METHOD AND SYSTEM FOR SUPERCRITICAL UNDERWATER COMBUSTION TYPE POWER GENERATION

    公开(公告)号:JP2000274214A

    公开(公告)日:2000-10-03

    申请号:JP8026699

    申请日:1999-03-24

    Abstract: PROBLEM TO BE SOLVED: To enable utilization of the original material such as low quality charcoal, heavy oil, and biomass as a fuel by continuously supplying the fluid fuel including the organic material and the alkali solution to a heat exchanger integrated burner, and burning the organic material underwater at a temperature and a pressure near supercritical state. SOLUTION: Organic material 1 is mixed with water by a slurry adjusting unit 2 so as to adjust the fuel slurry as a fluid fuel. The slurry and the alkali solution 3 are pressurized by each pump 4, 5 so as to be passed through a waste heat recording heat-exchanger 6. Heat from the mixture fluid is exchanged by the heat of the fluid flowed out of a heat exchanger integrated burner 7, and temperature of the mixture fluid becomes 400-700 deg.C. The heated mixture fluid is supplied to a heat exchanger integrated burner 7, and the air 8 as the oxidant gas is compressed by a compressor 9, and passed through the heat exchanger 6 for heating, and the compressed and heated air is supplied to the burner 7. The organic material included in the mixture fluid is burned with the oxygen included in the air, and steam is generated by the combustion heat of the heat exchanger integrated burner 7, and electrical energy is extracted by a power generator 11.

    VISCOSITY-COEFFICIENT MEASURING APPARATUS

    公开(公告)号:JPH02291942A

    公开(公告)日:1990-12-03

    申请号:JP11270589

    申请日:1989-05-01

    Abstract: PURPOSE:To make it possible to measure the coefficient of viscosity simply and accurately by constituting an apparatus with a vibrator, a circuit for grounding a housing, a variable capacitor, dielectric-loss measuring device, and a balance detector. CONSTITUTION:A torsional vibrator 1 is held in a sample fluid cell 3 with housings 2. The inside of the cell 3 is filled with a fluid to be measured. Electrodes which are provided on the surfaces of the vibrator 1 are connected to the measuring bridge terminals of a dielectric-loss measuring device 4 through conductor wires 5. A synthesizer 6 which imparts a frequency input and a bal ance detector 7 which detects the balance of the bridge are connected to the corresponding terminals of the measuring device 4. The housing 2 is grounded to the grounding terminal of the bridge through a conductor wire 8. Thus the effect of the housing 2 in measurement is removed. A zero-position moving variable capacitor 9 which is connected to the vibrator 1 in parallel is prepared. The capacitance of the capacitor 9 is selected in measuring the width of a half value. Therefore, the zero position of the capacitance of the dielectric-loss measuring device corresponding to the capacitance of the capacitor 9 can be arbitrarily selected.

    APPARATUS FOR PORTIONWISE SAMPLING FRACTIONATED COMPONENT IN FLUID FROM SUPERCRITICAL FLUID CHROMATOGRAPHY

    公开(公告)号:JPS63200059A

    公开(公告)日:1988-08-18

    申请号:JP3370987

    申请日:1987-02-17

    Abstract: PURPOSE:To portionwise sample a fractionated component at high purity efficiently and continuously without using an adsorbing column and without receiving the restriction of the number of times of fractionation, by providing a change-over valve between a separation column and a low pressure side and portionwise sampling the fractionated component by the operation of the change-over valve. CONSTITUTION:The first flow channel consisting of lines 9, 10 connects a change-over valve 2 and a separation column 1 and the second flow channel composed of a line 12 connects the change-over valve 2 and the separation column 1 through a minute flow rate control valve 7. The third flow channel consisting of lines 14, 15, 24 connects the change-over valve 2 and a low pressure region through a back pressure control valve 8, and the fourth flow channel consisting of lines 16-18, 20-22, 23 connects the change-over valve 2 and the low pressure region through a portionwise sampling change-over valve 3 and portionwise sampling containers a-c. When a supercritical fluid having a mixture to be separated dissolved therein is introduced into the separation column 1, the supercritical fluid wherein the mixture is fractionated into respective components is allowed to flow out from the separation column 1 in a time series manner. Hereupon, the change-over valves 2, 3 are operated in relation to a fractionated component detector 6 and the connection state of each flow channel is altered and each of the fractionated components is portionwise sampled in each of the portionwise sampling containers a-c.

    METHOD FOR DECOMPOSING DIOXINS WITH SUPERCRITICAL WATER

    公开(公告)号:JPH09327678A

    公开(公告)日:1997-12-22

    申请号:JP14694096

    申请日:1996-06-10

    Abstract: PROBLEM TO BE SOLVED: To make dioxins harmless by an industrially advantageous method wherein inorg. powder contg. dioxins is dispersed into supercritical water held at least at the critical temp. and at least under the critical pressure and dioxins are decomposed under this condition. SOLUTION: Inorg. powder contg. dioxins, water and open air are filled in a reactor and it is heated at 653-873K being at least critical temp. of water, pref. 653-773K. In this case, the reaction pressure is controlled by wt. of water filled in the reactor and 22-40MPa, pref. 25-35MPa is pref. After a specified reaction time passes, in the case where an oxidizing agent is not incorporated, at least 96.5% dioxins in the reactor are decomposed and in the case where such an oxidizing agent as hydrogen peroxide and oxygen gas is incorporated, at least 98.5% dioxins are decomposed. Thereby, dioxins can be made harmless by an industrially advantageous method without necessitating high reaction temp. and complicated reaction control.

    METHOD OF DECOMPOSING FLUOROCARBON

    公开(公告)号:JPH02274269A

    公开(公告)日:1990-11-08

    申请号:JP9612089

    申请日:1989-04-14

    Abstract: PURPOSE:To easily constitute a process of rendering fluorocarbon or fluorocarbon-containing materials harmless and prevent emission of harmful materials out of a system by decomposing the fluorocarbon or fluorocarbon- containing materials inside a high temperature - high pressurized water in a temperature and a pressure (supercritical) condition exceeding the critical temperature and critical pressure. CONSTITUTION:A high temperature - high pressurized water is fed to a reactor together with a fluorocarbon or fluorocarbon-containing material. As the conditions of that time, a temperature exceeding the critical temperature of water, for example, 380 deg.C or more, and a pressure over the critical pressure of water, for example, 300atm or more, are preferred. The feed quantity of fluorocarbon is preferably less than 1/100 by mole ratio to water. When the fluorocarbon is chlorofluoromethane containing no hydrogen, the greater part is hydrolyzed in this reactor, forming carbon dioxide water, and hydrogen halide. The hydrogen halide in the product is neutralized by alkali and made harmless.

    PRODUCTION AND CONCENTRATION OF FURFURAL

    公开(公告)号:JPH02108682A

    公开(公告)日:1990-04-20

    申请号:JP25990388

    申请日:1988-10-14

    Abstract: PURPOSE:To efficiently obtain highly concentrated furfural by extracting aqueous solution, etc., containing pentose such as xylose by using acid as catalyst and using supercritical fluid. CONSTITUTION:In a process producing furfural from aqueous solution containing pentose such as xylose or hemicellulose in plant body using acid as catalyst, a fluid having temperature and pressure exceeding critical temperature and critical pressure is made into contact with reacting liquid in reacting vessel and circulated, then furfural is extracted and recovered to outside of the reaction system. Preferably, the supercritical fluid containing furfural is circulated through a filling column having structure refluxing a part of concentrated liquid and the other concentrating column, thus concentration of furfural is enriched.

    METHOD FOR DETOXICATE POLYCHLORINATED BIPHENYL BY SUPERCRITICAL WATER

    公开(公告)号:JPH10225632A

    公开(公告)日:1998-08-25

    申请号:JP11596697

    申请日:1997-05-07

    Abstract: PROBLEM TO BE SOLVED: To detoxicate polychlorinated biphenyl by decomposing it with supercritical water alone, supercritical water admixed with alkali or supercritical water admixed with alkali and an oxidizing agent. SOLUTION: About 50-150 weight units of water, based on one weight unit of PCB, 50-150 weight units of water and 1-5 weight units of such an alkali as sodium hydroxide or 50-150 weight units of water, 2-20 weight units of an oxidizing agent such as hydrogen peroxide and 1-5 weight units of an alkali such as sodium hydroxide are filled in a reactor and heated above the critical temp. of water in a heating furnace. The reaction pressure is adjusted in accordance with the weight of water filled in the reactor, and the reaction time is controlled to 5-60min. Oxygen, air, etc., are used as the oxidizing agent as well as hydrogen peroxide. Sodium carbonate is used as the alkali besides sodium hydroxide. Consequently, the high reaction temp. and long reaction time are not needed to make polychlorinated biphenyl harmless without causing the resynthesis of PCB.

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