High-temperature and ultrahigh-pressure reheat steam boiler of biomass direct combination energy-conservation circulating fluidized bed

A circulating fluidized bed, reheated steam technology, applied in fluidized bed boilers, steam boilers, fluidized bed combustion equipment, etc., can solve the problems of yellow straw biomass difficulty, short continuous operation time, and low boiler unit efficiency. , to achieve clean and efficient combustion of steam-water cycle temperature control, solve energy waste and environmental pollution, easy to adjust

Pending Publication Date: 2019-09-10
哈尔滨红光锅炉总厂有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The present invention solves the difficulty of directly burning yellow straw biomass in the existing biomass circulating fluidized bed boiler, the continuous operation time is short, the efficiency of the boiler unit is low, the pollution discharge is high, the feeding is not smooth, and the reliability is poor, resulting in a high failure rate of the boiler , the difficult problem of biomass molding, and then propose a biomass direct combustion energy-saving circulating fluidized bed high temperature and ultra high pressure reheating steam boiler

Method used

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  • High-temperature and ultrahigh-pressure reheat steam boiler of biomass direct combination energy-conservation circulating fluidized bed
  • High-temperature and ultrahigh-pressure reheat steam boiler of biomass direct combination energy-conservation circulating fluidized bed
  • High-temperature and ultrahigh-pressure reheat steam boiler of biomass direct combination energy-conservation circulating fluidized bed

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specific Embodiment approach 1

[0020] Specific implementation mode one: combine Figure 1 to Figure 7 Describe this embodiment, a biomass direct combustion energy-saving circulating fluidized bed high temperature ultra-high pressure reheat steam boiler described in this embodiment, it includes a furnace 2, a first tail flue 4, a connecting flue 5 and a second tail The flue 6, this embodiment also includes a biomass direct combustion system 1 and a separation and return system 3, the biomass direct combustion system 1 is installed at the lower part of the furnace 2, the upper part of the furnace 2 is connected with the upper part of the separation and return system 3, and the furnace The lower part of 2 is connected to the lower part of the separation and return system 3, the smoke inlet of the first tail flue 4 is connected to the upper part of the separation and return system 3, and the lower part of the first tail flue 4 is connected to the second tail by connecting the flue 5 The lower part of the flue 6...

specific Embodiment approach 2

[0022] Specific implementation mode two: combination Figure 1 to Figure 7 Describe this embodiment, the biomass direct combustion system 1 of a biomass direct combustion energy-saving circulating fluidized bed high-temperature and ultra-high pressure reheating steam boiler in this embodiment includes a biomass direct combustion feeding device 1-1, a feeder Device 1-2, secondary air device 1-3, tertiary air device 1-4 and slag discharge device 1-5, tertiary air device 1-4, biomass direct combustion feeding device 1-1, secondary air device 1 -3. The charging device 1-2 is installed in the lower part of the furnace 2 sequentially from top to bottom.

[0023] The biomass enters the lower part of the furnace 2 through the biomass direct combustion feeding device 1-1 for combustion, and the bed material enters the lower part of the furnace 2 through the feeding device 1-2 for internal fluidization. The biomass direct combustion feeding device 1-1 and the feeding The device 1-2 is ...

specific Embodiment approach 3

[0026] Specific implementation mode three: combination Figure 1 to Figure 7 Describe this embodiment, the separation and return system 3 of a biomass direct combustion energy-saving circulating fluidized bed high-temperature and ultra-high pressure reheating steam boiler in this embodiment is composed of a separator 3-1 and a return device 3-2. The smoke outlet of the furnace 2 is connected to the upper part of the first tail flue 4 through the separator 3-1, and the outlet of the return device 3-2 is connected to the lower part of the furnace 2. Other components and connections are the same as those in the first embodiment.

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Abstract

The invention discloses a high-temperature and ultrahigh-pressure reheat steam boiler of a biomass direct combination energy-conservation circulating fluidized bed, relates to the high-temperature andultrahigh-pressure reheat steam boiler, in particular to the high-temperature and ultrahigh-pressure reheat steam boiler of the biomass direct combination energy-conservation circulating fluidized bed, and solves the problems of difficult direct combustion of yellow straw biomasses, shorter continuous operation time, low boiler unit efficiency, more pollution discharge, blocked feeding, weak reliability, higher boiler failure rate and difficult biomass formation. A biomass direct combustion system is mounted at the lower part of a hearth; the upper part of the hearth is connected with the upper part of a separation and return system; the lower part of the hearth is connected with the lower part of the separation and return system; a smoke inlet of a first tail flue is connected with the upper part of the separation and return system; and the lower part of the first tail flue is connected with the lower part of a second tail flue through a connecting flue. The high-temperature and ultrahigh-pressure reheat steam boiler of the biomass direct combination energy-conservation circulating fluidized bed belongs to the field of power generation and combined heat and power generation.

Description

technical field [0001] The invention relates to a high-temperature, ultra-high-pressure reheating steam boiler, in particular to a biomass direct combustion energy-saving circulating fluidized bed high-temperature, ultra-high-pressure reheating steam boiler, which belongs to the field of power generation and combined heat and power generation. Background technique [0002] The existing biomass circulating fluidized bed boiler is difficult to directly burn the yellow straw biomass, the continuous operation time is short, the efficiency of the boiler unit is low, the pollution is high, the feeding is not smooth, and the reliability is poor, resulting in a high failure rate of the boiler. Contents of the invention [0003] The present invention solves the difficulty of directly burning yellow straw biomass in the existing biomass circulating fluidized bed boiler, the continuous operation time is short, the efficiency of the boiler unit is low, the pollution discharge is high, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F22B31/00F23C10/26F22G3/00F23L9/00F23J15/02
CPCF22B31/0007F22G3/00F23C10/26F23J15/022F23L9/00
Inventor 张福强
Owner 哈尔滨红光锅炉总厂有限责任公司
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