Oil shale semicoke fluidized combustion circulation gas heating technology

A technology for oil shale semi-coke and circulating gas, which is applied in the petroleum industry, direct heating dry distillation, coke oven and other directions to achieve the effect of solving environmental problems

Active Publication Date: 2015-04-01
NORTHEAST DIANLI UNIVERSITY +1
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  • Claims
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Problems solved by technology

[0008] The purpose of the present invention is to substantially improve the existing process route of heating and circulating gas with gas combustion, and to combine the oil shale semi-coke fluidized bed combustion with the membrane wall heat exchanger in the furnace and the tail tube heat exchanger The oil shale semi-coke fluidized combu

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  • Oil shale semicoke fluidized combustion circulation gas heating technology

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[0020] Hereinafter, the present invention will be further explained with the drawings and embodiments.

[0021] Reference figure 1 In the oil shale semi-coke fluidized combustion cycle gas heating process of the present invention, the oil shale semi-coke >0~15mm is fed from the feed port 3 into the fluidized bed furnace 1, and the remaining gas is fed from the remaining gas burner 4 Fluidized bed furnace 1, semi-coke and residual gas enter the fluidized bed furnace 1 and burn at low temperature at 850~950℃; part of the heat released by the combustion of semi-coke and residual gas in the fluidized bed furnace 1 heats the membrane walls around the furnace Part of the circulating gas flowing in the heat exchanger 2 flows through the high-temperature air preheating tube heat exchanger 19, the high-temperature gas heating tube heat exchanger 17, and the medium-temperature gas heating heating tube heat exchanger. 14 and the low-temperature air preheating tube heat exchanger 13, the fl...

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Abstract

An oil shale semicoke fluidized combustion and circulation gas heating technology is characterized by comprising the steps of sending oil shale semicoke greater than 0-15mm and residual gas into a fluid bed for low temperature combustion, heating circulation gas flowing in a diaphragm wall heat exchanger with a part of heat released by the combustion, discharging the other part of heat along with smoke generated by the combustion after exchanging heat with a tubular heat exchanger, allowing high-temperature ash and slag generated by the combustion of the semicoke to enter a fluid bed slag cooler for cooling, conveying cooled low-temperature ash and slag to a slag yard, allowing smoke to carry fly ash generated by the combustion to be discharged after exchanging the heat with a high-temperature air preheating tubular heat exchanger, a medium-high temperature gas heating tubular heat exchanger and a low-temperature air preheating tubular heat exchanger, mixing the circulation gas after heating cold circulation gas from a cold gas main line via the diaphragm wall heat exchanger with the cold gas, heating the mixed gas, and allowing the smoke temperature at an outlet of a hearth to be 850-950 DEG C, and hot circulation gas temperature at a hot gas outlet to be less than 720 DEG C.

Description

technical field [0001] The invention relates to the technical field of dry distillation of oil shale gas heat carrier. It is an oil shale semi-coke fluidized combustion cycle gas heating process, which can also be used for coal, waste tires, plastics, and biomass. Background technique [0002] Oil shale is an important energy resource. The reserves of oil shale resources in the world are very huge, and its reserves are as high as (10~15)×10 18 kJ, accounting for about (26-43) × 10 of the total amount of various energy sources in the world 18 35% of kJ, which is higher than the known reserves of crude oil in the world (8×10 18 ~10×10 18 kJ). [0003] The development and utilization of oil shale currently mainly adopts the carbonization furnace-based process route for carbonization and refining. The existing carbonization furnace-based process route uses gas heat carrier as the main heat carrier: the heat cycle gas is used as the main heating carrier to add to the middle o...

Claims

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Application Information

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IPC IPC(8): C10B53/06C10B49/10
CPCY02P20/129C10B53/06C10B49/10
Inventor 刘洪鹏王擎贾春霞柏静儒张金然黄兴伟
Owner NORTHEAST DIANLI UNIVERSITY
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