Hydrogasification semi-coke pulping method
A technology for hydrogenation, gasification and semi-coke, which is applied in the field of coal chemical industry, can solve the problems of blockage and damage of filter 28 and induced draft fan 27, reduce the gasification efficiency of coal-water slurry, affect the gasification process of coal-water slurry, etc. The effect of pulping, improving the utilization rate of semi-coke, and ensuring continuous and stable operation
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Embodiment 1
[0020]Such asFigure 2-3 As shown, the hydrogenated semi-coke pulping device includes a pulping stirring tank 1, a Venturi mixer 2 is provided at the inlet of the pulping stirring tank 1, and a pulping agitator is provided in the pulping stirring tank 1 3. The top of the rotating shaft of the pulping agitator 3 passes through the top of the pulping agitating tank 1 and is fixedly connected with the output shaft of the pulping rotating motor 4. The top of the pulping agitating tank 1 is provided with a semi-coke treatment chamber 5, a semi-coke treatment chamber The interior of 5 is connected with the interior of the pulping mixing tank 1, the bottom of the semi-coke processing chamber 5 is connected to the top of the pulping mixing tank 1, and the top of the semi-coke processing chamber 5 is provided with an emptying pipe 6; in the semi-coke processing chamber 5 At least two arcuate trays 7 are staggered. In this embodiment, the number of trays 7 is 4, and the trays 7 are arranged ho...
Embodiment 2
[0023]The method for preparing hydrogenated semi-coke pulp by using embodiment 1 includes a start-up phase and a stable operation phase, in which:
[0024]1) Start-up stage: Add 60% of the volume of industrial fresh water into the pulp mixing tank 1, and the semi-coke is pneumatically transported to the Venturi mixer 2 to mix with the industrial fresh water transported to the Venturi mixer 2. The pressure of pneumatic conveying is 0.5MPa, the operating pressure of slurry mixing tank 1 is 0.1MPa, and the mass ratio of the semi-coke conveyed by pneumatic to the industrial fresh water introduced into the Venturi mixer 2 is 5:5, and the pre-pulping is obtained ; The pre-made slurry enters the slurry mixing tank 1 for stirring, and the stirring speed is 30r / min; during the mixing process, the industrial fresh water is introduced into the semi-coke processing chamber 5, and the semi-coke and the semi-coke are pneumatically conveyed The mass ratio of the industrial fresh water in the coke tre...
Embodiment 3
[0033]The method for preparing hydrogenated semi-coke pulp by using embodiment 1 includes a start-up phase and a stable operation phase, in which:
[0034]1) Start-up stage: Add 70% of the volume of industrial fresh water into the pulp mixing tank 1, and the semi-coke is pneumatically transported to the Venturi mixer 2 to mix with the industrial fresh water transported to the Venturi mixer 2. The pressure of pneumatic conveying is 0.6MPa, the operating pressure of slurry mixing tank 1 is 0.15MPa, the mass ratio of the semi-coke conveyed by pneumatic to the industrial fresh water introduced into the Venturi mixer 2 is 7:5, and the pre-pulping is obtained ; The pre-made pulp enters the pulp mixing tank 1 for stirring, and the stirring speed is 40r / min; during the stirring process, the industrial fresh water is introduced into the semi-coke treatment chamber 5, and the semi-coke and the semi-coke conveyed by pneumatic conveying The mass ratio of the industrial fresh water in the coke trea...
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