公开(公告)号：US08865079B2

公开(公告)日：2014-10-21

申请号：US13391742

申请日：2010-08-12

Applicant: Yasuhiro Onishi ,  Yuzuru Kato ,  Eiichi Yamada

Inventor： Yasuhiro Onishi ,  Yuzuru Kato ,  Eiichi Yamada

IPC: B01J8/18 ,  C10G2/00

CPC classification number: C10G2/342 ,  B01J8/1809 ,  B01J8/1827 ,  C10G2300/4031

Abstract: A hydrocarbon synthesis reaction apparatus includes a reactor, and a synthesis gas supply line through which a synthesis gas is supplied to the reactor, and syntheses hydrocarbons by contacting the synthesis gas and the catalyst slurry in the reactor. The hydrocarbon synthesis reaction apparatus includes a spare supply line which is connected to the synthesis gas supply line, and supplies inert gas or hydrogen gas to the reactor through the synthesis gas supply line when supply of the synthesis gas to the synthesis gas supply line from the synthesis gas supply device is stopped, and a fluid heating device which heats at least one of a fluid which flows through a flowing line of the synthesis gas supply line located closer to the reactor than a portion connected with the spare supply line, and a fluid which flows through the spare supply line.

Abstract translation: 烃合成反应装置包括反应器和合成气供给管线，合成气通过该合成气供给到反应器，通过使反应器中的合成气和催化剂浆料接触来合成烃。 烃合成反应装置包括与合成气供给管线连接的备用供给管线，在从合成气供给管路向合成气供给管路供给合成气体时，通过合成气供给管线向反应器供给惰性气体或氢气 合成气体供给装置停止，并且流体加热装置，其加热流过比合成气供应管线更靠近反应器的流动管线的流体中的至少一个，而不是与备用供应管线连接的部分，以及流体 其流经备用供应线。

公开(公告)号：US20140135410A1

公开(公告)日：2014-05-15

申请号：US14006998

申请日：2012-03-13

Applicant: Yasuhiro Onishi ,  Kazuhiko Tasaka ,  Tomoyuki Mikuriya

Inventor： Yasuhiro Onishi ,  Kazuhiko Tasaka ,  Tomoyuki Mikuriya

IPC: C07C1/04

CPC classification number: C07C1/041 ,  B01J8/1809 ,  B01J8/22 ,  B01J19/0013 ,  B01J19/0033 ,  B01J2208/00061 ,  B01J2208/00274 ,  B01J2208/00548 ,  B01J2208/00646 ,  B01J2219/00202 ,  B01J2219/00213 ,  B01J2219/00231 ,  B01J2219/00238 ,  C10G2/342 ,  C10G2300/4031 ,  C10G2300/4081

Abstract: The hydrocarbon synthesis reaction apparatus is provided with a synthesis gas supply line in which a synthesis gas is compressed and supplied by a first compressor, a reactor configured to accommodate a catalyst slurry, a gas-liquid separator configured to separate an unreacted synthesis gas and hydrocarbons discharged from the reactor into a gas and a liquid, a first recycle line in which the unreacted synthesis gas after separation into a gas and a liquid is compressed and recycled into the reactor by a second compressor, and a second recycle line configured to recycle a residual unreacted synthesis gas after separation into a gas and a liquid into the inlet side of the first compressor at the time of start-up operation when the synthesis gas is gradually increased in the amount to be introduced.

Abstract translation: 烃合成反应装置设置有合成气供给管线，其中合成气由第一压缩机，构造成容纳催化剂浆料的反应器压缩并供应，气液分离器，其构造成分离未反应的合成气和烃 从反应器排放到气体和液体中的第一再循环管线，其中分离成气体和液体后的未反应的合成气被第二压缩机压缩并再循环到反应器中的第一再循环管线，以及第二循环管线， 当合成气以引入量逐渐增加时，在启动操作时将分离成气体和液体的液体分离成第一压缩机入口侧的残留未反应合成气。

公开(公告)号：US20120172458A1

公开(公告)日：2012-07-05

申请号：US13391853

申请日：2010-08-12

Applicant: Yasuhiro Onishi

Inventor： Yasuhiro Onishi

IPC: C07C27/00 ,  B01J19/00

CPC classification number: C10G2/30 ,  B01J2219/00006 ,  C10G2/342 ,  C10G2/344

Abstract: A hydrocarbon synthesis reaction apparatus synthesizes hydrocarbons by a Fischer-Tropsch synthesis reaction. The apparatus includes a reactor; a flowing line; a first cooling unit; a second cooling unit; a first separating unit which separates the liquid hydrocarbons condensed by the first cooling unit from the gaseous hydrocarbons; and a second separating unit which separates the liquid hydrocarbons condensed by the second cooling unit from the gaseous hydrocarbons. The first cooling unit cools the hydrocarbons which flow through the flowing line to a temperature range equal to or lower than a condensing point at which a wax fraction condenses, and higher than a freezing point at which the wax fraction solidifies. The second cooling unit cools the hydrocarbons which flow through the flowing line to a temperature range lower than the temperature to which the gaseous hydrocarbons are cooled by the first cooling unit, and higher than a freezing point at which a middle distillate solidifies.

Abstract translation: 烃合成反应装置通过费 - 托合成反应合成烃。 该装置包括反应器; 流线 第一个冷却单元; 第二冷却单元; 第一分离单元，其将由第一冷却单元冷凝的液体烃与气态烃分离; 以及第二分离单元，其将由第二冷却单元冷凝的液体烃与气态烃分离。 第一冷却单元将流过流动管线的烃冷却至等于或低于蜡馏分冷凝的凝结点并高于蜡馏分固化的凝固点的温度范围。 第二冷却单元将流过流动管线的烃冷却至低于气态烃被第一冷却单元冷却的温度的温度范围，并且高于中间馏分固化的凝固点。

公开(公告)号：US20110201696A1

公开(公告)日：2011-08-18

申请号：US12998191

申请日：2009-09-25

Applicant: Yasuhiro Onishi ,  Eiichi Yamada

Inventor： Yasuhiro Onishi ,  Eiichi Yamada

IPC: C07C27/00 ,  B01J19/00

CPC classification number: C10G2/332 ,  B01J8/22 ,  B01J2208/00141 ,  B01J2219/00006 ,  C10G2/32 ,  C10G2/342 ,  C10G2300/807

Abstract: A hydrocarbon synthesis reaction apparatus which synthesizes a hydrocarbon compound by a chemical reaction of a synthesis gas including hydrogen and carbon monoxide as the main components, and a slurry having solid catalyst particles suspended in a liquid, the hydrocarbon synthesis reaction apparatus is provided with: a reactor which contains the slurry; a synthesis gas introduction part which introduces the synthesis gas into the reactor; and a synthesis gas heating part which is provided in the synthesis gas introduction part to heat the synthesis gas introduced into the reactor to the decomposition temperature of carbonyl compounds or higher.

Abstract translation: 一种烃合成反应装置，其通过包含氢和一氧化碳的合成气作为主要成分的化学反应合成烃化合物，以及具有悬浮在液体中的固体催化剂颗粒的浆料，所述烃合成反应装置具有： 含有浆料的反应器; 将合成气引入反应器的合成气导入部， 以及合成气加热部，其设置在合成气导入部中，以将导入反应器的合成气加热至羰基化合物的分解温度以上。

公开(公告)号：US20110196048A1

公开(公告)日：2011-08-11

申请号：US12998187

申请日：2009-09-25

Applicant: Yasuhiro Onishi ,  Yuzuru Kato ,  Eiichi Yamada

Inventor： Yasuhiro Onishi ,  Yuzuru Kato ,  Eiichi Yamada

IPC: C07C1/04 ,  B01J19/00

CPC classification number: B01J4/002 ,  B01J4/008 ,  B01J8/22 ,  B01J2204/002 ,  B01J2208/0007 ,  B01J2208/00274 ,  B01J2208/00548 ,  B01J2219/00006 ,  C10G2/342

Abstract: A hydrocarbon synthesis reaction apparatus which synthesizes a hydrocarbon compound by a chemical reaction of a synthesis gas including a hydrogen and a carbon monoxide as the main components, and a slurry having solid catalyst particles suspended in a liquid, the apparatus is provided with: a reactor in which the synthesis gas contacts with the slurry; and an unreacted gas supply device which draws unreacted gas from the reactor, then pressurizes the unreacted gas, and supplies the unreacted gas to a constituent device which constitutes the hydrocarbon synthesis reaction apparatus.

Abstract translation: 一种烃合成反应装置，其通过包含氢和一氧化碳的合成气作为主要成分的化学反应合成烃化合物，以及具有悬浮在液体中的固体催化剂颗粒的浆料，该装置设有：反应器 其中合成气与浆料接触; 以及未反应气体供给装置，从反应器抽出未反应气体，然后对未反应气体进行加压，将未反应气体供给到构成烃合成反应装置的构成装置。

公开(公告)号：US20090220389A1

公开(公告)日：2009-09-03

申请号：US12097161

申请日：2005-12-14

Applicant: Yasuhiro Onishi ,  Kenichiro Fujimoto ,  Masaru Ihara ,  Yoshifumi Suehiro ,  Yasumasa Morita ,  Kiyoshi Inaba ,  Toshio Shimizu ,  Osamu Iwamoto

Inventor： Yasuhiro Onishi ,  Kenichiro Fujimoto ,  Masaru Ihara ,  Yoshifumi Suehiro ,  Yasumasa Morita ,  Kiyoshi Inaba ,  Toshio Shimizu ,  Osamu Iwamoto

IPC: B01J8/24

CPC classification number: B01J8/228 ,  B01J8/007 ,  B01J8/085 ,  B01J8/1818 ,  B01J8/22 ,  B01J2208/00123 ,  B01J2208/00539 ,  B01J2208/0061 ,  C10G2/342 ,  C10G2300/4006 ,  C10G2300/805

Abstract: A bubble column-type slurry bed reaction system is provided in which an operating system, which synthesizes liquid hydrocarbons by the Fischer-Tropsch (FT) synthesis reaction and separates and derives a catalyst and liquid hydrocarbon products from a slurry composed of gas, liquid and solid phases, can be simplified, and deterioration of catalyst particles caused by attrition and so forth can be reduced. In this FT synthesis reaction system, a bubble column-type slurry bed Fischer-Tropsch synthesis reaction process, in which synthesis gas supplied continuously from the bottom of a reactor and suspended catalyst particles are contacted to form liquid hydrocarbons, gaseous hydrocarbons and water, a process in which a slurry of suspended liquid products formed in the Fischer-Tropsch synthesis reaction process and catalyst particles moves from the reactor to the lower portion of a separation vessel through a downwardly inclined transfer pipe to separate the catalyst particles and gaseous products, a process in which the liquid products formed in the Fischer-Tropsch synthesis reaction process is sent to the separation vessel through a horizontal connecting pipe installed above the downwardly inclined transfer pipe and derived from its apex, a process in which liquid products are derived from the separation vessel, and a process in which aslurry in which catalyst particles are concentrated is derived from the bottom of the separation vessel and circulated to the bottom of the reactor, are driven by the driving force of synthesis gas introduced from the bottom of the reactor and which rises through the slurry bed reactor without using an external drive power source for circulation, and the formed liquid hydrocarbon products, gaseous hydrocarbon products and water are separated and derived without using an external drive power source for separation.

Abstract translation: 提供了一种气泡塔型浆床反应系统，其中通过费 - 托（FT）合成反应合成液态烃的操作系统，分离并从由气体，液体和 可以简化固相，并且可以减少由磨损等引起的催化剂颗粒的劣化。 在该FT合成反应系统中，将泡沫塔型浆料床费 - 托合成反应过程从反应器底部连续供应的合成气和悬浮的催化剂颗粒接触形成液态烃，气态烃和水， 其中在费 - 托合成反应过程中形成的悬浮液体产物的浆料和催化剂颗粒通过向下倾斜的转移管从反应器移动到分离容器的下部以分离催化剂颗粒和气态产物的过程， 其中在费 - 托合成反应过程中形成的液体产物通过安装在向下倾斜的输送管上方并从其顶点衍生的水平连接管送到分离容器，其中液体产物从分离容器 ，以及其中催化剂颗粒浓缩的浆料的方法 来自分离容器的底部并循环到反应器的底部，由从反应器底部引入并通过浆料床反应器的合成气的驱动力驱动，而不使用外部驱动电源 循环，并且形成的液体烃产物，气态烃产物和水分离和衍生而不使用外部驱动电源进行分离。

公开(公告)号：US07325173B2

公开(公告)日：2008-01-29

申请号：US11092768

申请日：2005-03-30

Applicant: Akira Kikutake ,  Masato Matsumiya ,  Yasuhiro Onishi

Inventor： Akira Kikutake ,  Masato Matsumiya ,  Yasuhiro Onishi

IPC: G06F11/00

CPC classification number: G11C29/24 ,  G06F11/1052

Abstract: During a first data compression test mode which disables an error correction function, first test data are written to a first regular memory block. Second test data are written to not only a second regular memory block, but a parity memory block. By changing the number of bits distributed to the first and second test data (compression rate of data), a data compression test for a parity memory block can be performed without need to increase the number of test terminals. As a result, the test time can be decreased and the test cost can be decreased.

Abstract translation: 在禁止纠错功能的第一数据压缩测试模式期间，将第一测试数据写入第一常规存储器块。 第二测试数据不仅写入第二常规存储器块，而且写入奇偶校验存储器块。 通过改变分配给第一和第二测试数据的位数（数据的压缩率），可以执行奇偶校验存储器块的数据压缩测试，而不需要增加测试终端的数量。 结果，可以减少测试时间并降低测试成本。

公开(公告)号：US20070046283A1

公开(公告)日：2007-03-01

申请号：US11501240

申请日：2006-08-09

Applicant: Yasuhiro Onishi ,  Masanobu Horino ,  Katsumi Ohashi

Inventor： Yasuhiro Onishi ,  Masanobu Horino ,  Katsumi Ohashi

IPC: G01R31/28

CPC classification number: H05K3/1233 ,  H05K3/3484 ,  H05K2203/162 ,  H05K2203/163

Abstract: A solder material test apparatus includes a control unit and a storage unit which stores master data in advance in which a printing process time when a printing process is performed by using a test-sample solder material is associated with deterioration degree data of the test-sample solder material at the printing process time. The control unit includes a deterioration degree data acquiring unit which acquires deterioration degree data for indicating a deterioration degree of a test-sample solder material, a reading unit which reads a printing process time associated with deterioration degree data set as a limit value with reference to master data and reads a printing process time associated with the deterioration degree data acquired by the deterioration degree data acquiring unit, an operating unit which operates an available remaining time that indicates difference between the printing process times, and a display control unit which informs the available remaining time to a user.

Abstract translation: 焊料测试装置包括控制单元和存储单元，其预先存储主数据，其中通过使用测试样品焊料进行打印处理的打印处理时间与测试样品的劣化程度数据相关联 焊料在印刷过程中的时间。 控制单元包括劣化度数据获取单元，其获取用于指示测试样品焊料材料的劣化程度的劣化度数据，读取单元，其读取与设置为极限值的劣化度数据相关联的打印处理时间，参考 读取与恶化度数据获取单元获取的劣化度数据相关联的打印处理时间，操作指示打印处理时间之间的差异的可用剩余时间的操作单元和通知可用的显示控制单元 留给用户的时间。

公开(公告)号：US20050217292A1

公开(公告)日：2005-10-06

申请号：US11082788

申请日：2005-03-18

Applicant: Yasuhiro Onishi ,  Hidefumi Uesugi

Inventor： Yasuhiro Onishi ,  Hidefumi Uesugi

IPC: F25B1/00 ,  F25B41/00 ,  F25B49/00 ,  F25B49/02

CPC classification number: F25B49/02 ,  F25B41/00 ,  F25B2600/2509 ,  F25B2700/1931 ,  F25B2700/1933 ,  F25B2700/21151 ,  F25B2700/21152

Abstract: A refrigerating system comprises a compressor, a condenser, an expansion valve, an evaporator, sensors for detecting respectively a temperature and a pressure of a refrigerant sucked into the compressor, and a pressure of a refrigerant discharged from the compressor, a liquid injection system including an injection passage and a flow control valve connected in the injection passage, and a control means for estimating a temperature of gas refrigerant discharged from the compressor, from detected values delivered from the sensors, and for delivering an instruction for controlling the injection quantity of the liquid refrigerant, depending upon the estimated temperature, to the flow regulating valve, thereby it is possible to control a temperature of the discharged gas from the compressor to a set value, irrespective of an operating condition.

Abstract translation: 制冷系统包括压缩机，冷凝器，膨胀阀，蒸发器，用于分别检测吸入压缩机的制冷剂的温度和压力的传感器以及从压缩机排出的制冷剂的压力;液体喷射系统，包括 连接在喷射通道中的喷射通道和流量控制阀，以及用于从传感器传送的检测值估计从压缩机排出的气体制冷剂的温度的控制装置，以及用于传送控制装置的喷射量的指令 取决于估计的温度的液体制冷剂到流量调节阀，从而可以将来自压缩机的排出气体的温度控制到设定值，而与操作条件无关。

公开(公告)号：US09452405B2

公开(公告)日：2016-09-27

申请号：US12998201

申请日：2009-09-25

Applicant: Yasuhiro Onishi ,  Akihiko Hirama

Inventor： Yasuhiro Onishi ,  Akihiko Hirama

IPC: B01J8/22 ,  C10G2/00 ,  B01J8/18

CPC classification number: B01J8/22 ,  B01J8/1827 ,  B01J2208/00274 ,  B01J2208/003 ,  B01J2208/00911 ,  C10G2/32 ,  C10G2/342

Abstract: A liquid-fuel synthesizing method includes a synthesizing step of synthesizing liquid fuels by making a synthesis gas including a carbon monoxide gas and a hydrogen gas as the main components and a slurry having solid catalyst particles suspended in a liquid react with each other in a reactor, and a synthesis gas supply step of supplying the synthesis gas to the reactor from a plurality of supply devices provided in the reactor so as to have different heights.

Abstract translation: 液体燃料合成方法包括通过使包含一氧化碳气体和氢气的合成气作为主要成分来合成液体燃料的合成步骤以及悬浮在液体中的固体催化剂颗粒的浆料在反应器中彼此反应 以及从设置在反应器中的多个供给装置向反应器供给合成气以使其具有不同高度的合成气供给工序。