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    • 4. 发明公开
    • MEMBRANE VESSEL USED IN DEWATERING DEVICE
    • 在EINERENTWÄSSERUNGSVORRICHTUNGVERWENDETESMEMBRANGEFÄSS
    • EP2617481A1
    • 2013-07-24
    • EP11824992.9
    • 2011-09-01
    • Mitsubishi Heavy Industries, Ltd.
    • TANAKA, YukioTACHIBANA, ShinyaOSORA, HiroyukiOGINO, ShinjiHIRAYAMA, Haruaki
    • B01D63/00B01D63/06
    • B01D63/00B01D61/366B01D61/368B01D63/066B01D65/00B01D2313/08B01D2313/086B01D2313/20
    • Provided is a membrane container 6 used in a dehydrator 1. The membrane container 6 according to the present invention has: a casing 10 including a fluid inlet 14 through which treated fluid flows; and a fluid outlet 16 from which the treated fluid flows out; and a membrane container body 9 including a plurality of flow paths 11 which is arranged along the flow direction of the treated fluid and in parallel to one another. Each of the plurality of flow paths 11 includes a most upstream portion 11A which is connected to the fluid inlet 14, and a most downstream portion 11C which is connected to the fluid outlet 16. Return portions 15 and 17 configured to reverse the flow direction of the treated fluid are provided between the most upstream portion 11A and the most downstream portion 11C. After passing through the fluid inlet 14, the treated fluid flows from the most upstream portion 11A down to the most downstream portion 11C via the return portions 15 and the upper return portion 17.
    • 设置有用于脱水机1的膜容器6.本发明的膜容器6具有:包括流体入口14的壳体10,被处理流体流过该流体入口14; 和流体出口16,经处理的流体从该出口流出; 以及膜容器主体9,其包括沿着被处理流体的流动方向并且彼此平行配置的多个流路11。 多个流路11中的每一个包括连接到流体入口14的最上游部分11A和连接到流体出口16的最下游部分11C。构造成使流体流动方向反转的返回部分15和17 被处理流体设置在最上游部分11A和最下游部分11C之间。 经过流体入口14后,处理过的流体经由返回部分15和上返回部分17从最上游部分11A向下流动到最下游部分11C。
    • 6. 发明公开
    • AMMONIA SYNTHESIS SYSTEM AND METHOD
    • 氨合成系统和方法
    • EP3190088A1
    • 2017-07-12
    • EP15837863.8
    • 2015-04-21
    • Mitsubishi Heavy Industries, Ltd.
    • SAKURAI, MikiyaTANAKA, YukioOKUZUMI, NaoyaOSORA, HiroyukiHIRAYAMA, Haruaki
    • C01C1/02
    • C01C1/047B01D53/002B01J23/462B01J23/58B01J23/63C01C1/02C01C1/0411C09K5/04F25B9/002Y02P20/52
    • The present invention comprises: an ammonia converter 13 that synthesizes ammonia; a discharge line L 11 that discharges a synthesis gas 14 which includes an obtained ammonia gas 12A and an unreacted source gas 11A; a water cooled condenser 16 that is interdisposed in the discharge line L 11 and cools the synthesis gas 14 with a coolant 15; an ammonia separator 17 into which the cooled synthesis gas 14A is introduced, said separator 17 separating the ammonia gas 12A and liquid ammonia 12B; a source return line L 12 that returns the source gas including the separated ammonia gas 12A to the ammonia converter 13 side as a return source gas 11B; and a compressor 18 that is interdisposed in the source return line L 12 and compresses the return source gas 11B. The ammonia concentration in the return source gas 11B intro - duced into the ammonia converter 13 is 5 mol% or more and an ammonia synthesis catalyst that synthesizes the ammonia gas 12A in the ammonia converter 13 is a ruthenium catalyst.
    • 本发明包括:合成氨的氨转化器13; 排出包含获得的氨气12A和未反应的原料气体11A的合成气体14的排出管线L11; 水冷冷凝器16,其插置在排放管线L11中并用冷却剂15冷却合成气体14; 将冷却的合成气体14A导入其中的氨分离器17,所述分离器17分离氨气12A和液氨12B; 将包含分离出的氨气12A的原料气体作为返回原料气体11B返回到氨气转换器13侧的原料返回管线L12; 以及插入到源返回管线L12并压缩返回源气体11B的压缩机18。 在氨转换器13中流入的返回原料气体11B中的氨浓度为5摩尔%以上,在氨转换器13中合成氨气体12A的氨合成催化剂为钌催化剂。
    • 10. 发明公开
    • DEHYDRATOR
    • 脱水机
    • EP2230003A1
    • 2010-09-22
    • EP09702932.6
    • 2009-01-13
    • Mitsubishi Heavy Industries, Ltd.
    • YUKUMOTO, AtsuhiroOSORA, HiroyukiSEIKI, YoshioHIRAYAMA, HaruakiTANAKA, YukioKASHIWAGI, HideoINOUE, Katsufumi
    • B01D61/36B01D61/58C07C29/76C07C31/08
    • B01D61/362B01D61/58B01D2313/24B01D2317/022C07C29/76C07C31/08
    • Provided is a dehydrator that requires no excessively large apparatus structure and achieves cost-saving while maintaining suction efficiency at a desired level by use of suction means. A dehydrator 100 for separating water from a target liquid 13 includes at least two water separation membrane units 1a and 1b which are provided in series in a flow direction of the target liquid 13. The water separation membrane unit 1a on an upstream side out of the water separation membrane units 1a and 1b is connected to suction means 7 for sucking a gas phase containing water through one condenser 4, and the one condenser 4 condenses water in the gas phase and thereby separates the water. The gas phase sucked by the suction means 7 from the one condenser 4 is transferred to at least one downstream condenser 8 provided downstream of the one condenser 4, and the downstream condenser 8 condenses water in the gas phase and thereby separates the water. The water separation membrane unit 1b on a downstream side of the water separation membrane unit 1a is connected to a steam ejector 3, and the condenser 4 for condensing water in a gas phase passed through the steam ejector 3 condenses water and thereby separates the water.
    • 本发明提供一种脱水装置,其不需要过大的装置结构,并且通过使用吸引装置将吸引效率维持在所希望的水平的同时实现成本节约。 用于从目标液体13中分离水的脱水器100包括沿目标液体13的流动方向串联设置的至少两个脱水膜单元1a和1b。在脱水器100的上游侧的脱水膜单元1a 水分离膜单元1a和1b连接到抽吸装置7,用于通过一个冷凝器4抽吸含水的气相,并且该一个冷凝器4冷凝气相中的水,从而分离水。 由吸入装置7从一个冷凝器4吸入的气相转移到设置在一个冷凝器4下游的至少一个下游冷凝器8,而下游冷凝器8冷凝气相水并由此分离水。 在水分离膜单元1a的下游侧的水分离膜单元1b连接到蒸汽喷射器3,并且用于冷凝通过蒸汽喷射器3的气相水的冷凝器4冷凝水从而分离水。