Biomass three-section type entrained flow bed gasification technology with function of waste heat utilization
An entrained-bed, three-stage technology, applied in the field of biomass gasification and biomass three-stage entrained-bed gasification, can solve the problems of reduced carbon conversion efficiency, corrosion, metal corrosion, etc. The effect of protecting the environment
Image
Examples
specific Embodiment approach 2
[0107] Implement on the basis of specific implementation mode 1 implementation, such as figure 1 As shown, the top of the high-temperature entrained bed of the three-stage entrained-bed gasifier device is arranged with a down-flow burner, and the carbon powder, pyrolysis gas and oxygen enter the high-temperature en-flow bed through the down-flow burner The gasification reaction is carried out in the high-temperature air-flow bed, the syngas goes down in the high-temperature air-flow bed, enters the high-temperature heat exchanger through the connecting channel formed by the smooth tube membrane water wall on the inner wall, and goes up to cool after being rectified and rectified, and then passes through the inner wall by the smooth tube The connecting channel formed by the membrane water wall enters the low temperature heat exchanger and is rectified by the rectifier and then descends to cool down. The biomass raw material used is still Quercus sp. (see Table 1 in Embodiment 1...
specific Embodiment approach 3
[0114] It is still implemented on the basis of specific implementation mode 1, such as figure 2 As shown, only: the top of the high-temperature entrained bed of the three-stage entrained entrained gasifier device is arranged with a down-flow burner, and the carbon powder, pyrolysis gas and oxygen enter the high-temperature air through the down-flow burner. The gasification reaction is carried out in the entrained bed, and the synthesis gas descends in the high-temperature entrained bed, enters the high-temperature heat exchanger through rectification and constriction to cool down, and then enters the low-temperature heat exchanger through the connecting channel whose inner wall is composed of a smooth tube membrane water wall And after rectification and necking rectification, it goes up to cool down. The biomass raw material used is still Quercus sp. (see Table 1 in Embodiment 1) as an example, and the main process operating conditions are as in Embodiment 1. The result obta...
specific Embodiment approach 4
[0121] It is still implemented on the basis of specific implementation mode 1, such as image 3 As shown, only: the lower part of the high-temperature entrained bed of the three-stage entrained-bed gasifier device is arranged with a horizontal burner, and the charcoal powder, pyrolysis gas and oxygen enter the high-temperature air through the horizontal burner. The gasification reaction is carried out in the entrained bed, and the syngas goes up in the high-temperature entrained bed, enters the high-temperature heat exchanger through rectification and constriction, and then enters the low-temperature heat exchanger through the connecting channel formed by the smooth tube membrane water wall on the inner wall and After being rectified by the rectifier, it is cooled downwards. The biomass raw material used is still Quercus sp. (see Table 1 in Embodiment 1) as an example, and the main process operating conditions are as in Embodiment 1. The result obtained through implementation...
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Abstract
Description
Claims
Application Information
- IPC
- C10J3/56; C10J3/54; C10J3/72
- CPC
- C10J2300/094; C10J3/56; C10J3/86; C10J3/62; C10J3/76; C10J2300/0916; C10J2300/1846; C10J3/485
- Inventors
- 韩剑锋