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91. 发明专利

BR112015021760A2 acelerador de crescimento de planta 未知
公开(公告)号：BR112015021760A2
公开(公告)日：2017-07-18
申请号：BR112015021760
申请日：2014-03-06
申请人： COSMO OIL CO LTD
发明人： JUN LI , SHIGEYUKI WATANABE , YASUNOBU UEDA , YASUTOMO TAKEUCHI
IPC分类号： A01G7/00 , A01N37/44 , A01P21/00
摘要： resumo “acelerador de crescimento de planta” trata-se de um acelerador de crescimento de planta que compreende, como um ingrediente ativo, ácido 5-amino-4-hidroxipentanóico de fórmula (1) h2nch2ch(oh)ch2ch2coor1 (1) em que r1 representa um átomo de hidrogênio ou um grupo hidrocarboneto que tem de 1 a 10 átomos de carbono, um derivado do mesmo ou um sal do mesmo.

92. 发明专利

MY162163A HYDROCARBON COMPOUND SYNTHESIS REACTION SYSTEM AND FINELY DIVIDED PARTICLE REMOVAL METHOD 未知
公开(公告)号：MY162163A
公开(公告)日：2017-05-31
申请号：MYPI2010004266
申请日：2009-03-12
申请人： NIPPON STEEL ENG CO LTD , JAPAN OIL GAS & METALS JOGMEC , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN PETROLEUM EXPLORATION CO LTD , COSMO OIL CO LTD
发明人： ONISHI YASUHIRO , KATO YUZURU , MURATA ATSUSHI , YAMADA EIICHI
IPC分类号： C10G2/00 , B01D39/12 , B01J8/22
摘要： A SYNTHESIS REACTION SYSTEM (1) IS PROVIDED WITH: A REACTOR (10) WHICH SYNTHESIZES A HYDROCARBON COMPOUND BY A CHEMICAL REACTION OF A SYNTHESIS GAS INCLUDING HYDROGEN AND CARBON MONOXIDE AS MAIN COMPONENTS, AND A SLURRY HAVING SOLID CATALYST PARTICLES SUSPENDED IN LIQUID; A SEPARATOR (36) WHICH SEPARATES THE HYDROCARBON COMPOUND FROM THE SLURRY; AND A FILTERING DEVICE (91) WHICH FILTERS THE HYDROCARBON COMPOUND EXTRACTED FROM THE SEPARATOR TO TRAP POWDERED CATALYST PARTICLES.

93. 发明专利

EA026920B1 СПОСОБ ГИДРОКРЕКИНГА И СПОСОБ ПОЛУЧЕНИЯ МИНЕРАЛЬНОГО МАСЛА 未知
公开(公告)号：EA026920B1
公开(公告)日：2017-05-31
申请号：EA201290290
申请日：2010-10-26
申请人： JAPAN OIL GAS & METALS JOGMEC , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN PETROLEUM EXPLORATION CO LTD , COSMO OIL CO LTD , NIPPON STEEL ENG CO LTD
发明人： TASAKA KAZUHIKO , TANAKA YUICHI , IWAMA MARIE
IPC分类号： C10G47/36 , C10G2/00
摘要： Способгидрокрекингапарафиновойфракции, которыйвключаетстадиюгидрокрекингапарафиновойфракции, содержащейсяв жидкихуглеводородах, синтезированныхпореакциисинтезаФишера-Тропша, сполучениемтакимобразомпродуктагидрокрекинга, стадиюфракционнойперегонки, гдеуказанныйпродуктгидрокрекингаподаютв ректификационнуюколонну, вкоторойтемператураотборакубовойфракцииустановленанапостоянномзначении, иполучаютпоменьшеймересреднийдистилляти кубовоемаслоизуказаннойректификационнойколонны, стадиюрециркуляции, накоторойвсеуказанноекубовоемаслоповторноподаютнауказаннуюстадиюгидрокрекинга, истадиюконтролированиягидрокрекинга, накоторойконтролируютстадиюгидрокрекингапарафиновойфракциис использованиемскоростипотокауказанногокубовогомаслав качествеиндикатора.

94. 发明专利

AU2012233954B2 Hydrogenation refining catalyst and method for producing a hydrocarbon oil 未知
公开(公告)号：AU2012233954B2
公开(公告)日：2017-05-04
申请号：AU2012233954
申请日：2012-03-26
申请人： COSMO OIL CO LTD , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN OIL GAS & METALS JOGMEC , JAPAN PETROLEUM EXPLORATION CO LTD , NIPPON STEEL & SUMIKIN ENG CO
发明人： TANAKA YUICHI , NIITSUMA TAKUYA , TASAKA KAZUHIKO , IWAMA MARIE
IPC分类号： B01J23/42 , C10G45/62
摘要： This hydrogenation refining catalyst contains both a carrier containing an amorphous composite metal oxide having solid acidity, and at least one type of active metal selected from the noble metals of group 8 to group 10 of the periodic table and supported on the aforementioned carrier. This hydrogenation refining catalyst contains a carbonaceous material containing carbon atoms, and the amount of the carbonaceous material contained in the hydrogenation refining catalyst is 0.05-1 mass% in terms of carbon atoms.

95. 发明专利

AU2012233964B2 Kerosene base material production method and kerosene base material 未知
公开(公告)号：AU2012233964B2
公开(公告)日：2017-04-27
申请号：AU2012233964
申请日：2012-03-26
申请人： COSMO OIL CO LTD , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN OIL GAS & METALS JOGMEC , JAPAN PETROLEUM EXPLORATION CO LTD , NIPPON STEEL & SUMIKIN ENG CO
发明人： NIITSUMA TAKUYA
IPC分类号： C10L1/04 , C10G2/00 , C10G7/00
摘要： This kerosene base material production method is characterized in obtaining, by removing paraffin of seven carbons or less from a first distillate with an initial boiling point of 95 - 140°C and an end point of 240 - 280°C that is obtained from a hydrogenated oil of a Fischer-Tropsch synthetic oil, a second distillate wherein the content of paraffin of seven carbons or less is 0.1 - 0.7 mass%.

96. 发明专利

CA2906435C HYDROCARBON SYNTHESIS REACTION APPARATUS 未知
公开(公告)号：CA2906435C
公开(公告)日：2017-04-18
申请号：CA2906435
申请日：2014-03-19
申请人： JAPAN PETROLEUM EXPLORATION CO LTD , JAPAN OIL GAS & METALS JOGMEC , INPEX CORP , JX NIPPON OIL & ENERGY CORP , NIPPON STEEL & SUMIKIN ENG CO , COSMO OIL CO LTD
发明人： MURATA ATSUSHI , YAMADA EIICHI , MURAHASHI KAZUKI , KATO YUZURU , ONISHI YASUHIRO
IPC分类号： C10G2/00 , B01J8/22 , B03B5/28 , B03B5/64 , B03C1/00
摘要： This hydrocarbon synthesis apparatus is provided with: a reactor for bringing a syngas which comprises carbon monoxide gas and hydrogen gas as main components into contact with a slurry obtained by suspending a solid catalyst in a liquid hydrocarbon compound, and thus synthesizing liquid hydrocarbon compounds by a Fischer-Tropsch process; a filter which is provided in the reactor and which separates the liquid hydrocarbon compounds from the catalyst; and a pulverized catalyst particles discharging means for discharging pulverized catalyst particles to the outside of the reactor, said pulverized catalyst particles being formed by pulverization of the solid catalyst contained in the slurry.

97. 发明专利

EA026314B1 СИСТЕМА УПРАВЛЕНИЯ ТЕМПЕРАТУРОЙ 未知
公开(公告)号：EA026314B1
公开(公告)日：2017-03-31
申请号：EA201391020
申请日：2012-01-17
申请人： JAPAN OIL GAS & METALS JOGMEC , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN PETROLEUM EXPLORATION CO LTD , COSMO OIL CO LTD , NIPPON STEEL & SUMIKIN ENG CO
发明人： MORITA KENTAROU , KATO YUZURU
IPC分类号： B01J19/00 , C10G2/00
摘要： Системауправлениятемпературойпонастоящемуизобретениюявляетсясистемойуправлениятемпературойдляутилизациитеплотыреакциивнутриреактора, вкоторомпротекаетэкзотермическаяреакция, суправлениемтемсамымтемпературойвнутриреактора. Системауправлениятемпературойснабженабарабаномс охладителем, вкоторомжидкийохладительнаходитсяв состояниипарожидкостногоравновесия, блокомотводатепла, которыйрасположеннареакторедлявнутреннейциркуляциижидкогоохладителя, подаваемогоизбарабанас охладителем, блокомопределениятемпературы, которыйопределяеттемпературувнутриреактора, ирегуляторомдавления, которыйуправляетдавлениемвнутрибарабанас охладителем. Регулятордавленияуправляетдавлениемвнутрибарабанас охладителемнаосноверазностимеждуфактическойтемпературойвнутриреактора, определеннойблокомопределениятемпературы, ипредварительнозаданнымзначениемтемпературывнутриреактора, темсамымуправляятемпературойжидкогоохладителявнутрибарабанас охладителем.

98. 发明专利

MY160609A SYSTEM FOR SEPARATING CATALYST 未知
公开(公告)号：MY160609A
公开(公告)日：2017-03-15
申请号：MYPI2011001347
申请日：2009-09-25
申请人： JAPAN OIL GAS & METALS JOGMEC , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN PETROLEUM EXPLORATION CO LTD , COSMO OIL CO LTD , NIPPON STEEL ENG CO LTD
发明人： YASUHIRO ONISHI , YUZURU KATO , EIICHI YAMADA , KENTAROU MORITA
IPC分类号： B01J8/22 , B01J8/00 , C10G2/00
摘要： A SYSTEM (81) FOR CATALYST SEPARATION IN WHICH SOLID CATALYST PARTICLES ARE SEPARATED FROM A HYDROCARBON SYNTHESIZED BY THE CHEMICAL REACTION OF SYNTHESIS GAS COMPRISING HYDROGEN AND CARBON MONOXIDE AS MAJOR COMPONENTS WITH A SLURRY OBTAINED BY SUSPENDING THE CATALYST PARTICLES IN A LIQUID. THE SYSTEM (81) COMPRISES: A REACTOR (30); A STORAGE TANK (85) IN WHICH A SLURRY DISCHARGED FROM THE REACTOR (30) IS STORED; MULTIPLE FILTERS (104, 113) THROUGH WHICH THIS SLURRY IS FILTERED; AND A FILTRATE RESERVOIR IN WHICH A FILTRATE PASSED THROUGH THE MULTIPLE FILTERS IS COLLECTED, THE MULTIPLE FILTERS (104, 113) HAVING BEEN SERIALLY DISPOSED IN A SLURRY PASSAGEWAY LEADING FROM THE STORAGE TANK (85) TO THE FILTRATE RESERVOIR. (FIG. 2)

99. 发明专利

MY160346A METHOD FOR REMOVING SULFUR COMPOUNDS IN CASTABLE 未知
公开(公告)号：MY160346A
公开(公告)日：2017-02-28
申请号：MYPI2012003877
申请日：2011-02-21
申请人： JAPAN OIL GAS & METALS JOGMEC , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN PETROLEUM EXPLORATION CO LTD , COSMO OIL CO LTD , NIPPON STEEL ENG CO LTD , CHIYODA CORP
发明人： HODOSHIMA SHINYA , YAGI FUYUKI , WAKAMATSU SHUHEI , KAWAZUISHI KENICHI
IPC分类号： B01J8/00 , B01J8/02 , C01B3/24
摘要： A SITUATION WHERE SULFUR COMPOUNDS ORIGINATING FROM A CASTABLE ARE MIXED INTO SYNTHESIS GAS PRODUCED BY WAY OF A REFORMING REACTION AND THE MIXED SULFUR COMPOUNDS ARE SEPARATED AND COLLECTED WITH CARBON DIOXIDE AND FURTHER FED INTO A REFORMER TO THEREBY DEGRADE THE REFORMING CATALYST OF THE REFORMER BY SULFUR POISONING IS AVOIDED. PURGE GAS THAT IS STEAM OR STEAM-CONTAINING GAS IS MADE TO FLOW INTO THE PIPING TO BE USED FOR A SYNTHESIS GAS PRODUCTION APPARATUS AND DRIED OUT TO REMOVE THE SULFUR COMPOUNDS CONTAINED IN THE CASTABLE PRIOR TO THE START-UP OF OPERATION OF THE SYNTHESIS GAS PRODUCTION APPARATUS, IN ORDER TO PREVENT THE SULFUR COMPOUNDS FROM BEING RELEASED BY HOT SYNTHESIS GAS.

100. 发明专利

BR112013024490A2 método para interromper operação de reator 未知
公开(公告)号：BR112013024490A2
公开(公告)日：2016-12-27
申请号：BR112013024490
申请日：2012-03-15
申请人： COSMO OIL CO LTD , INPEX CORP , JAPAN OIL GAS & METALS JOGMEC , JAPAN PETROLEUM EXPLORATION CO LTD , JX NIPPON OIL & ENERGY CORP , NIPPON STEEL & SUMIKIN ENG CO
发明人： ARAI SHINYA
IPC分类号： C10G2/00
摘要： método para interromper operação de reator a presente invenção refere-se a método para interromper operação de um reator que inclui etapa de interromper suprimento de gás de síntese para interromper o suprimento de um gás de síntese contendo gás monóxido de carbono e gás hidrogênio ao reator, uma etapa de descarregar pasta para descarregar a pasta do reator; e uma etapa de suprir vapor para suprir vapor em uma temperatura mais alta que as temperaturas de decomposição das carbonilas metálicas ao reator, através do que descarregando a matéria gasosa no reator; e etapa de detectar gás monóxido de carbono para detectar a quantidade gás monóxido de carbono contida na matéria gasosa descarregada do reator. na etapa de suprir vapor, o suprimento de vapor é interrompido, quando a quantidade de gás monóxido de carbono declina continuamente para um valor menor que um valor de referência predeterminado.

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