RECHANGEABLE BATTERY
    23.
    发明专利

    公开(公告)号:JPS60182670A

    公开(公告)日:1985-09-18

    申请号:JP3816384

    申请日:1984-02-28

    Abstract: PURPOSE:To obtain a high performance secondary battery having high discharge voltage by using electrolyte comprising organic solvent and solute and using specific carbon material having different property in a positive electrode and a negative electrode. CONSTITUTION:Activated carbon or activated carbon fiber is used in a positive electrode 2 and graphite or graphitized carbon fiber is used in a negative electrode 1, and electrolyte comprising organic solvent and solute is used. As the activated carbon material, for example, coconut shell activated carbon having a surface area of 500-1,000m /g or activated carbon fiber having a surface area of 300-3,000m /g is used. As graphite material for the negative electrode, highly graphitized material such as graphite powder or graphitized carbon fiber is preferable, especially cloth or felt having large surface area comprising highly graphitized carbon fiber is preferable in terms of electrode production. As solute of the electrolyte, LiCIO4, LiBF4, LiPF6 , LiAsF6 having Li is preferable.

    RECHARGEABLE BATTERY
    24.
    发明专利

    公开(公告)号:JPS6054181A

    公开(公告)日:1985-03-28

    申请号:JP16233183

    申请日:1983-09-02

    Abstract: PURPOSE:To provide a light weight and high power battery having good charge- discharge performance by using an electroconductive high polymer doped with cations as a positive electrode, carbon fibers doped with cations as a negative electrode, and electrolyte containing the above anions and cations. CONSTITUTION:A high polymer such as polyacetylene or polyparaphenylene is made electroconductive by electrochemically doping anions and used as a positive electrode 1. Carbon fibers electrochemically doped with cations is used as a negative electrode 3. A solution containing anions same as those doped in the positive electrode 1 and cations same as those doped in the negative electrode 2, and having suitable conductivity when those ions are dissolved, and having high decomposition voltage so that it does not decompose at a maximum voltage in charging is used as electrolyte.

    PRODUCTION OF HIGHLY CONDUCTIVE POLYACETYLENE FILM

    公开(公告)号:JPS57164109A

    公开(公告)日:1982-10-08

    申请号:JP4936381

    申请日:1981-04-03

    Abstract: PURPOSE:To produce the titled film having high electric conductivity, by coating the surface of a solid with a catalyst solution containing an electron-accepting compound or an electron-donating compound and bringing the surface into contact with acetylene gas. CONSTITUTION:A solution of a Ziegler catalyst-type coordinated anionic polymerization catalyst (e.g., titanium tetrabutoxidetriethylaluminum system) containing an electron-accepting compound (e.g., tetracyano-p-quinodimethane) or an electron-donating compound (e.g., tetrathiafulvalene) is applied to the surface of the wall of a polymerization vessel or to a solid not reactive with the catalyst (e.g., glass) and then acetone, O2 and acetylene gas purified to

    HIGH DENSITY ACETYLENE POLYMER FILM

    公开(公告)号:JPS5682822A

    公开(公告)日:1981-07-06

    申请号:JP16037779

    申请日:1979-12-12

    Abstract: PURPOSE:To titled film especially suitable for an organic semiconductor material having a low void, low electrical resistance, and high mechanical strength, having a specific bulk density. CONSTITUTION:A solution of a Ziegler catalyst for anionic polymerization of coordination, comprising mainly a combination of a transition metal compound preferably that of Ti, Pd, etc. and an organometallic compound of a metal of the I-III groups of the periodic table, to be dissolved in an organic solvent. e.g., toluene, etc. uniformly, for example, is applied to the wall of a polymirizer, the surface of a solid which do not react with the catalyst, to form a liquid film of the catalyst solution. Acetylene is introduced to form an acetylene polymer film on the surface of the catalyst solution. To increase the bulk density of the film, a new catalyst solution is applied to the surface of the acetylene polymer again and the same operation is repeated, to give the desired film having a bulk density not less than 0.65.

    METHOD OF RECOVERING THERMAL ENERGY

    公开(公告)号:JPS5670832A

    公开(公告)日:1981-06-13

    申请号:JP14541379

    申请日:1979-11-12

    Abstract: PURPOSE:To enable an efficent thermal-energy recovery using an absorption-type heat pipe by a method wherein an organic compd. and an amine compd. are combined as the component of working fluid. CONSTITUTION:An absorbent (an organic compd. and an amine compd., wherein the one with higher b.p. constitutes the major component) is guided into the heat recoverer 1 through the pipe 7. The absorbent absorbs the vapor of component to be absorbed (an organic compd. and amine compd., wherein the one with lower b.p. is the major component) which is guided into the heat recoverer 1 through gas pipe 11. The absorbent generates heat, raising its temperature and recovers thermal energy QH. The absorbent solution passing through the heat-exchanger 5, is reduced in pressure by a valve 6, and sent to the regenerator 2. Thermal energy Q1 being given in the regenerator 2, the absorbent solution discharges the absorbed vapor and the vapor is liquefied by being cooled in the condenser 3. The liquid is sent to the temporary generator 4 pressurized by a pump 10, where the liquid is given heat energy Q2 and vaporized, which enters the heat recoverer 1.

    ABSORPTIONNTYPE HEAT PUMP
    28.
    发明专利

    公开(公告)号:JPS5670081A

    公开(公告)日:1981-06-11

    申请号:JP14541279

    申请日:1979-11-12

    Abstract: PURPOSE:The titled heat pump, capable of giving thermal energy of high temperature without the danger of solid deposition and with a slight corrosion, and prepared by using an alcohol compound as an absorbent and an amine compound as an agent to be absorbed. CONSTITUTION:An absorption type heat pump prepared by using an alcohol compound, preferably 1,4-butanediol, ethylene glycol or glycerol, as an absorbent and an amine compound, e.g. n-propylamine or isobutylamine, as an agent to be absorbed. On the other hand, if an amine compound is used as the absorbent, heptylamine or diethylenetriamine is preferred, and methanol or n-propanol is used as an alcohol compound which is the agent to be absorbed. EFFECT:Usable as a thermal energy storage material which is capable of separating the agent to be absorbed by giving thermal energy to the absorbent which absorbed the agent and taking out the thermal energy by absorbing the agent to be absorbed in the absorbent.

    MANUFACTURE OF SILICON NITRIDE POWDER

    公开(公告)号:JPS5617910A

    公开(公告)日:1981-02-20

    申请号:JP9262979

    申请日:1979-07-23

    Abstract: PURPOSE:To obtain silicon nitride powder having superior characteristics by dispersing finely divided silica powder in a polyacrylonitrile type polymer followed by heat treatment in an atmosphere contg. nitrogen or ammonia. CONSTITUTION:A polyacrylonitrile type polymer contg. finely divided silica powder dispersed is heat treated in an atmosphere contg. nitrogen and/or ammonia optionally after heat treatment in an oxidizing atmosphere. The silica used is preferably amorphous and has high purity and

    METHOD OF TREATING COKEEOVEN GAS DESULFURIZATION WASTE LIQUID

    公开(公告)号:JPS55106591A

    公开(公告)日:1980-08-15

    申请号:JP1436179

    申请日:1979-02-13

    Abstract: PURPOSE:To recover high-purity ammonium sulfate and decrease COD and NH4-H in drained water, by adding Cu (compound) and ammonia water to a coke-oven gas desulfurization waste liquid so that the copper concentration becomes a prescribed value and by causing wet oxidation under a limited condition and concentrating a reaction liquid separated from a gas. CONSTITUTION:Cu (compound) 4 and NH35 are added to a coke-oven gas desulfurization waste liquid 1 and diluting water 2 in a storage vessel 3 so that the copper concentration of the waste liquid becomes 0.1-50ppm. The pressure of the waste liquid is raised by a boosting pump 6. After a gas 8 containing O2 is compressed at 7 and introduced into the waste liquid, the liquid is conducted to a wet oxidation column 9. Wet oxidation is caused by the O2-containing gas at a temperature of 150 deg.C or more while a portion of water is kept liquid. The waste liquid is separated from a gas at 10. The exhaust gas is washed at 11 and then released at 12. The separated solution is introduced into a crystallization vessel 13 and heated to remove moisture 14. The concentrated liquid is conducted to a separator 15 so that drained water 18 is separated. Ammonium sulfate separated from the liquid is dried at 16 at that high-purity ammonium sulfate 17 is recovered.

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