Household garbage coupling fluidized bed grading pyrolysis gasification technology
A technology for domestic waste and pyrolysis gasification is applied in the field of providing a coupled fluidized bed classification pyrolysis gasification process for domestic waste, which can solve the problems of difficult phenolic water, removal of tar, and difficulty in utilization and difficulty in utilization.
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Embodiment 1
[0014] Example 1, the domestic waste is first deironed and pulverized by the deironing pulverizer (10), and then the 0-6mm garbage particles are dried by the sleeve type drum dryer (11), and the generated water vapor containing peculiar smell is hot As a part of the gasification agent, hot garbage particles and a small amount of heat carrier are sent to the middle and lower part of the entrained bed reactor (13) coupled with the fluidized bed (1), mixed with gasification gas and circulating ash, and lifted upwards for hydrogen pyrolysis. Two-stage gas-solid separation, the high-temperature crude semi-coke separated by the first-stage gas-solid separator (5) returns to the turbulent fluidized bed (12) at the bottom of the coupled fluidized bed (1) through the feeder (6), and is mixed with air and Water vapor reacts at 800-1100°C to generate gasification gas, which flows upward together with circulating ash to form material circulation; the high-temperature fine semi-coke separat...
Embodiment 2
[0015] Example 2, the domestic garbage is first deironed and pulverized by the deironing pulverizer (10), and then the 0-6mm garbage particles are dried by the sleeve type drum dryer (11), and the generated water vapor containing peculiar smell is hot As a part of the gasification agent, hot garbage particles and a small amount of heat carrier are sent to the middle and lower part of the entrained bed reactor (13) coupled with the fluidized bed (1), mixed with gasification gas and circulating ash, and lifted upwards for hydrogen pyrolysis. Two-stage gas-solid separation, the high-temperature crude semi-coke separated by the first-stage gas-solid separator (5) returns to the turbulent fluidized bed (12) at the bottom of the coupled fluidized bed (1) through the return device (6), and is mixed with oxygen and Water vapor reacts at 800-1100°C to generate gasification gas, which flows upward together with circulating ash to form material circulation; the high-temperature fine semi-...
Embodiment 3
[0016] Embodiment 3, the air in embodiment 1 is changed into oxygen-enriched air, other is identical.
[0017] The domestic waste coupling fluidized bed staged pyrolysis gasification process provided by the present invention not only rationally utilizes heat energy, eliminates tar in the gasification process, solves the problem of fly ash in fluidized bed gasification, and eliminates dioxin and Odor, high methane gas content, at the same time, the gas does not contain tar, does not produce phenol water; low oxygen consumption, high gasification efficiency, high gasification intensity, small equipment volume, low steel consumption, greatly reduced fixed investment, and exhaust emissions Ash process is simple.
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