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    • 3. 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.
    • 5. 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.