专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

EP2435540B1 PROCESS FOR RECOVERY OF CARBON DIOXIDE FROM A FLUID STREAM, IN PARTICULAR FROM SYNGAS 有权转让
标题翻译：从流体中回收二氧化碳的方法，特别是从合成气中回收二氧化碳
公开(公告)号：EP2435540B1
公开(公告)日：2018-04-04
申请号：EP10723987.3
申请日：2010-05-25
申请人： BASF SE , JGC Corporation
发明人： KATZ, Torsten , SIEDER, Georg , TANAKA, Koji
IPC分类号： C10K1/08
CPC分类号： C10K1/08 , Y02C10/06 , Y02E20/16 , Y02E20/18 , Y02E20/185
摘要： A process for removing carbon dioxide from a fluid comprises the steps of: (a) treating the fluid by bringing it into countercurrent contact with a liquid absorbent in a first absorption zone and thereafter in a second absorption zone to absorb at least part of the carbon dioxide contained in the fluid into the absorbent; (b) depressurizing the loaded absorbent to release a first stream of carbon dioxide and yield a partially regenerated absorbent; (c) recycling a first stream of the partially regenerated absorbent into the first absorption zone; (d) heating a second stream of the partially regenerated absorbent to release a second stream of carbon dioxide and yield a regenerated absorbent; (e) recycling the regenerated absorbent into the second absorption zone; (f) condensing water vapor entrained in the second stream of carbon dioxide by cooling the second stream of carbon dioxide and transferring at least part of the heat recovered to the partially regenerated absorbent by indirect heat exchange. The invention provides a two-stage carbon dioxide recovery process wherein the overall energy required for carbon dioxide recovery is reduced and/or wherein at least part of the carbon dioxide is recovered at a pressure higher than atmospheric pressure so as to reduce the energy required for compression of the carbon dioxide, e.g., for sequestration. Also disclosed is a plant for removing carbon dioxide from a fluid.

2. 发明公开

EP2822143A1 POWER SUPPLY DEVICE, ELECTRICITY STORAGE DEVICE, AND ELECTRICITY STORAGE SYSTEM 有权
标题翻译： STROMERSERSGUNGSVORRICHTUNG，STROMSPEICHERVORRICHTUNG UND STROMSPEICHERSTEMTEM
公开(公告)号：EP2822143A1
公开(公告)日：2015-01-07
申请号：EP13754155.3
申请日：2013-03-04
申请人： JGC Corporation , University of Tsukuba
发明人： NAKAYAMA Tomonori , ISHIDA Masayoshi , HASEGAWA Hiroaki , HIRAOKA Kazutaka , NAGAI Toshiyuki , KAKIZAKI Nobuo
IPC分类号： H02J7/35 , H01M2/20 , H01M10/44 , H01M10/48
CPC分类号： H02J7/35 , H01M10/44 , H01M10/48 , H02J3/385 , H02J7/345 , Y02E10/58 , Y02E70/40
摘要： A power supply apparatus that receives electric power from a power generation apparatus having a varying output and supplies electric power to an outside, the apparatus comprising: a power storage device that has a larger amount by which electric power is stored and/or a lower self-discharge rate than a capacitor device used as a passive device and also has higher charge and discharge efficiency and/or higher responsiveness than a secondary battery, the power storage device receiving electric power from the power generation apparatus and discharging electric power to the outside; a current control unit that controls a current supplied from the power storage device to the outside; and a control unit that controls a current and a voltage of the power generation apparatus by charging and discharging the power storage device so as to maximize an amount of power generation by the power generation apparatus.
摘要翻译：一种从具有变化的输出的发电装置接收电力并向外部供电的电力供给装置，所述装置包括：蓄电装置，其具有较大的蓄电量和/或较低的自身 - 电荷比率比用作无源器件的电容器器件还要高于二次电池具有更高的充放电效率和/或更高的响应性，蓄电装置从发电装置接收电力并向外部放电; 电流控制单元，其将从蓄电装置供给的电流控制到外部; 以及控制单元，其通过对所述蓄电装置进行充电和放电来控制所述发电装置的电流和电压，以使所述发电装置的发电量最大化。

3. 发明公开

EP2435540A1 PROCESS FOR RECOVERY OF CARBON DIOXIDE FROM A FLUID STREAM, IN PARTICULAR FROM SYNGAS 有权转让
标题翻译：用于从合成气OBTAINING二氧化碳流体流动，尤其是
公开(公告)号：EP2435540A1
公开(公告)日：2012-04-04
申请号：EP10723987.3
申请日：2010-05-25
申请人： BASF SE , JGC Corporation
发明人： KATZ, Torsten , SIEDER, Georg , TANAKA, Koji
IPC分类号： C10K1/08
CPC分类号： C10K1/08 , Y02C10/06 , Y02E20/16 , Y02E20/18 , Y02E20/185
摘要： A process for removing carbon dioxide from a fluid comprises the steps of: (a) treating the fluid by bringing it into countercurrent contact with a liquid absorbent in a first absorption zone and thereafter in a second absorption zone to absorb at least part of the carbon dioxide contained in the fluid into the absorbent; (b) depressurizing the loaded absorbent to release a first stream of carbon dioxide and yield a partially regenerated absorbent; (c) recycling a first stream of the partially regenerated absorbent into the first absorption zone; (d) heating a second stream of the partially regenerated absorbent to release a second stream of carbon dioxide and yield a regenerated absorbent; (e) recycling the regenerated absorbent into the second absorption zone; (f) condensing water vapor entrained in the second stream of carbon dioxide by cooling the second stream of carbon dioxide and transferring at least part of the heat recovered to the partially regenerated absorbent by indirect heat exchange. The invention provides a two-stage carbon dioxide recovery process wherein the overall energy required for carbon dioxide recovery is reduced and/or wherein at least part of the carbon dioxide is recovered at a pressure higher than atmospheric pressure so as to reduce the energy required for compression of the carbon dioxide, e.g., for sequestration. Also disclosed is a plant for removing carbon dioxide from a fluid.

4. 发明公开

EP1930076A1 CATALYST FOR CATALYTIC PARTIAL OXIDATION OF HYDROCARBON AND PROCESS FOR PRODUCING SYNTHESIS GAS 审中-公开
标题翻译：催化剂用于烃类催化部分氧化和工艺生产合成气
公开(公告)号：EP1930076A1
公开(公告)日：2008-06-11
申请号：EP06797886.6
申请日：2006-09-06
申请人： JGC Corporation , OSAKA GAS CO., LTD.
发明人： FUJIE, Hirokazu , WATANABE, Yoshiyuki , MURATA, Chizu
IPC分类号： B01J23/89 , C01B3/40
CPC分类号： B01J23/8946 , B01J23/005 , B01J23/894 , B01J37/0009 , B01J37/0205 , B01J37/0207 , B01J37/08 , C01B3/386 , C01B3/40 , C01B2203/0261 , C01B2203/1058 , C01B2203/1064 , C01B2203/1082 , Y02P20/52
摘要： [Problem] To provide a catalyst for catalytic partial oxidation having a high activity and a long-term durability; and to provide a method capable of attaining long-term stable catalytic partial oxidation.
[Means for Solution] The catalyst for catalytic partial oxidation comprises a carrier obtained by adding nickel and at least one of barium and lanthanum to alumina or an alumina precursor followed by firing it, and a platinum group element such as rhodium held by the carrier. The carrier is obtained, for example, by firing at a temperature not lower than 600°C, and in the firing step, nickel aluminate is formed. The catalyst is filled into a heat-insulating reactor; and oxygen and steam and hydrogen are added to a starting hydrocarbon (when the starting hydrocarbon contains hydrogen, adding hydrogen thereto is unnecessary), and this is fed into the reactor.
摘要翻译： [问题]为了提供一种具有高活性和长期耐久性催化部分氧化的催化剂; 并且，提供一种能够实现有长期稳定的催化部分氧化的方法。 [解决手段]用于催化部分氧化的催化剂包含通过加入镍和钡中的至少一种和镧氧化铝或随后烧成的氧化铝前体得到的载体，和铂族元素：如通过载体保持铑。该载体获得，例如，通过在温度不低于600℃下烧结，并且在烧成工序中，镍铝形成。催化剂填充到绝热反应器; 和氧气和蒸汽和氢气加入到原料烃（当原料烃中含有氢，向其中加入氢是不必要的），并且这被进料到反应器。

5. 发明授权

EP1338557B1 METHOD AND APPARATUS FOR REMOVING SULFUR COMPOUND IN GAS CONTAINING HYDROGEN SULFIDE, MERCAPTAN, CARBON DIOXIDE AND AROMATIC HYDROCARBON 有权
标题翻译：方法和装置脱除硫化合物的硫化从硫醇，二氧化碳和芳香烃含瓦斯
公开(公告)号：EP1338557B1
公开(公告)日：2005-03-23
申请号：EP00969836.6
申请日：2000-10-18
申请人： JGC Corporation
发明人： ISHIGAKI, Shinya, c/o JGC Corp., Research Center , KIDA, Mitsuru, c/o JGC Corporation , SASAKI, Takashi, c/o JGC Corporation
IPC分类号： C01B17/04 , B01D53/34 , C10L3/10
CPC分类号： C10L3/102 , B01D2257/304 , B01D2257/306 , C01B17/0404 , C01B17/0408 , C10L3/10

6. 发明授权

EP0902078B1 Petroleum processing method 有权
标题翻译： Erdölverarbeitungsverfahren
公开(公告)号：EP0902078B1
公开(公告)日：2004-12-22
申请号：EP98307397.4
申请日：1998-09-11
申请人： JGC Corporation
发明人： Inomata, Makoto , Okumura, Toshiya, c/o JGC Corporation , Nigamatsu, Shigeki
IPC分类号： C10G65/04 , C10G69/08
CPC分类号： C10G67/00 , C10G65/04 , C10G67/06 , C10G69/08

7. 发明公开

EP1352946A1 METHOD OF DESULFURIZING GAS OIL FRACTION, DESULFURIZED GAS OIL, AND DESULFURIZER FOR GAS OIL FRACTION 审中-公开
标题翻译：脱硫轻油GROUP法脱硫瓦斯油和汽油组获得脱硫
公开(公告)号：EP1352946A1
公开(公告)日：2003-10-15
申请号：EP01983811.9
申请日：2001-11-16
申请人： JGC Corporation
发明人： NAGAMATSU, Shigeki, c/o JGC CORPORATION , ABE, Jun, c/o JGC CORPORATION Res & Dev. Center , SUGIMOTO, Akira, c/o JGC CORPORATION , INOMATA, M., c/o JGC CORPORATION Res & Dev Center , WATANABE, Tetsuya, c/o JGC CORPORATION
IPC分类号： C10G65/16
CPC分类号： C10G65/16 , B01J23/882 , C10G2300/1059 , C10G2300/202 , C10G2300/207 , C10G2400/06
摘要： The process for desulfurizing a gas oil fraction according to the invention comprises a low-boiling gas oil fraction hydrodesulfurization step (I) wherein a low-boiling gas oil fraction is desulsurized under the condition of a H 2 /Oil ratio of 70 to 200 Nm 3 /kl to obtain a treated oil, a high-boiling gas oil fraction hydrodesulfurization step (II) wherein a high-boiling gas oil fraction is desulsurized under the condition of a H 2 /Oil ratio of 200 to 800 Nm 3 /kl to obtain a treated oil, and a step (III) wherein the treated oil obtained in the step (I) is mixed with the treated oil obtained in the step (II), and in this process, at least a part of a gas containing unreacted hydrogen in the step (II) is used for the hydrodesulfurization of the step (I). According to the invention, there can be provided a process and an apparatus for desulfurizing a gas oil fraction, which are capable of using hydrogen and energy efficiently and capable of producing a highly desulfurized gas oil in a small catalytic amount. According to the invention, further, a desulfurized gas oil which is economically produced and has a sufficiently decreased sulfur content can be provided. According to the invention, furthermore, there can be provided an apparatus for desulfurizing a gas oil fraction, which is capable of using a hydrogen gas and energy efficiently, capable of being simplified in its constitution, capable of reducing cost of equipment, control of apparatus, labor of maintenance, apparatus area, etc. and capable of highly desulfurizing a gas oil fraction economically.
摘要翻译：用于脱硫瓦斯油馏分雅丁到发明的方法包括worin低沸点瓦斯油馏分70的H 2 /油比的条件下desulsurized至200nm <低沸点轻油馏分加氢脱硫步骤（I） 3> / KL，以获得处理过的油，高沸点轻油馏分加氢脱硫步骤（II）worin高沸点瓦斯油馏分的200至800nm的H 2 /油比的条件下desulsurized <3> / KL以获得处理过的油，以及步骤（III）worin在工序（I）得到的处理油与在工序（II）中得到的处理过的油混合，并在此过程中，至少一个的气体的一部分在步骤包含未反应的氢（II）被用于步骤（I）的加氢脱硫。。根据本发明，可以用于脱硫轻油馏分，其能够使用氢和能量高效的，并且可在小的催化量制备高脱硫瓦斯油的提供的方法和设备来。。根据本发明，进一步地，脱硫气油所有这在经济上制造并且具有充分降低的硫含量可以提供。。根据本发明，进一步，也可以被提供给装置的脱硫轻油馏分，所有这些是能够使用氢气和能量高效的，能够在其结构被简化，能够降低设备的成本，装置的控制的，维护，设备区域等的实验室和能够高度脱硫轻油馏分经济。

8. 发明公开

EP1338557A1 METHOD AND APPARATUS FOR REMOVING SULFUR COMPOUND IN GAS CONTAINING HYDROGEN SULFIDE, MERCAPTAN, CARBON DIOXIDE AND AROMATIC HYDROCARBON 有权
标题翻译：方法和装置脱除硫化合物的硫化从硫醇，二氧化碳和芳香烃含瓦斯
公开(公告)号：EP1338557A1
公开(公告)日：2003-08-27
申请号：EP00969836.6
申请日：2000-10-18
申请人： JGC Corporation
发明人： ISHIGAKI, S., c/o JGC Corp., Res. & Devel. Center , KIDA, Mitsuru, c/o JGC Corporation , SASAKI, Takashi, c/o JGC Corporation
IPC分类号： C01B17/04
CPC分类号： C10L3/102 , B01D2257/304 , B01D2257/306 , C01B17/0404 , C01B17/0408 , C10L3/10
摘要： A method and an apparatus for removing sulfur compounds, such as H 2 S and mercaptans, contained in an impurity gas contained in a natural gas or the like by recovering them as elementary sulfur, characterized in that it comprises a step of separating the impurity gas from the natural gas or the like, a concentration step of separating the impurity gas into a concentrated gas comprising H 2 S as a main component and a residual gas comprising mercaptans and CO 2 as main components, a step of subjecting the concentrated gas to a Claus reaction process to recover H 2 S as elementary sulfur, a step of heating the off-gas from the Claus reaction process to a temperature of 700°C or less and mixing the heated off-gas with the above residual gas, a step of subjecting the resultant mixed gas to a hydrogenation process to convert sulfur compounds such as a mercaptan to H 2 S by using a reduction catalyst, and a step of separating the H 2 S and recycling it to the above Clause reaction process.
摘要翻译：一种用于除去硫化合物，发色方法以及装置，包括：如H 2 S和硫醇，载于含有天然气或类似物中的杂质气体通过回收它们作为元素硫，其特征在于在没有它包括从分离的杂质气体的步骤天然气或类似物，杂质气体分离成浓缩的气体包含H 2 S作为主要成分和残余气体包括硫醇和CO 2作为主要成分的浓缩步骤，将浓缩的气体到克劳斯反应过程的步骤，以回收 H2S为元素硫，通过上述残留气体，使所得到的混合气体到的步骤从克劳斯反应过程中加热尾气至700℃或更低的温度和混合所述加热的废气的步骤氢化方法转化硫的化合物：如硫醇以H2S通过使用还原催化剂，并分离H 2 S和其再循环到上述第反应处理的步骤。

9. 发明授权

EP1230323B1 SYSTEM AND METHOD FOR OIL FUEL BURNING INTEGRATED COMBINED CYCLE POWER GENERATION 有权
标题翻译：系统和方法的综合ÖLBRENNUNG及联合循环发电设备
公开(公告)号：EP1230323B1
公开(公告)日：2003-05-07
申请号：EP00974957.3
申请日：2000-11-13
申请人： JGC Corporation
发明人： OKADA, Tsuyoshi , MASHIKO, Yoshinori , SASAKI, Tomoyoshi , INOMATA, Makoto
IPC分类号： C10G67/16 , C10G45/00 , F02C7/22
CPC分类号： F02C3/22 , C10G45/00 , C10G67/00 , C10G2300/107 , F01K23/068 , F02C3/24 , F02C3/28 , F02C7/22 , F05D2270/13 , Y02E20/14 , Y02E20/16 , Y02E20/18
摘要： A light portion is extracted from feed oil by a separation system. The light portion is then subject to a hydrotreatment to obtain impurity-removed fuel oil which is stored in an intermediate tank. A residue of the feed oil after extraction of the light portion is gasified to obtain syngas (H2 gas + CO gas) which is used as basic fuel for power generation in a power generation system. The fuel oil is fed to the power generation system as auxiliary fuel for supplementing the power generation based on the syngas. The power generation system includes a plurality of gas turbines and generators. The number of the gas turbines to be driven by the fuel oil is controlled to adjust the power generation amount depending on demand.

10. 发明公开

EP1249485A1 PETROLEUM PROCESSING METHOD AND DEVICE THEREFOR 审中-公开
标题翻译： VERFAHREN UND VORRICHTUNG祖国石油公司
公开(公告)号：EP1249485A1
公开(公告)日：2002-10-16
申请号：EP99959757.8
申请日：1999-12-10
申请人： JGC Corporation
发明人： OKADA, Tsuyoshi, JGC Corporation , SUGIMOTO, Akira, JGC Corporation , KUBO, Masatoshi, JGC Corporation , KATOH, Yoshio
IPC分类号： C10G7/06 , C10G7/00
CPC分类号： C10G67/02 , B01D3/10 , B01D3/146 , C10G7/06 , C10G53/02
摘要： A petroleum processing method for fractionating a feed oil into atmospheric distillate, vacuum distillate and vacuum residue, the petroleum processing method comprising the steps of:

(i) performing an atmospheric distillation of a feed oil to thereby attain a separation thereof into atmospheric distillate and reduced crude; and
(ii) subjecting the reduced crude to a vacuum distillation without heating to thereby attain a separation thereof into vacuum distillate and vacuum residue.
Thus, there can be provided a method and an apparatus which enable obtaining vacuum distillate from reduced crude in an economical manner without heating the reduced crude.
摘要翻译：在大气压下蒸馏粗油（1a），在常压下得到底油（1c）。随后真空蒸馏未加热的底部油。 - 石油加工设备还包括独立权利要求。该设备包括常压蒸馏设备（打顶机）（2）和减压蒸馏设备（3）。在常压蒸馏装置和减压蒸馏装置之间不设置加热炉。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式