A post treatment process containing a fast gas-solid separation structure after plasma coal cracking
A technology of plasma and coal cracking, which is applied in the post-processing field of plasma coal cracking process, can solve the problems of reducing cooling efficiency and consuming cooling water, and achieve the effect of improving cooling efficiency, improving comprehensive value, and increasing product added value
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Embodiment 1
[0024] The plasma torch uses hydrogen as the working gas, the input power is 3.8-4.2MW, the hydrogen flow rate is 100-110kg / h, the average temperature of the hydrogen plasma exceeds 3000K, and the temperature in the central area is 5000-6000K. The pyrolysis product temperature is 1200~1500K, the speed is 150~200m / s, and the pyrolysis product enters the rapid separation device (the gas-solid separation device disclosed in the prior art patent CN1267564), the gas residence time is 80ms, and the solid phase residence time is the separation efficiency 75%. The gas separated from the gas outlet, that is, the gas phase intermediate product, enters the quenching device, is rapidly cooled with circulating water, and is lowered to room temperature (thereby terminating the thermal decomposition of the product, increasing the content of acetylene in the cracked gas, and avoiding the decomposition reaction of acetylene at high temperature), to obtain the volume content 10% acetylene gas m...
Embodiment 2
[0026] The plasma torch uses hydrogen as the working gas, the input power is 3.8-4.2MW, the hydrogen flow rate is 100-110kg / h, the average temperature of the hydrogen plasma exceeds 3000K, and the temperature in the central area is 5000-6000K. The pyrolysis product temperature is 1200~1500K, the speed is 150~200m / s, and the pyrolysis product enters the rapid separation device (the gas-solid separation device disclosed in the prior art patent CN1267564), the gas residence time is 80ms, and the solid phase residence time is the separation efficiency 75%. The gas separated from the gas outlet, that is, the gas phase intermediate product, enters the quenching device, is rapidly cooled with circulating water, and is lowered to room temperature (thereby terminating the thermal decomposition of the product, increasing the content of acetylene in the cracked gas, and avoiding the decomposition reaction of acetylene at high temperature), to obtain the volume content 10% acetylene gas m...
Embodiment 3
[0028] The plasma torch uses hydrogen as the working gas, the input power is 3.8-4.2MW, the hydrogen flow rate is 100-110kg / h, the average temperature of the hydrogen plasma exceeds 3000K, and the temperature in the central area is 5000-6000K. The pyrolysis product temperature is 1200~1500K, the speed is 150~200m / s, and the pyrolysis product enters the rapid separation device (the gas-solid separation device disclosed in the prior art patent CN1267564), the gas residence time is 80ms, and the solid phase residence time is the separation efficiency 75%. The gas separated from the gas outlet, that is, the gas phase intermediate product, enters the quenching device, is rapidly cooled with propane, and is lowered to room temperature (thereby terminating the thermal decomposition of the product, increasing the content of acetylene in the cracked gas, and avoiding the decomposition reaction of acetylene at high temperature), and obtaining the volume content of acetylene 6% and 9% et...
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