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121. 发明申请

US20160312258A1 METHOD FOR PRODUCING FERMENTATION-RAW-MATERIAL SUGAR SOLUTION AND METHOD FOR PRODUCING CHEMICAL OBTAINED BY FERMENTING THE FERMENTATION-RAW-MATERIAL SUGAR SOLUTION 审中-公开
标题翻译：生产发酵原料糖解决方案的方法和生产通过发酵原料糖解决方案获得的化学品的方法
公开(公告)号：US20160312258A1
公开(公告)日：2016-10-27
申请号：US15101900
申请日：2013-12-06
申请人： JGC CORPORATION
发明人： MAKOTO IKEO , SHOHEI OKINO , DAISUKE TANEDA
IPC分类号： C12P19/14 , C12P19/02 , C12P7/14
CPC分类号： C12P19/14 , C12P7/10 , C12P7/14 , C12P7/16 , C12P7/18 , C12P7/46 , C12P7/56 , C12P19/02 , C12P2201/00 , C12P2203/00 , C13K1/02 , Y02E50/10 , Y02E50/16 , Y02E50/17
摘要： A method for producing a fermentation-raw-material sugar solution includes a step of saccharifying non-food biomass to obtain a low-concentration-sugar-containing solution, and a step of mixing the low-concentration-sugar-containing solution with a sugar or high-concentration-sugar-containing solution derived from food biomass to obtain a fermentation-raw-material sugar solution.
摘要翻译：发酵原料糖溶液的制造方法包括使非食品生物质糖化以获得低浓度含糖溶液的步骤，以及将低浓度含糖溶液与糖混合的步骤或来自食物生物质的高浓度含糖溶液以获得发酵原料糖溶液。

122. 发明申请

US20160238312A1 LIQUEFIED GAS PRODUCING FACILITY AND LIQUEFIED GAS PRODUCING METHOD 审中-公开
标题翻译：液化气生产设备和液化气生产方法
公开(公告)号：US20160238312A1
公开(公告)日：2016-08-18
申请号：US15023674
申请日：2015-01-14
申请人： JGC CORPORATION , ELBRONS B.V.
发明人： YUZURU KAKUTANI , TERU ASAKA , MARC ELLMER
IPC分类号： F25J1/00
CPC分类号： F25J1/0022 , B01D53/1462 , B01D2252/20 , B01D2256/245 , C10L3/101 , C10L3/102 , F25J1/004 , F25J1/0052 , F25J1/0055 , F25J1/0087 , F25J1/021 , F25J1/0216 , F25J1/0259 , F25J1/0283 , F25J1/0292 , F25J1/0296
摘要： A liquefied gas producing facility is provided and includes: a first heat exchanger, a first refrigerant compressor, a second heat exchanger, a second refrigerant compressor, air-cooling heat exchangers for a first refrigerant, air-cooling condensers for a first refrigerant, air-cooling heat exchangers for a second refrigerant, air-cooling condensers for a second refrigerant and a mist spraying device. The liquefied gas producing facility can produce liquefied gas by liquefying feed gas which contains methane as a main component.
摘要翻译：提供一种液化气体生产设备，包括：第一热交换器，第一制冷剂压缩机，第二热交换器，第二制冷剂压缩机，用于第一制冷剂的空气冷却热交换器，用于第一制冷剂的空气冷却冷凝器，空气用于第二制冷剂的冷却热交换器，用于第二制冷剂的冷却冷凝器和喷雾装置。液化气生产设备可以通过液化以甲烷为主要成分的原料气来生产液化气。

123. 发明授权

US09382169B2 Lower olefins producing catalyst and method for producing lower olefins using same 有权
标题翻译：低级烯烃生产催化剂和使用其生产低级烯烃的方法
公开(公告)号：US09382169B2
公开(公告)日：2016-07-05
申请号：US13333383
申请日：2011-12-21
申请人： Atsushi Okita , Kazunori Honda , Chizu Inaki , Jumpei Takahashi , Masashi Yamaguchi , Yumiko Yoshikawa , Shinji Iwade , Tohru Setoyama
发明人： Atsushi Okita , Kazunori Honda , Chizu Inaki , Jumpei Takahashi , Masashi Yamaguchi , Yumiko Yoshikawa , Shinji Iwade , Tohru Setoyama
IPC分类号： B01J29/06 , C07C1/20 , B01J29/40 , B01J35/02 , B01J37/00 , B01J35/00 , B01J37/02 , B01J35/04
CPC分类号： C07C1/20 , B01J29/40 , B01J35/0026 , B01J35/023 , B01J35/026 , B01J35/04 , B01J37/0009 , B01J37/0246 , B01J2229/186 , B01J2229/42 , C07C2521/04 , C07C2521/08 , C07C2521/16 , C07C2529/40 , C07C2529/70 , Y02P20/52 , Y02P30/42 , C07C11/04 , C07C11/06
摘要： A lower olefin producing catalyst which has high olefin production efficiency and maintains its activity for a long period of time when lower olefins are produced from an oxygen-containing compound, which is a solid catalyst used in producing lower olefins from an oxygen-containing compound, includes a solid-state catalyst component containing an MFI-type zeolite, in which, at a position where the shortest distance to the outer surface is maximum among all positions inside a structure of the solid catalyst, the thickness defined as a distance twice the shortest distance from the point to the outer surface is in a range of from 0.1 to 2.0 mm, and a method for producing lower olefins.
摘要翻译：一种低级烯烃生产催化剂，其具有高的烯烃生产效率，并且由含氧化合物制备低级烯烃长时间保持其活性，该含氧化合物是用于从含氧化合物制备低级烯烃的固体催化剂，包括含有MFI型沸石的固态催化剂组分，其中在固体催化剂结构内的所有位置中与外表面的最短距离最大的位置处的厚度定义为两倍最短的距离从点到外表面的距离在0.1至2.0mm的范围内，以及生产低级烯烃的方法。

124. 发明授权

US08956046B2 Bag with port member and connection structure thereof 有权
标题翻译：袋口及其连接结构
公开(公告)号：US08956046B2
公开(公告)日：2015-02-17
申请号：US13824272
申请日：2011-11-22
申请人： Kazuhiro Umenaka , Takeshi Kojima , Naomi Hashimoto , Toshiyuki Yamagishi , Kanehide Oota
发明人： Kazuhiro Umenaka , Takeshi Kojima , Naomi Hashimoto , Toshiyuki Yamagishi , Kanehide Oota
IPC分类号： B65D33/16 , B65D71/50 , B65D75/58
CPC分类号： B65D33/16 , B65D71/502 , B65D75/5872 , Y10S383/906
摘要： A bag with a port member according to the present invention includes a bag having an opening and a port member attached to the opening. In addition, the port member has a tubular insertion portion and a bag side connection portion that is connected to a container side connection portion of other container, and the bag is positioned on the innermost circumferential face side of the bag with a port member on an inner face of the insertion portion. According to the bag with a port member, the bag with a port member that can reduce a residual amount of contents to be as small as possible when the contents inside the bag are taken out can be provided.
摘要翻译：根据本发明的具有端口构件的袋包括具有开口的袋和附接到开口的端口构件。另外，端口部件具有与其他容器的容器侧连接部连接的管状插入部和袋侧连接部，袋位于袋的最内周面侧，端口部件位于插入部分的内表面。根据具有端口构件的袋，可以提供具有端口构件的袋，当取出袋中的内容物时，可以减少残留量的内容物尽可能小。

125. 发明授权

US08865434B2 Method of producing saccharides containing glucose as major constituent 有权
标题翻译：以葡萄糖为主要成分的糖类生产方法
公开(公告)号：US08865434B2
公开(公告)日：2014-10-21
申请号：US13335697
申请日：2011-12-22
申请人： Daisuke Taneda , Makoto Ikeo
发明人： Daisuke Taneda , Makoto Ikeo
IPC分类号： C12P19/14
CPC分类号： C12P19/14
摘要： A method of producing saccharides containing glucose as the major constituent by degrading at least one selected from the group consisting of cellulose and hemicellulose with a cellulose saccharifying enzyme is provided. The method includes the steps of: mixing a cellulose material and a solution containing cellulose saccharifying enzyme to prepare a mixture; and saccharifying the cellulose material with the saccharifying enzyme. A gross energy density Y (W/m3) subjected to the mixture and a substrate concentration X (w/v%) of the cellulose material to the enzyme solution satisfy a formula (1) below during the step of saccharifying. Y≦−0.0125X2+1.195X+23.25 (1)
摘要翻译：提供了通过用纤维素糖化酶降解从纤维素和半纤维素组成的组中选出的至少一种来生产含有葡萄糖作为主要成分的糖的方法。该方法包括以下步骤：将纤维素材料和含有纤维素糖化酶的溶液混合以制备混合物; 并用糖化酶糖化纤维素材料。经过混合物的总能量密度Y（W / m3）和纤维素材料的底物浓度X（w / v％）与酶溶液在糖化步骤中满足下式（1）。 Y＆nlE; -0.0125X2 + 1.195X + 23.25（1）

126. 发明申请

US20140017162A1 SULFUR RECOVERY UNIT AND SULFUR RECOVERY METHOD 有权
标题翻译： SULFUR恢复单元和SULFUR恢复方法
公开(公告)号：US20140017162A1
公开(公告)日：2014-01-16
申请号：US14007971
申请日：2012-04-02
申请人： Tatsuo Kamisuki , Hiroyuki Kosasayama , Yasushi Yamada , Shingo Arai , Mitsuru Kida
发明人： Tatsuo Kamisuki , Hiroyuki Kosasayama , Yasushi Yamada , Shingo Arai , Mitsuru Kida
IPC分类号： C01B17/04 , B01J12/00
CPC分类号： C01B17/0447 , B01J8/0419 , B01J12/00 , B01J2208/00256 , B01J2208/0053 , C01B17/0404 , C01B17/0417
摘要： A sulfur recovery unit comprising: a reaction furnace configured to carry out a high-temperature Claus reaction between hydrogen-sulfide-containing gas and oxygen-containing gas introduced to the reaction furnace; a sulfur condenser configured to cool reaction gas discharged from the reaction furnace and condense sulfur contained in the reaction gas; and a pipe that connects the reaction furnace to the sulfur condenser, wherein the reaction furnace is fixed to the ground; and the sulfur condenser and the pipe are arranged so as to be able to move relative to the reaction furnace.
摘要翻译：一种硫回收装置，其特征在于，包括：反应炉，其配置为在含有硫化氢的气体和导入所述反应炉的含氧气体之间进行高温克劳斯反应; 硫冷凝器，其构造为冷却从反应炉排出的反应气体，并冷凝反应气体中所含的硫; 以及将反应炉连接到硫冷凝器的管，其中反应炉固定在地面上; 并且硫冷凝器和管被布置成能够相对于反应炉移动。

127. 发明授权

US08551442B2 Reactor for synthesizing hydrogen sulfide, apparatus for producing hydrogen sulfide, apparatus for producing sodium hydrogen sulfide, method for producing hydrogen sulfide, and method for producing sodium hydrogen sulfide 有权
标题翻译：硫化氢的合成反应器，硫化氢的制造装置，硫化氢的制造装置，硫化氢的制造方法以及硫化氢的制造方法
公开(公告)号：US08551442B2
公开(公告)日：2013-10-08
申请号：US13781757
申请日：2013-03-01
申请人： Hiroshi Umino , Nobuhiro Yamada , Tsutomu Katagiri , Hiromitsu Shibuya , Shuichi Oguro , Naoyoshi Iwasaki
发明人： Hiroshi Umino , Nobuhiro Yamada , Tsutomu Katagiri , Hiromitsu Shibuya , Shuichi Oguro , Naoyoshi Iwasaki
IPC分类号： B01J19/00 , C01B17/16 , C01B17/32
CPC分类号： B01J19/0013 , C01B17/162 , C01B17/32
摘要： A reactor for synthesizing hydrogen sulfide in which sulfur and hydrogen are subjected to gas-phase reaction in the absence of a catalyst to synthesize hydrogen sulfide, the reactor including: a reactor body that retains liquid sulfur in a bottom portion thereof; a heating unit that gasifies part of the liquid sulfur; a hydrogen gas supply unit that supplies hydrogen gas into the liquid sulfur; and a heat-exchanging portion provided in a gas-phase reaction region located above the liquid surface of the liquid sulfur in the reactor body, wherein heat-exchanging portion is configured such that the reaction temperature in the gas-phase reaction region is controlled to be within a predetermined temperature range by changing the heat exchange amount per unit volume in a gas-phase reaction region located farther from the liquid surface from the heat exchange amount per unit volume in a gas-phase reaction region located closer to the liquid surface.
摘要翻译：一种用于合成硫化氢的反应器，其中硫和氢在不存在催化剂的情况下进行气相反应合成硫化氢，反应器包括：在其底部保留液态硫的反应器体; 加热单元，其使部分液体硫气化; 将氢气供给到液体硫中的氢气供给单元; 以及设置在位于反应器主体中的液体硫的液面上方的气相反应区域中的热交换部，其中，热交换部被配置为使气相反应区域的反应温度为在位于更靠近液面的气相反应区域内，通过使位于比液面更靠近的气相反应区域的每单位体积的热交换量与单位体积的热交换量相比，将单位体积的热交换量变更为预定的温度范围。

128. 发明授权

US07857964B2 Method of refining heavy oil and refining apparatus 有权
标题翻译：重油和精炼装置的精炼方法
公开(公告)号：US07857964B2
公开(公告)日：2010-12-28
申请号：US10468508
申请日：2002-02-19
申请人： Yoshinori Mashiko , Akira Sugimoto , Tsuyoshi Okada
发明人： Yoshinori Mashiko , Akira Sugimoto , Tsuyoshi Okada
IPC分类号： C10G67/04 , B01D11/00
CPC分类号： C10G67/0463 , C10G21/003 , C10G21/14 , C10G21/30 , C10G67/0418 , C10G67/0436 , C10G67/049 , Y10S208/01
摘要： The present invention relates to a method in which grades of oil are refined according to their object from a feed oil. This method has a solvent extraction process that obtains an extracted oil, and a hydrogenation process that subjects the obtained extracted oil to hydrogenation process in the presence of hydrogen and a catalyst to obtain a hydrorefined oil. The solvent extraction conditions are selected by using the poly-aromatic concentration as an index for calculating the concentration of heptane insoluble components in the residue of the extracted oil obtained by the solvent extraction process that cannot be fractionally distilled.
摘要翻译：本发明涉及一种根据其来自进料油的目的对油等级进行精炼的方法。该方法具有获得萃取油的溶剂萃取方法以及在氢气和催化剂存在下使所得萃取油进行氢化处理以获得加氢精制油的氢化方法。通过使用聚芳族浓度作为计算通过不能分馏的溶剂萃取方法得到的提取油残留物中庚烷不溶成分的浓度的指标来选择溶剂萃取条件。

129. 发明申请

US20100200812A1 PRODUCTION METHOD FOR RAW GAS FOR AMMONIA SYNTHESIS AND PRODUCTION APPARATUS THEREFOR 审中-公开
标题翻译：用于氨合成原料气的生产方法及其生产装置
公开(公告)号：US20100200812A1
公开(公告)日：2010-08-12
申请号：US12677297
申请日：2007-11-29
申请人： Nobuhiro Yamada , Yoshinori Mashiko , Shuichi Funatsu , Yoshiyuki Watanabe
发明人： Nobuhiro Yamada , Yoshinori Mashiko , Shuichi Funatsu , Yoshiyuki Watanabe
IPC分类号： C09K3/00 , B01J8/02
CPC分类号： C01B3/382 , C01B3/025 , C01B3/386 , C01B3/48 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/0445 , C01B2203/047 , C01B2203/0475 , C01B2203/068
摘要： There is provided a method for producing a raw gas for ammonia synthesis in which light hydrocarbons from a tube 3, steam from a tube 6 and oxygen-enriched air having an oxygen concentration of 40 to 60% by volume from an oxygen-enriched air supply source 7 are heated and are then introduced to a one-step reforming reactor 5 to thereby carry out a steam reforming reaction and an air partial oxidation reaction at the same time, and the resultant is subsequently passed through a shift reactor 12, a decarbonating device 14 and a methanation reactor 16 to remove carbon monoxide and carbon dioxide, thereby yielding a raw gas suitable for ammonia synthesis having a hydrogen to nitrogen molar ratio of about 3:1.
摘要翻译：提供了一种用于氨合成的原料气体的制造方法，其中来自管3的轻烃，来自管6的蒸汽和氧浓度为40至60体积％的富氧空气从富氧空气供应源7被加热，然后被引入一步重整反应器5中，从而同时进行蒸汽重整反应和空气部分氧化反应，然后使所得物经过变换反应器12，脱碳装置 14和甲烷化反应器16，以除去一氧化碳和二氧化碳，从而产生适合氨合成的原料气体，其氢 - 氮摩尔比为约3:1。

130. 发明申请

US20100179366A1 PROCESS AND APPARATUS FOR PRODUCING PROPYLENE 有权
标题翻译：生产丙烯的方法和装置
公开(公告)号：US20100179366A1
公开(公告)日：2010-07-15
申请号：US12376772
申请日：2007-09-19
申请人： Hirofumi Ito , Jiro Yoshida , Shuichi Funatsu , Koji Ooyama , Nobuyasu Chikamatsu
发明人： Hirofumi Ito , Jiro Yoshida , Shuichi Funatsu , Koji Ooyama , Nobuyasu Chikamatsu
IPC分类号： C07C1/20 , B01J8/00
CPC分类号： C07C2/06 , C07C1/20 , C07C2523/02 , C07C2529/40 , Y02P20/52 , C07C11/06
摘要： A process for producing propylene, which including feeding at least one of dimethyl ether and methanol to a reactor to be reacted in the presence of a catalyst; supplying an obtained reaction product to a separator by which low-boiling compounds having a boiling point of −50° C. or lower at atmospheric pressure among the reaction product are separated; and recycling a proportion of at least 70% of a total amount of the separated low-boiling compounds to said reactor.
摘要翻译：一种生产丙烯的方法，其包括将二甲醚和甲醇中的至少一种进料到在催化剂存在下反应的反应器中; 将得到的反应产物供给到反应产物中的大气压下沸点为-50℃以下的低沸点化合物的分离器; 并将所分离的低沸点化合物的总量的至少70％的比例再循环到所述反应器中。

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