A system and method for producing coal tar, coal gas and semi-coke by solid heat carrier activated gas flash pyrolysis coal
A solid heat carrier and coal tar technology, applied in the field of coal chemical industry, can solve the problems of investment, high energy consumption, low oil production rate, easy carbonization and deactivation of catalysts, etc.
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Embodiment 1
[0075] Embodiment 1: as figure 1 As shown, a solid heat carrier activated gas flash pyrolysis coal production system for coal tar, gas and semi-coke, including raw coal primary processing device, pyrolysis reaction separator, semi-coke heating separator, recycling device, Coal tar recovery device and semi-coke cooling device; part of the semi-coke powder from the pyrolysis reaction separator enters the semi-coke heating separator 10, and the pyrolysis reaction separator is used to pyrolyze dry coal to produce raw coal gas and medium-temperature semi-coke; semi-coke The heating separator is used to further heat and separate the medium-temperature semi-coke to produce high-temperature semi-coke and high-temperature flue gas; the high-temperature flue gas from the semi-coke heating separator 10 enters the recycling device, and the coal tar recovery device uses raw coal gas to produce coal tar and high-temperature flue gas. Coal gas; semi-coke cooling device uses medium-temperatur...
Embodiment 2
[0080] Embodiment 2: For energy saving and emission reduction, energy recycling. The recycling device of the present invention comprises a supplementary combustion chamber 11, a high-temperature gas heat exchanger 12 and a desulfurization and denitrification reactor 13, the outlet of the cyclone separator group is connected with the inlet of the supplementary combustion chamber 11, and the outlet of the supplementary combustion chamber 11 is exchanged with the high-temperature gas. The heat exchanger 12 is connected, and the outlet of the flue gas circulation fan 1, the gas outlet of the coal tar generating device, and the inlet of the pressurized air are also connected to the inlet of the high-temperature gas heat exchanger 12, and the inlet of the flue gas circulation fan 1 is connected to the cloth bag Another outlet of the dust collector 2; the outlet of the high-temperature gas heat exchanger 12 is connected with the inlet of the desulfurization and denitrification reactor...
Embodiment 3
[0081] Embodiment 3: In order to optimize the pyrolysis process, such as figure 2 As shown, the gas-solid separator in the pyrolysis reaction separator of the present invention includes a settling chamber housing 8-14, a pyrolysis fast splitter 8-4, a primary stripping device and a secondary stripping device, and the settling chamber housing 8 One end of -14 is located in the second flaring section, the other end of the shell 8-14 in the settling chamber is located in the third straight line section, the primary stripping device is located in the shell 8-14 of the inner settling chamber, and the secondary stripping device is located in the settling chamber shell 8-14. At the second straight section of chamber 8-13; the first-stage stripping device includes a first-stage conical drainage cone 8-5, a first-stage cone bucket 8-6, and a first-stage stripping gas ring pipe 8 placed in sequence from top to bottom -21, the large-diameter section of the first-stage cone bucket 8-6 is...
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