A coupled gasification method of coal and gaseous hydrocarbons by adjusting the hydrogen-carbon ratio of synthesis gas
A technology of gaseous hydrocarbons and gas hydrogen, which is applied in the field of coal gasification, can solve the problems of high prices of natural gas, etc., and achieve the effects of simple method, reduced equipment investment, and reduced device operating costs
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Embodiment 1
[0033] The coupled gasification method in this embodiment is: feed coal, natural gas and oxygen together from the multi-channel gasification nozzles on the top of the gasifier, and carry out the gasification reaction at a temperature of 1150°C and a pressure of 3.0 MPa to obtain synthesis gas and molten hot slag; the multi-channel gasification nozzle on the top of the gasifier is provided with a gaseous hydrocarbon conversion channel, and the ratio of the furnace length to the furnace diameter of the gasifier is 3:1. Make a mass concentration of 60% coal-water slurry, the flow of coal-water slurry in the co-feeding process is 38007.58kg / h (equivalent to dry coal flow is 22804.55kg / h), the flow of natural gas is 19003.79Nm 3 / h, the oxygen flow rate used in the coal-water slurry gasification process is 16012.64Nm 3 / h, the flow rate of oxygen used in the natural gas gasification process is 14252.84Nm 3 / h, the amount of synthesis gas generated is 103657.31Nm 3 / h, the main co...
Embodiment 2
[0045] The coupled gasification method in this embodiment is: feed coal, natural gas and oxygen together from the multi-channel gasification nozzles on the top of the gasifier, and carry out the gasification reaction at a temperature of 1150°C and a pressure of 3.0 MPa to obtain synthesis gas and molten hot slag; the multi-channel gasification nozzle on the top of the gasifier is provided with a gaseous hydrocarbon conversion channel, and the ratio of the furnace length to the furnace diameter of the gasifier is 3:1. Make the coal-water slurry that mass concentration is 60%, the flow rate of coal-water slurry in the described co-feeding process is 38007.58kg / h (equivalent dry coal flow rate is 22804.55kg / h), the flow rate of natural gas is 12002.39Nm 3 / h, the oxygen flow rate used in the coal-water slurry gasification process is 16012.64Nm 3 / h, the oxygen flow rate for the natural gas gasification process is 7201.43Nm 3 / h, the amount of synthesis gas generated is 85167.06N...
Embodiment 3
[0051] The coupled gasification method in this embodiment is: feed coal, natural gas and oxygen together from the multi-channel gasification nozzles on the top of the gasifier, and carry out the gasification reaction at a temperature of 1150°C and a pressure of 3.0 MPa to obtain synthesis gas and molten hot slag; the multi-channel gasification nozzle on the top of the gasifier is provided with a gaseous hydrocarbon conversion channel, and the ratio of the furnace length to the furnace diameter of the gasifier is 3:1. Make a mass concentration of 60% coal-water slurry, the flow of coal-water slurry in the co-feeding process is 38007.58kg / h (equivalent to dry coal flow is 22804.55kg / h), the flow of natural gas is 9501.67Nm 3 / h, the oxygen flow rate used in the coal-water slurry gasification process is 16012.64Nm 3 / h, the oxygen flow rate for the natural gas gasification process is 5225.92Nm 3 / h, the amount of synthesis gas produced is 78565.16Nm 3 / h, the main components of...
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