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    • 1. 发明专利
    • Electrolytic method
    • 电解法
    • JP2008063613A
    • 2008-03-21
    • JP2006241731
    • 2006-09-06
    • Chlorine Eng Corp Ltdクロリンエンジニアズ株式会社
    • SHINOMIYA YOSHITSUGUTOKUMORI TSUNEO
    • C25B11/03B01J35/02C25B1/00
    • PROBLEM TO BE SOLVED: To stably continue the electrolysis of an electrolyte containing impurities using an electrode having high strength and high toughness. SOLUTION: A three-dimensional electrode 15 fabricated by bending a plurality of snicks 12 which are formed in a plate-like metal electrode substrate 11 toward the same direction to form an elastic conductive body 13 is used for the electrolysis of the electrolyte containing the impurities such as the electrolysis of white liquor. The three-dimensional electrode with higher strength and higher toughness is provided only by bending the plurality of the formed snicks. When the three-dimensional electrode is used in an ion exchange membrane electrolytic cell, the positional relation among mutual members is made stable, thus polysulfide ion or the like can be produced at high efficiency without mechanically damaging an ion exchange membrane or the like and without excessively deforming the same nor making power supply insufficient. Since the electrode has a wide surface area, the impurities deposited per unit surface area is made small to continue the electrolysis over a long period. COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:使用高强度和高韧性的电极来稳定地继续电解含有杂质的电解质。 解决方案:通过将形成在板状金属电极基板11中的多个小鸭12朝向相同方向弯曲形成弹性导电体13而制造的三维电极15用于电解电解质 含有诸如电解白液的杂质。 仅通过弯曲多个形成的小鸡来提供具有较高强度和较高韧性的三维电极。 当在离子交换膜电解槽中使用三维电极时,相互构件之间的位置关系变得稳定,因此可以高效率地生产多硫化物离子等,而不会机械损伤离子交换膜等, 过度变形,也不会使电力供应不足。 由于电极具有宽的表面积,所以每单位表面积沉积的杂质被制成较小的长时间继续电解。 版权所有(C)2008,JPO&INPIT
    • 4. 发明专利
    • FRACTIONATION METHOD OF ORGANIC SUBSTANCE BY MOLECULAR WEIGHT
    • JPH08243305A
    • 1996-09-24
    • JP4859695
    • 1995-03-08
    • CHLORINE ENG CORP LTD
    • TOKUMORI TSUNEO
    • B01D11/04
    • PURPOSE: To produce the rectification effect by differential temperature to perform effective fractionation by continuously feeding carbon dioxide in a supercritical or a subcritical state of lower temperature than that of an extraction tank from below the extraction tank held at fixed temperature to perform extraction. CONSTITUTION: An extraction tank 1 filled with an organic substance is heated by a heater 8, and carbon dioxide in a supercritical or a subcritical state heated by a heat exchanger 9 to a temperature lower than that of the extraction tank 1 is fed from below the extraction tank 1. By forming the temperature gradient in the extraction tank 1, the rectification effect is produced to economically take out the components of different molecular weight distribution from the tank 1. Thus by the extraction tank 1 of simple structure, fractionation of high rectification effect is performed. In this way, from a mixture of components of different molecular weight such as that of silicone oil, perfluoropolyether, lower alcohol ester of fatty acid, the components of different molecular weight are effectively fractionated.
    • 6. 发明专利
    • METHOD FOR EXTRACTING AND SEPARATING COLORING MATTER FROM KRILL
    • JPH0457853A
    • 1992-02-25
    • JP17054990
    • 1990-06-28
    • CHLORINE ENG CORP LTDITANO REITOU KK
    • TOKUMORI TSUNEOSUMIDA YOKOTSUYAMA KOICHIKUNISHIRO IYOKOOKADA HARUOTANI TOSHIFUMI
    • C09B61/00
    • PURPOSE:To prepare a reddish orange coloring matter having a high safety in a high concn. by extracting, with CO2 in a supercritical state, krill shells of which the protein has been decomposed by a protease. CONSTITUTION:Krill shells are treated with a protease to decompose the protein in the shells and the treatment product is filtered. The residue of filtration is dried to give treated shells having a water content of 6-8% and a mean particle size of 200 mum or lower. The treated shells are put into an extraction vessel 5. An extractant comprising a liq. CO2 in an amt. of 30-40 pts.wt. based on one pt.wt. treated shells having a coloring matter concn. of 30 mg/100 g is supplied through a supercooling apparatus 2 to a pump 3, pressurized at the pump 3 to 100-250 kg/cm , heated with a heat exchanger 4 to 35-40 deg.C to bring it into a supercritical state, and transferred to the extraction vessel 5 to extract an oil in the treated shells. After the pressure of the oil-contg. CO2 in the supercritical state is reduced to 40-60 kg/cm with a pressure reducing valve 6, the CO2 is delivered through a selector valve 11 to the first separating vessel 7 to separate the oil, and recycled through a selector valve 13, a pressure reducing valve 9, a condense 10, a water separator 15, and a storage vessel 1 to the extraction vessel 5. Then, selector valves 11 and 13 are closed while selector valves 12 and 14 are opened, and the CO2 contg. the coloring matter is transferred to the second separating vessel 8, where the CO2 is evaporated to give a coloring matter with a concn. of 2000-10000 mg/100g.