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    • 3. 发明专利
    • Method for optimizing food material transportation network
    • 优化食品运输网络的方法
    • JP2012138000A
    • 2012-07-19
    • JP2010290852
    • 2010-12-27
    • Mayekawa Mfg Co LtdSimulation Technology Kk有限会社シミュレーション・テクノロジー株式会社前川製作所
    • YOSHIKAWA TOMOIKUITO KAZUTOSHITATSUMI HIROYUKI
    • G06Q50/28
    • PROBLEM TO BE SOLVED: To provide a method for optimizing a food material transportation network, capable of optimizing the food material transportation network so as to achieve an optimal economical efficiency, and capable of evaluating the effectiveness of enhancement and improvement of transportation means against food material loss and supply deficiency at a demander.SOLUTION: Data of: the freshness deterioration speed of a selected food material; the maximum transport capacity for each kind of transport means; average speed and food material temperature during transportation; the position of a supply source and the degree of freshness deterioration at a carry-out time; the position of a cargo booking delivery center, the upper limit value of the degree of freshness deterioration of the food material at a receiving time and the increase value of the degree of freshness deterioration of the food material in the cargo booking delivery center; the position of a demander, its food material demand amount and the upper limit value of the degree of freshness deterioration of the food material at a receiving time; the sales price of the food material corresponding to the degree of freshness deterioration; and the transport cost and constraint condition for each kind of transport means are input to a computer. Then, the transport amount of the food material as an optimization variable and the total profit of whole food material transport network as an object function are set, and the computer is caused to calculate the transport amount for each kind of transport means at which the object function becomes maximum under the input conditions.
    • 要解决的问题:提供一种优化食品物料运输网络的方法,能够优化食品运输网络,从而达到最佳的经济效益,并能够评估运输手段的增强和改进的有效性 针对需求者的食品损失和供应缺陷。 数据:所选食品的新鲜度下降速度; 每种运输工具的最大运输能力; 运输过程中平均速度和食物料温度; 供应源的位置和进出时间的新鲜度变质程度; 货物预订配送中心的位置,接收时间食品材料的新鲜度变化程度的上限值以及货物预订交付中心的食品的新鲜度变差程度的增加值; 需求者的位置,其食品需求量和食品在接收时的新鲜度变化程度的上限值; 食品的销售价格对应于新鲜度的变质程度; 并且将各种传送装置的传输成本和约束条件输入到计算机。 然后,将作为优化变量的食品材料的输送量和作为目标函数的整个食品输送网络的总利润进行设定,并且使计算机计算出各种运送装置的运送量, 功能在输入条件下变为最大值。 版权所有(C)2012,JPO&INPIT
    • 4. 发明专利
    • Dual refrigerating cycle device
    • 双制冷循环装置
    • JP2008224206A
    • 2008-09-25
    • JP2008096627
    • 2008-04-02
    • Mayekawa Mfg Co Ltd株式会社前川製作所
    • FUJIMA KATSUMIAKABOSHI SHINJIROYOSHIKAWA TOMOIKU
    • F25B7/00F25B1/00F25B9/06F25B43/00
    • F25B9/008F25B1/10F25B2309/061
    • PROBLEM TO BE SOLVED: To provide a cryogenic cooling object fluid by a device easy in maneuvering operation and maintenance by reducing the number of constituting apparatuses by a simple structure, in a refrigerator using a carbon dioxide as a refrigerant in a dual refrigerating cycle device.
      SOLUTION: This dual refrigerating cycle device has a compressor in which a low-dimensional refrigerant can circulate between a cascade heat exchanger 31 and a condenser 2 and which compresses the carbon dioxide to saturation pressure or supercritical pressure at a temperature of an ordinary temperature level, the condenser for forming a high-pressure carbon dioxide from the compressor as a carbon dioxide liquid or a supercritical carbon dioxide fluid by cooling by the low-dimensional refrigerant circulating between the cascade heat exchanger and the condenser, a CO2 expander 3 for forming a CO2 liquid or a supercritical CO2 fluid from the condenser as solid-gas two-phase CO2 being a mixture of solid CO2 and CO2 gas by reducing pressure to pressure and a temperature level of a triple point or lower of CO2, and a CO2 sublimating means for sending the sublimated CO2 gas to the compressor by supplying cold heat by the sublimation of the solid-gas two-phase CO2 to the cooling object fluid from a cooling load 6.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 解决的问题:通过简单的结构,通过减少构成装置的数量,通过容易操作和维护的装置,在使用双重制冷的二氧化碳作为制冷剂的冰箱中提供低温冷却对象流体 循环装置。 解决方案:该双制冷循环装置具有压缩机,其中低维制冷剂可在级联热交换器31和冷凝器2之间循环,并且在普通温度下将二氧化碳压缩至饱和压力或超临界压力 温度水平的冷凝器,用于通过在级联热交换器和冷凝器之间循环的低维制冷剂冷却而从压缩机形成高压二氧化碳作为二氧化碳液体或超临界二氧化碳流体的冷凝器,用于 通过降低压力和三重或更低的二氧化碳的温度水平,形成来自冷凝器的CO 2液体或超临界CO 2流体,作为固体CO 2和CO 2气体的混合物的固体气体二相CO 2 升华装置,用于通过将固体气体二相CO 2的升华向冷却对象流体提供冷热来将升华的CO 2气体送入压缩机 d从冷负荷6。版权所有(C)2008,JPO&INPIT
    • 5. 发明专利
    • Method and apparatus for preparing dry ice
    • 干冰制备方法与装置
    • JP2008214190A
    • 2008-09-18
    • JP2008158338
    • 2008-06-17
    • Mayekawa Mfg Co Ltd株式会社前川製作所
    • MATSUDA JUNJIFUJIMA KATSUMIYOSHIKAWA TOMOIKUSUZUKI HIROYUKI
    • C01B32/55C01B32/50
    • Y02P20/544
    • PROBLEM TO BE SOLVED: To provide a method and an apparatus for preparing dry ice where high concentration gaseous CO 2 recovered utilizing factory exhaust heat is used for a refrigerant of a CO 2 liquefying cycle, further, by a supercooled supercritical CO 2 cooled by cold utilizing exhaust heat, the increase of function and the increase of efficiency are made possible, and to provide an apparatus therefor. SOLUTION: Utilizing high concentration gaseous CO 2 recovered utilizing factory exhaust heat as a refrigerant, supercooled supercritical CO 2 is formed by a compressor 12, and gaseous CO 2 coolers 26, 27, 28, the supercooled supercritical CO 2 is separated into liquefied CO 2 and gaseous CO 2 by a first gas-liquid separation pressure reduction means 31, the gaseous CO 2 is made to flow back to the compressor 12, so as to form a CO 2 liquefying cycle, from the liquefied CO 2 , the gaseous CO 2 is separated together with the production of dry ice by a second gas-liquid separation pressure reduction means 33, and the gaseous CO 2 is made to flow back to the CO 2 liquefying cycle. COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种制备干冰的方法和装置,其中使用工厂废热回收的高浓度气态CO 2 用于CO 2的制冷剂, / SB>液化循环,此外,通过利用废热冷却冷却的过冷超临界CO SB <2> SB可以实现功能的增加和效率的提高,并提供其设备。 解决方案:利用工厂废热作为制冷剂回收利用高浓度气体CO 2 ,过冷超临界CO 2 由压缩机12形成,气态CO 2 冷却器26,27,28,将过冷超临界CO SB <2>分离成液化CO 2 和气态CO 2 第一气液分离压力降低装置31,使气态CO 2 回流到压缩机12,从而形成CO 2 液化循环,从 液化的CO 2 气态CO 2 与通过第二气液分离减压装置33产生的干冰一起分离,气态CO 2 回流到CO 2 液化循环。 版权所有(C)2008,JPO&INPIT
    • 6. 发明专利
    • Co2 refrigeration cycle device and supercritical refrigeration operation method therefor
    • 二氧化碳制冷循环装置及其超临界制冷运行方法
    • JP2006292229A
    • 2006-10-26
    • JP2005111709
    • 2005-04-08
    • Mayekawa Mfg Co Ltd株式会社前川製作所
    • FUJIMA KATSUMIYOSHIKAWA TOMOIKUYOSHIDA TAKESHI
    • F25B1/047F25B1/00F25B43/00
    • F25B2309/061F25B2341/0662F25B2400/13F25B2400/23
    • PROBLEM TO BE SOLVED: To provide a refrigeration device having further improved refrigeration effect, and capable of accomplishing stable refrigeration operation, by adopting an economizer cycle for a supercritical refrigeration cycle using CO
      2 refrigerant having various advantages as a refrigerant, and to provide a supercritical refrigeration operation method therefor.
      SOLUTION: In this refrigeration device performing the supercritical refrigeration cycle, the CO
      2 refrigerant is cooled after compressing it to a supercritical area, the cooled CO
      2 refrigerant is performed with gas-liquid separation after decompressing it, the gasified CO
      2 refrigerant is introduced into a screw compressor 2, and only the low-temperature liquid refrigerant is evaporated by an evaporator 1. In the refrigeration device, the gas-liquid mixed refrigerant primarily decompressed by an expansion valve 4 is performed with the gas-liquid separation by a gas-liquid separator 5, a gas phase part g after the gas-liquid separation is introduced into an enclosing space S (a part of an intermediate pressure in a compression process) of the screw compressor 2, and a liquid phase part r after the gas-liquid separation is introduced into a capillary tube 6 for adiabatically expanding the liquid phase part r by a capillary, and thereafter is evaporated by the evaporator 1.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:为了提供一种具有进一步提高的制冷效果并且能够实现稳定制冷操作的制冷装置,通过采用具有各种各样的CO 2 SBB制冷剂的超临界制冷循环的节能循环 作为制冷剂的优点,并提供其超临界制冷操作方法。 解决方案:在执行超临界制冷循环的制冷装置中,将CO 2 制冷剂在压缩至超临界区后进行冷却,执行冷却的CO 2 制冷剂 在减压后进行气液分离,将气化的CO 2 制冷剂引入螺杆式压缩机2中,只有低温液体制冷剂被蒸发器1蒸发。在制冷装置中, 首先通过气液分离器5进行气液分离,首先通过膨胀阀4进行减压的气液混合制冷剂,将气液分离后的气相部g导入封闭空间S(一部分 螺杆压缩机2的压缩中间压力)和气液分离后的液相部分r被引入毛细管6中,用于通过毛细管使液相部分r绝热膨胀,然后被 eva 托运人1.版权所有(C)2007,JPO&INPIT
    • 10. 发明专利
    • Method for producing soybean product and system used therefor
    • 生产大豆产品的方法及其使用的系统
    • JP2003299452A
    • 2003-10-21
    • JP2002107779
    • 2002-04-10
    • Mayekawa Mfg Co Ltd株式会社前川製作所
    • OKAMOTO NAOHITOKITAMURA KAZUSHIGEUCHIYAMA SATOSHIYOSHIKAWA TOMOIKUJITOSHO NOBUYUKIMINEURA KIYOSHIKAWAMURA KUNIAKI
    • A23L11/00A23L1/20
    • PROBLEM TO BE SOLVED: To provide a soybean product having improved nutritive value by suppressing industrial wastes such as bean-curd refuse rejected in a production process of the soybean product. SOLUTION: The method for producing the soybean product is carried out as follows. Raw material soybeans are cooled to the glass transition temperature with a temperature regulating and a humidity regulating cabinet 11 and then pulverized with a cooling pulverizer 12 to provide powder. Water and other auxiliary materials are added to the resultant powder and mixed therewith in a mixer 13 to afford a mixture. The obtained mixture is heated with a heater and cooler 14 and then cooled and a coagulant is added to provide a coagulated material (a gel-like material). The coagulated material is further placed in a mold (filled and packaged in a container), then subjected to a heating and cooling treatment and completely coagulated to afford the soybean product. COPYRIGHT: (C)2004,JPO
    • 待解决的问题:通过抑制在大豆制品的生产过程中被拒绝的豆腐垃圾等工业废物来提供具有改善的营养价值的大豆制品。 解决方案:制备大豆产品的方法如下进行。 原料大豆用温度调节机构11冷却至玻璃化转变温度,然后用冷却粉碎机12粉碎以提供粉末。 将水和其它辅助材料加入到所得粉末中并在混合器13中混合以提供混合物。 将获得的混合物用加热器和冷却器14加热,然后冷却并加入凝结剂以提供凝结的材料(凝胶状材料)。 将凝固的材料进一步放置在模具中(填充并包装在容器中),然后进行加热和冷却处理并完全凝固,得到大豆产品。 版权所有(C)2004,JPO