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    • 42. 发明专利
    • Nitrogen manufacturing method and device
    • 硝酸盐制造方法和装置
    • JP2008164236A
    • 2008-07-17
    • JP2006355080
    • 2006-12-28
    • Taiyo Nippon Sanso Corp大陽日酸株式会社
    • IRISAWA MAKOTOTACHIBANA HIROSHINOJIMA TOSHIYUKI
    • F25J3/04
    • F25J3/04424F25J3/04254F25J3/04284F25J3/04624F25J2200/04F25J2200/54F25J2205/02F25J2210/42F25J2250/20
    • PROBLEM TO BE SOLVED: To provide a nitrogen manufacturing method and device with a high product yield even when a product nitrogen pressure is low.
      SOLUTION: First raw material air is separated into first nitrogen gas and a first oxygen enriched liquefied fluid, the first oxygen enriched liquefied fluid is separated into second raw material air and a second oxygen enriched liquefied fluid, and indirect heat exchange of the second oxygen enriched liquefied fluid and the first nitrogen gas is carried out to produce first liquefied nitrogen and a first oxygen enriched gas fluid. Second raw material air is separated into second nitrogen gas and a third oxygen enriched liquefied fluid, indirect heat exchange is carried out between the second nitrogen gas and the third oxygen enriched liquefied fluid to produce second liquefied nitrogen and a second oxygen enriched gas fluid, indirect heat exchange is carried out between the second oxygen enriched liquefied fluid and the first nitrogen gas to produce the first liquefied nitrogen and a third oxygen enriched gas fluid, and the first nitrogen gas is derived as a first product nitrogen gas and the second nitrogen gas is derived as a second product nitrogen gas.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:即使当产品氮压低时,也提供具有高产品产率的氮气制造方法和装置。 解决方案:将第一原料空气分离成第一氮气和第一富氧液化液,将第一富氧液化流体分离成第二原料空气和第二富氧液化流体,并间接换热 第二富氧液化流体和第一氮气被执行以产生第一液化氮气和第一富氧气体流体。 将第二原料空气分离成第二氮气和第三富氧液化液,在第二氮气和第三富氧液化液之间进行间接热交换,以产生第二液化氮和第二富氧气体流体,间接 在第二富氧液化流体和第一氮气之间进行热交换以产生第一液化氮和第三富氧气体流体,第一氮气作为第一产物氮气导出,第二氮气为 作为第二产品氮气导出。 版权所有(C)2008,JPO&INPIT
    • 44. 发明专利
    • Air separation device
    • 空气分离装置
    • JP2007205714A
    • 2007-08-16
    • JP2007122811
    • 2007-05-07
    • Kobe Steel Ltd株式会社神戸製鋼所
    • HASHIMOTO TAMOTSUOYAMA TAKASHITOMISAKA YASUSHI
    • F25J3/04
    • F25J3/04303F25J3/0409F25J3/04206F25J3/04224F25J3/04284F25J3/044F25J3/04412F25J3/04478F25J3/04509F25J2200/72F25J2235/04F25J2250/40F25J2250/42F25J2250/50F25J2290/62
    • PROBLEM TO BE SOLVED: To provide a technique capable of extracting a product gas until an air separation device comes into a normal operation after restarting the operation of the air separation device. SOLUTION: This air separation device is provided with: a high-pressure distillation tower and a low-pressure distillation tower for separating material air into liquid oxygen and liquid nitrogen; a liquid storage tank for storing the separated liquid oxygen or liquid nitrogen; and a heat exchanger for evaporating and converting the liquid oxygen and/or the liquid nitrogen into a product gas by using compressed material air as a heat source. This air separation device is characterized in that a liquid extraction amount regulation valve is arranged in a line connecting the distillation tower to the liquid storage tank, and the device is provided with a pressing means for adjusting pressure in the liquid storage tank independently of the distillation tower when the liquid extraction amount regulation valve is closed. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种能够抽出产物气体直到空分装置在重新启动空气分离装置的操作之后进入正常操作的技术。 解决方案:该空气分离装置设有:高压蒸馏塔和用于将空气分离成液氧和液氮的低压蒸馏塔; 用于储存分离的液氧或液氮的液体储存罐; 以及通过使用压缩材料空气作为热源将液态氧和/或液氮蒸发并转化成产品气体的热交换器。 该空气分离装置的特征在于,在连接蒸馏塔与液体储罐的管路上配置有液体提取量调节阀,该装置设有用于独立于蒸馏调节储液罐内的压力的按压装置 液体提取量调节阀关闭时塔。 版权所有(C)2007,JPO&INPIT
    • 47. 发明专利
    • Air separating method and its device
    • 空气分离方法及其装置
    • JP2006284075A
    • 2006-10-19
    • JP2005103645
    • 2005-03-31
    • Taiyo Nippon Sanso Corp大陽日酸株式会社
    • NOJIMA TOSHIYUKITATSUMI TAKASHI
    • F25J3/04
    • F25J3/04254F25J3/04284F25J3/04315F25J3/0443F25J2200/34F25J2210/40F25J2210/42F25J2210/50F25J2230/52F25J2245/02
    • PROBLEM TO BE SOLVED: To provide an air separating method having simple and easy-to-control construction for taking out medium pressure product nitrogen gas and medium pressure product oxygen gas while reducing a product power consumption rate without using an oxygen gas compressor or a liquid oxygen pump, and to provide its device.
      SOLUTION: The air separating method comprises a first separation step of using a high pressure tower 5 for separating material air into nitrogen gas fluid and first oxygen enriched liquefied fluid, a second separation step of using an auxiliary tower 7 for separating the first oxygen enriched liquefied fluid into air composition fluid and second oxygen enriched liquefied fluid, a first indirect heat exchange step of using a condenser 12 at the lower part of the auxiliary tower 7 for indirect heat exchange between the nitrogen gas fluid and the second oxygen enriched liquefied fluid, a third separation step of a low pressure tower 20 for separating a second oxygen enriched gas fluid into third oxygen enriched gas fluid and liquefied oxygen, a compression step of using an air booster 51 for compressing the air composition fluid, a second indirect heat exchange step of using an evaporator 21 at the lower part of the low pressure tower 20 for indirect heat exchange between the air composition fluid and the liquefied oxygen, a product nitrogen gas collection step, and a product oxygen gas collection step.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种空气分离方法,其具有简单易于控制的结构,用于在不使用氧气压缩机的同时降低产品功率消耗速率而取出中压产品氮气和中压产品氧气 或液氧泵,并提供其设备。 解决方案:空气分离方法包括使用高压塔5将材料空气分离成氮气流体和第一富氧液化液的第一分离步骤,使用辅助塔7分离第一分离步骤的第一分离步骤 富氧液化流体进入空气组合物流体和第二富氧液化流体,第一间接热交换步骤,在辅助塔7的下部使用冷凝器12,用于氮气流体和第二富氧液化塔之间的间接热交换 流体,用于将第二富氧气体流体分离为第三富氧气体流体和液化氧的低压塔20的第三分离步骤,使用用于压缩空气组成流体的空气增压器51的压缩步骤,第二间接热 在低压塔20的下部使用蒸发器21进行间接热交换的交换步骤 液体和液化氧,产品氮气收集步骤和产物氧气收集步骤。 版权所有(C)2007,JPO&INPIT
    • 48. 发明专利
    • Nitrogen manufacturing method and device
    • 硝酸盐制造方法和装置
    • JP2006132854A
    • 2006-05-25
    • JP2004323273
    • 2004-11-08
    • Taiyo Nippon Sanso Corp大陽日酸株式会社
    • IRISAWA MAKOTONOJIMA TOSHIYUKITATSUMI TAKASHI
    • F25J3/04
    • F25J3/04254F25J3/04284F25J3/04303F25J3/04424F25J2210/42
    • PROBLEM TO BE SOLVED: To provide a nitrogen manufacturing method and device capable of efficiently supplying product nitrogen.
      SOLUTION: The nitrogen manufacturing method comprises a first separating process of carrying out low temperature distillation of raw material air at a pressure of 0.8-1.1 MPa; a first indirect heat exchange process of carrying out indirect heat exchange between a first nitrogen gas and a first oxygen enriched liquefied fluid separated in the first separating process, to obtain a first liquefied nitrogen and a first oxygen enriched gas fluid; a second separating process of carrying out low temperature distillation of the first oxygen enriched gas fluid; a second indirect heat exchange process of carrying out indirect heat exchange between a second nitrogen gas and a second oxygen enriched liquefied fluid separated in the second separating process, to obtain a second liquefied nitrogen and a second oxygen enriched gas fluid; a cold generating process of adiabatically expanding the second oxygen enriched gas fluid to generate cold; a first product recovery process of leading out a part of the first nitrogen gas as a first product nitrogen gas; and a second product recovery process of leading out a part of the second nitrogen gas as a second product nitrogen gas after heat recovery.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供能够有效地供应氮气的氮气制造方法和装置。 解决方案:氮气制备方法包括在0.8-1.1MPa的压力下进行原料空气的低温蒸馏的第一分离过程; 在第一分离过程中分离的第一氮气和第一富氧液化流体之间进行间接热交换的第一间接热交换过程,以获得第一液化氮和第一富氧气体流体; 对第一富氧气体流体进行低温蒸馏的第二分离过程; 第二间接热交换过程,其在第二分离过程中分离的第二氮气和第二富氧液化流体之间进行间接热交换,以获得第二液化氮和第二富氧气体流体; 将第二富氧气体流体绝热膨胀以产生冷的冷产生过程; 将第一氮气作为第一产物氮气导出的第一产物回收过程; 以及第二产物回收过程,其在热回收之后引出一部分第二氮气作为第二产物氮气。 版权所有(C)2006,JPO&NCIPI