A device and process for producing hydrogen-rich synthesis gas by thermal conversion of waste plastics
A technology of waste plastics and synthesis gas, which is applied in the manufacture of combustible gases, the petroleum industry, special forms of dry distillation, etc., can solve the problems of human hazards, secondary pollution, and low utilization rate of waste plastics, and achieve accelerated pyrolysis conversion rate and improved The effect of product quality and energy utilization optimization
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Embodiment 1
[0050] Feed waste plastics into the device at a feed rate of 10kg / h, and control the temperature inside the horizontal tubular pyrolysis furnace 4 to 500°C under the action of water vapor and external heating for pyrolysis, and the pyrolysis part of the horizontal tubular pyrolysis furnace 4 The molar ratio of water vapor to carbon in waste plastics is H 2 O:C=1:1, the molar ratio H of the water vapor in the gasification part gasification furnace 14 to the carbon in the waste plastics 2 O:C=3:1, the molar ratio of calcium in the calcium oxide particles in the gasification furnace 14 to carbon in the waste plastics Ca:C=1.2:1, the gasification temperature is controlled at 600°C, and the particle size of the calcium oxide particles is 0.40 mm, the molar number of carbon and oxygen in the air in the pyrolysis solid residue entering the melting part C:O=1:1, the temperature in the molten pool is controlled at 1500°C, the system operates continuously for 1 hour, and the gas composi...
Embodiment 2
[0052] Feed waste plastics into the device at a feed rate of 20kg / h, and control the temperature of the pyrolysis furnace to 400°C under the action of water vapor and external heating for pyrolysis. The molar ratio of carbon in the plastic is H 2 O:C=1:2, the molar ratio H of water vapor in the gasification partial gasification furnace 14 and carbon in waste plastics 2 O:C=5:1, the amount of calcium oxide sprayed is based on the molar ratio of calcium to carbon in waste plastics Ca:C is 1.5:1, the gasification temperature is controlled at 550°C, and the particle size of calcium oxide particles is 0.50mm. The molar number of carbon and oxygen in the air in the pyrolysis solid residue entering the melting part is C:O=1:1, the temperature in the molten pool is controlled at 1400°C, the system is continuously operated for 1 hour, and the gas composition of the product is analyzed by GC. The result is as image 3 As shown, the calculated average volume concentration of the produc...
Embodiment 3
[0054] Feed waste plastics into the device at a feed rate of 30kg / h, and control the temperature inside the horizontal tubular pyrolysis furnace 4 to 550°C under the action of water vapor and external heating for pyrolysis, and the pyrolysis part of the horizontal tubular pyrolysis furnace 4 The molar ratio of water vapor to carbon in waste plastics is H 2 O:C=1:1.5, the molar ratio H of the water vapor in the gasification part gasification furnace 14 to the carbon in the waste plastics 2 O:C=3:1, the amount of calcium oxide sprayed is based on the molar ratio of calcium to carbon in waste plastics Ca:C is 1.2:1, the gasification temperature is controlled at 600°C, and the particle size of calcium oxide particles is 0.50mm. The molar number of carbon and oxygen in the air in the pyrolysis solid residue entering the melting part is C:O=1:1, the temperature in the molten pool is controlled at 1600°C, the system operates continuously for 1 hour, and the gas composition of the pro...
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