Low-quality fuel pyrolysis process

A low-quality fuel, pyrolysis technology, used in the petroleum industry, direct heating dry distillation, special forms of dry distillation, etc., can solve the problems of only burning off, not getting finished semi-coke, difficult to separate, etc., to improve thermal efficiency, improve Effective utilization and the effect of reducing energy loss

Active Publication Date: 2014-08-13
吉林省利用厚生能源科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The fluidized bed pyrolysis process is widely used due to its fast reaction speed and high tar yield. However, this process usually uses solid particles as the heat source carrier. The semi-coke and solid particles produced during the pyrolysis process are fine and mixed together, making it difficult to separate , can only be burned, so the production process usually does not get the finished semi-coke, such as patent No. 200710063368.2 and 200910272712.8
Although the patent No. 200910215125.5 can use the fluidized bed pyrolysis process to produce semi-coke and tar, its semi-coke products need to be cooled by an external medium, which consumes additional system heat and increases the energy consumption of the production system, and its fluidization medium is The use of uncooled combustible gas causes a large amount of tar vapor carried in the combustible gas to flow back into the fluidized bed for secondary decomposition, and becomes a small molecule flammable alkane gas, which greatly reduces the tar yield of the system and increases the system efficiency. Cost of production

Method used

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  • Low-quality fuel pyrolysis process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0048] As attached figure 1 As shown, the elemental analysis of the dry ash-free base of lignite with a particle size of about 2mm and a water content of 37% is: C-70.5%, H-5.4%, O-22.2%, N-1.7%, S-0.2%, The high calorific value is 19.1MJ / kg. The lignite is indirectly heated by the high temperature flue gas with an inlet temperature of 530°C in the rotary drying furnace 1 to remove moisture to 5%, and then is sent to the electromagnetic vibrating feeder 5, and then sent to the gauge pressure through the discharge valve 6 In the 3kPa fluidized bed pyrolysis furnace 8, the heating surface of the inner heating tube bundle 7 is arranged in the fluidized bed pyrolysis furnace 8, and the high temperature flue gas of 810℃ flows through the inner heating tube bundle 7 to provide the lignite pyrolysis process Part of the heat required. The combustible gas produced during the pyrolysis process carries some solid particles out of the upper part of the fluidized bed pyrolysis furnace 8, ...

Embodiment 2

[0054] As attached figure 1 As shown, the elemental analysis of bituminous coal with a particle size of about 1mm and a water content of 12% is: C-76%, H-5.7%, O-17.3%, N-0.8%, S-0.2%, The high calorific value is 21.9MJ / kg. The bituminous coal is indirectly heated by high-temperature flue gas with an inlet temperature of 580°C in the rotary drying furnace 1 to remove moisture to 4%, and then sent to the electromagnetic vibrating feeder 5, and then sent to the gauge pressure through the discharge valve 6 In the 5kPa fluidized bed pyrolysis furnace 8, the heating surface of the inner heating tube bundle 7 is arranged in the fluidized bed pyrolysis furnace 8, and the high temperature flue gas at 850°C flows through the inner heating tube bundle 7 to provide the lignite pyrolysis process Part of the heat required. The combustible gas produced during the pyrolysis process carries some solid particles out of the upper part of the fluidized bed pyrolysis furnace 8, and then enters t...

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Abstract

The invention discloses a low-quality fuel pyrolysis process. The process comprises the following steps: by mutually combining a coke dry quenching technology and a fluidized bed pyrolysis technology, mixing coke quenching gas absorbing semi-coke heat with a part of high-temperature flue gas to be used as a fluidizing medium, returning cooled fluidized gas to a coke dry quenching furnace to be used as the coke quenching gas, and using the high-temperature flue gas obtained after burning pyrolysis gas as a system heat source. The low-quality fuel pyrolysis process adopts the fluidized bed rapid pyrolysis technology, and effectively absorbs the waste heat of high-temperature semi-coke and improves the heat efficiency of a system at the same time; moreover, the fluidizing medium and a coke quenching medium of the system are coupled for use so as to ensure the tar yield, reduce the coke quenching cost, and achieve the synchronous production of tar and the semi-coke by using the fluidized bed technology.

Description

technical field [0001] The invention relates to the field of chemical application technology, in particular to a low-quality fuel pyrolysis process. Background technique [0002] Low-quality fuels represented by lignite and lean coal have a total reserve of more than 110 billion tons in my country. They have the characteristics of high water content, oxygen content and volatile matter, low carbon content and calorific value. These low-quality fuels are buried shallow and easy to be exploited on a large scale, but they are not suitable for long-distance transportation because of their low mechanical strength, easy weathering, fragmentation, spontaneous combustion, and difficult chemical processing. They are also not suitable for direct combustion as fuel for power generation, as direct combustion is less heat efficient and emits 20% more greenhouse gases than burning high-quality anthracite coal. The above characteristics have greatly restricted the application of low-qualit...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10B49/22C10B53/04C10B57/10C10B39/02
CPCY02P20/129
Inventor 王凯孙荣峰范晓旭关海滨姜建国张卫杰
Owner 吉林省利用厚生能源科技有限公司
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