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Lignite drying and pyrolyzing device

A pyrolysis and drying technology, which is applied in the field of coal pyrolysis, can solve problems such as wasting heat energy, reducing heat energy utilization efficiency, and outlet pipe blockage, and achieves the effects of reducing production costs, improving heat energy utilization efficiency, and reducing energy consumption

Inactive Publication Date: 2012-07-18
SHANDONG UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

A large amount of tar will be produced in the process of coal pyrolysis. In the process of exporting the tar, as the temperature gradually decreases, the tar will gradually condense, and even solidify on the outlet pipe. The gradual accumulation will cause the outlet pipe to be blocked, causing safety hazards and reducing coal heat. The stability of the solution process
In the prior art, the high-temperature gas generated after coal pyrolysis is directly discharged to the outside after being adsorbed, which wastes a lot of heat energy and reduces the utilization efficiency of heat energy
In addition, in the actual production process, a high-temperature gas-solid separator needs to be installed outside the reactor, and the separator needs to be additionally heated to avoid condensation of heavy tar, which increases production costs and occupies a large space

Method used

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  • Lignite drying and pyrolyzing device
  • Lignite drying and pyrolyzing device

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Lignite with a moisture content of 42% by weight and a particle size of <25mm is continuously fed into the drying fluidized bed cylinder 1 at a feed rate of 1 ton / hour for drying. After drying, the moisture content of the lignite drops to <2%. It continuously enters the pyrolysis fluidized bed cylinder 2 through the coal falling pipe 3, the return mechanism 4, and the transfer pipe 5. The conveying pipeline 28 flows to the pyrolysis fluidized bed cylinder at a flow rate of 1800 cubic meters / hour (standard state) The combustion flue gas at 850°C is passed into the body 2 to quickly pyrolyze the lignite in the pyrolysis fluidized bed cylinder 2, and the pyrolysis gas phase product tar steam and coal gas will enter the cyclone separator 6 along with the combustion flue gas. The gas outlet pipe 7 passes through the first electric tar catcher 8 to obtain a large amount of tar and discharge it, and the gas enters a primary condenser 9 which controls the temperature of the gas b...

Embodiment 2

[0032] Lignite with a moisture content of 35wt% and a particle size of <30mm is continuously fed into the drying fluidized bed cylinder 1 at a feed rate of 2 tons / hour for drying. After drying, the moisture content of the lignite drops to <2.8%. It continuously enters the pyrolysis fluidized bed cylinder 2 through the coal falling pipe 3, the return mechanism 4 and the transfer pipe 5. The conveying pipeline 28 flows to the pyrolysis fluidized bed cylinder at a flow rate of 3000 cubic meters / hour (standard state) The combustion flue gas at 850°C is passed into the body 2 to quickly pyrolyze the lignite in the pyrolysis fluidized bed cylinder 2, and the pyrolysis gas phase product tar steam and coal gas will enter the cyclone separator 6 along with the combustion flue gas. The gas outlet pipe 7 passes through the first electric tar catcher 8 to obtain a large amount of tar and discharge it, and the gas enters a primary condenser 9 which controls the temperature of the gas between...

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Abstract

The invention discloses a lignite drying and pyrolyzing device. The device comprises a drying fluidized bed barrel and a pyrolyzing fluidized bed barrel, wherein a coal falling pipe is arranged at the bottom of the drying fluidized bed barrel and communicated with a material returning mechanism; the material returning mechanism is communicated with the pyrolyzing fluidized bed barrel through a transmission pipe; at least one stage of cyclone separator is arranged in the pyrolyzing fluidized bed barrel; the outlet of the last stage of cyclone separator is communicated with a coal gas outlet pipe of the pyrolyzing fluidized bed barrel; the coal gas outlet pipe is communicated with a first electrical tar precipitator; the first electrical tar precipitator is communicated with a primary condenser; and the primary condenser is communicated with the bottom of the drying fluidized bed barrel through a first fan. By the device, the phenomenon that a pipe is blocked in the process of discharging tar is avoided, a heat source can be recycled, the utilization efficiency of heat energy is improved, energy consumption in the process of pyrolyzing coal is reduced, and the production cost of pyrolyzing the coal is reduced.

Description

Technical field [0001] The invention relates to the field of coal pyrolysis, in particular to a lignite drying pyrolysis device. Background technique [0002] As an important energy source, coal generally needs to be converted to coal in the prior art to improve its utilization efficiency. Among them, the coal pyrolysis process is an important process for coal conversion. The hydrogen-rich components in the coal are reduced under relative temperature and conditions. Extracted with liquid and gas, benzene, naphthalene, anthracene, phenanthrene, and a variety of fused-ring aromatic hydrocarbon compounds and heterocyclic compounds that cannot be synthesized artificially can be obtained at the same time, which improves the utilization rate of coal. During the process of coal pyrolysis, a large amount of tar will be produced. As the temperature gradually decreases during the process of exporting the tar, the tar will gradually condense and even solidify on the export pipe. The gradual...

Claims

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Application Information

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IPC IPC(8): C10B49/10C10B57/10
Inventor 梁鹏张华伟武加峰赵辉王力
Owner SHANDONG UNIV OF SCI & TECH
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