫化氢的反应器（14,15），用于吸收硫化氢的硫化氢吸收剂在反应器（14,15）中产生的硫化氢和用于将流体从硫化氢吸收器（19）压缩并输送到反应器（14,15）的压缩机（21），所述冷却方法包括以下步骤：逐渐减压脱硫段（1）的加氢处理装置达到反应器材料不会脆化的压力水平，并且在停止供给待处理液体的操作之后，由于工厂中机械热膨胀的差异而使气体不会泄漏（操作压缩机） 21），并且在工厂关闭操作期间在炉（12）中完全熄灭燃烧器（12A，12B）。

5. 发明授权

US08685212B2 Starting-up method of fractionator 有权
$Starting-up method of fractionator$
标题翻译：分馏器的启动方法
公开(公告)号：US08685212B2
公开(公告)日：2014-04-01
申请号：US12998199
申请日：2009-09-25
申请人： Yuichi Tanaka , Hidekatsu Honda
发明人： Yuichi Tanaka , Hidekatsu Honda
IPC分类号： B01D3/14
CPC分类号： C10G7/00 , C10G2/32 , C10G7/12 , C10G2300/1022 , C10G2300/4031
摘要： A start-up method of a fractionator which fractionally distills FT synthesized hydrocarbons produced by the Fischer-Tropsch synthesis reaction, the method includes: discharging light FT synthesized hydrocarbons which exist in a gaseous state in an FT reactor performing the Fischer-Tropsch synthesis reaction from the FT reactor to the outside; cooling down the light FT synthesized hydrocarbons discharged from the FT reactor for liquefaction; supplying the liquefied light FT synthesized hydrocarbons to the fractionator; and heating the light FT synthesized hydrocarbons and circulating the light FT synthesized hydrocarbons to the fractionator.
摘要翻译：分馏塔分解馏分费 - 托合成反应产生的FT合成烃的分馏塔的启动方法，该方法包括：在进行费 - 托合成反应的FT反应器中放出气态的轻质FT合成烃， FT反应堆到外面; 冷却从FT反应器排出的轻质FT合成烃进行液化; 将液化的FT合成烃供应到分馏塔; 并加热轻质FT合成烃，并将轻质FT合成烃循环至分馏塔。

6. 发明申请

US20110207978A1 Method for starting-up naphtha fraction hydrotreating reactor 有权
$Method for starting-up naphtha fraction hydrotreating reactor$
标题翻译：启动石脑油馏分加氢处理反应器的方法
公开(公告)号：US20110207978A1
公开(公告)日：2011-08-25
申请号：US12998198
申请日：2009-09-25
申请人： Yuichi Tanaka , Hidekatsu Honda
发明人： Yuichi Tanaka , Hidekatsu Honda
IPC分类号： C07C5/02
CPC分类号： C10G45/02 , C10G45/00 , C10G59/02 , C10G2300/1022 , C10G2300/1044 , C10G2300/4031 , C10G2300/44 , C10G2400/02
摘要： A method for starting-up a naphtha fraction hydrotreating reactor which subjects a naphtha fraction obtained in a fractionator by fractional distillation of hydrocarbon compounds produced by a Fischer-Tropsch synthesis reaction to hydrotreating, the method comprising: charging in advance an inactive hydrocarbon compound corresponding to the naphtha fraction into a vapor-liquid separator to which hydrogenated naphtha, which has been subjected to hydrotreating in the naphtha fraction hydrotreating reactor, is transferred; mixing the inactive hydrocarbon compound drawn from the vapor-liquid separator and the naphtha fractions being transferred from the fractionator to the naphtha fraction hydrotreating reactor, and supplying a mixture of the naphtha fractions and the inactive hydrocarbon compound to the naphtha fraction hydrotreating reactor.
摘要翻译：一种用于启动石脑油馏分加氢处理反应器的方法，该方法包括：将通过费 - 托合成反应生产的烃化合物通过分馏在分馏塔中获得的石脑油馏分进行加氢处理，所述方法包括：预先将对应于石脑油馏分转移到已经在石脑油馏分加氢处理反应器中进行加氢处理的氢化石脑油的气液分离器中; 将从气液分离器抽取的惰性烃化合物和从分馏塔转移到石脑油馏分加氢处理反应器的石脑油馏分混合，并将石脑油馏分和非活性烃化合物的混合物供给石脑油馏分加氢处理反应器。

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