System and method for preparing methane from coal under condition of supercritical water
A supercritical water and supercritical technology, applied in the direction of bulk chemical production, petroleum industry, gas fuel, etc., to achieve the effect of large social benefits
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Embodiment 1
[0032] like figure 1 As shown, a coal-to-methane system under supercritical water conditions includes a high-pressure plunger pump 1, a delivery pipeline 8, a supercritical reactor 3, a condenser 4 and a gas-liquid separator 5, a high-pressure plunger pump 1, a supercritical The reactor 3 , the condenser 4 and the gas-liquid separator 5 are connected in sequence through a delivery pipeline 8 . A heater 9 is housed in the supercritical reactor 3 . A heat exchanger 2 is also provided on the delivery pipeline between the high-pressure plunger pump 1 , the supercritical reactor 3 and the condenser 4 . The output port of the high-pressure plunger pump 1 is connected to the first heat exchange channel of the heat exchanger 2, and the coal-water slurry output by the high-pressure plunger pump 1 is input into the heat exchanger 2 as a cold medium, and the coal-water slurry after heat exchange is input into the supercritical reaction device 3; the output port at the top of the superc...
Embodiment 2
[0035] A method for producing methane from coal-water slurry under supercritical conditions, comprising the following steps:
[0036] (1) The coal-water slurry A of a certain flow is pressurized by the coal-water slurry plunger pump 1, and enters the reactor 3 after passing through the heat exchanger 2;
[0037] (2) close the reactor outlet valve, after there is a certain amount of coal-water slurry in the kettle reactor 3, close the plunger pump of the coal-water slurry, and statically heat the coal-water slurry with a heater;
[0038] (3) When the pressure in the reactor 3 reaches 30 MPa and the temperature reaches 395° C., open the reactor outlet valve;
[0039] (4) Start the coal-water slurry plunger pump 1, pressurize the coal-water slurry A from the storage tank to 30MPa, continuously inject it into the reactor 3, and adjust the flow rate of the coal-water slurry plunger pump 1 to slowly rise to the rated value flow;
[0040] (5) The coal-water slurry enters the reacto...
Embodiment 3
[0044] like figure 1 As shown, this example is basically the same as Example 2. The coal-water slurry A is prepared from bituminous coal with a carbon content of 85% through fine washing, pressurized by the plunger pump 1 of the coal-water slurry, and after heat exchange by the heat exchanger 2 Enter the tubular supercritical reactor 3. In the reactor 3, it is heated by its own heater and reacts. The gas-vapor mixture coming out of the top of the reactor 3 is condensed by the condenser 4 after exchanging heat in the heat exchanger 2, and enters the gas-liquid separator 5 for gas-liquid separation. Separation affords gas product and water, respectively. The bottom of the reactor 3 is equipped with an inorganic salt separation system, and the valves V1 and V2 are intermittently opened at regular intervals to discharge inorganic salts and avoid damage to the equipment.
[0045] A method for producing methane from coal-water slurry under supercritical conditions, comprising the ...
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