Pyrolysis and gasification device and technology

Abstract

The invention discloses a pyrolysis and gasification device and technology. The device comprises three main reactors, namely, an uplink bed oxidation combustor, a downlink bed rapid pyrolyzer and a bubbling bed gasifier. Feed coal or a mixture of coal and biomass is added from the upper part of the pyrolyzer, is rapidly heated by high-temperature circulating semicoke from the combustor and has a catalytic pyrolysis reaction, and semicoke, tar and gas are produced; through rapid separation, fresh semicoke produced in the pyrolyzer and the high-temperature circulating semicoke are sent into the gasifier to have a gasification reaction with a gasification agent; the semicoke which is not gasified is continuously sent into the combustor to be partially oxidized and combusted under the action of oxygen, so that a large quantity of high-temperature circulating semicoke is obtained. The device and the technology have the advantages that a combustion-pyrolysis-gasification process in graded utilization of raw materials is coupled, co-production of high-quality tar, gas and synthesis gas is realized by the aid of the catalytic activity and the heat-carrying capability of the semicoke, and the economic benefit and the social benefit are high.

Description

technical field [0001] The invention relates to a pyrolysis gasification device and process, especially a three-tower high-throughput semi-coke circulating fluidized bed coal or a mixture of coal and biomass heat based on semi-coke's catalytic activity and self-heating capacity Degasification process. The invention belongs to the field of thermochemical conversion graded utilization of low-rank coal or mixture of coal and biomass coupled with pyrolysis-gasification-combustion. Background technique [0002] Coal is the main energy source in my country, and it will still play a dominant role in my country's energy structure for a long time to come. Among them, low-rank coal reserves represented by lignite and low-metamorphic bituminous coal account for 55% of the total coal resources. above. As high-metamorphic coal types become less and less, the optimal utilization of low-rank coals becomes increasingly important. However, low-rank coal has low degree of coalification, hig...

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Problems solved by technology

However, this process has the following disadvantages: First, due to the small particle size of the high-temperature circulating ash, there is a high dust content in the pyrolysis gas, which is likely to cause problems such as pipeline blockage and difficult separation of dust and tar. The calorific value is low, the density is low, and the heat transfer efficiency is not high; secondly, the pyrolysis device used in this process is a bubbling fluidized bed pyrolyzer. There are significant differences in the reaction stages, which reduces the select

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