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Oxygen-enriched combustion device and method of solid fuel circulating fluidized bed

A circulating fluidized bed and solid fuel technology, applied in fluidized bed combustion equipment, combustion methods, combustion types, etc., can solve the problems affecting the absorption of furnace heat, the layout of boiler heating surfaces, and the volume reduction of tail flue, etc. , to achieve the effect of reducing boiler cost, facilitating capture and subsequent utilization, and reducing metal consumption

Inactive Publication Date: 2016-06-22
NORTH CHINA ELECTRIC POWER UNIV (BAODING) +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The traditional oxy-fuel combustion fluidized bed boiler has the same cross-sectional area of ​​the furnace body in the dense-phase zone and the dilute-phase zone, and must go through a long transition section to achieve gas-solid separation; due to the increase in oxygen concentration and the decrease in circulating flue gas concentration, the boiler volume The corresponding reduction, especially the reduction in the volume of the tail flue, has brought great difficulties to the layout of the heating surface of the boiler, thus affecting the absorption of heat in the furnace and reducing the combustion efficiency of coal
In the oxyfuel combustion circulating fluidized bed, how to mix high-purity oxygen with recirculated flue gas and how to inject it into the furnace is a technical problem that needs to be solved mainly. Since there are particles with a particle size below 0.5 μm in the recirculated flue gas, it is different from high Concentration of oxygen (50% or more) mixing is very prone to deflagration and other safety accidents

Method used

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  • Oxygen-enriched combustion device and method of solid fuel circulating fluidized bed

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Embodiment 1

[0018] Such as figure 1 As shown, this embodiment discloses a partition control and multi-stage air distribution device for solid fuel fluidized bed oxygen-enriched combustion such as coal and biomass, including an air chamber 1 and an air distribution device 2 arranged above the air chamber 1 , the furnace 3 above the air distribution device 2, the furnace 3 is composed of three parts: the strong mixing zone 4 with a large lower cross-sectional area, the middle conical transition zone 5 and the quasi-flat flow zone 6 with a small upper cross-sectional area. Solid fuel such as coal or biomass and limestone feeding port 7 is provided in the upper part of zone 4, and a secondary air distribution pipe 8 is provided at the bottom of quasi-flat flow zone 6, and a high-temperature cyclone separator is connected to the upper part of quasi-flat flow zone 6 through pipes 9. The lower end of the high-temperature cyclone separator 9 is connected to the feeder 12, and the feeder 12 is con...

Embodiment 2

[0022] In this embodiment, the combustion device used is the same as that in Embodiment 1.

[0023] Mixed particles of coal powder and corn stalks (corn stalks account for 15% by volume) are used as fuel. During operation, the fuel and limestone are transported to the solid fuel and limestone feeding port 7 through the feeding device. into the furnace; the flue gas output by the high temperature cyclone separator 9 through the flue 16 with the heat exchanger 10 and the economizer 11 enters the medium temperature cyclone separator 13, and the flue gas output by the first flue gas circulation fan 14 is separated from the air Part of the oxygen output from the device 15 is mixed as the primary air; part of the oxygen output from the air separation device 15 is directly used as the secondary air; the flue gas output by the high-temperature cyclone separator 9 through the flue 16 passes through the second flue gas circulation fan 17 and the second flue gas circulation fan 17. Three...

Embodiment 3

[0026] In this embodiment, the combustion device used is the same as that in Embodiment 1.

[0027] The mixed fuel of pulverized coal and biomass molding particles (biomass mixed particles account for 30% by volume) is used as the fuel. During operation, the fuel and limestone are transported to the solid fuel and limestone feeding port 7 through the feeding device. Under the action, it is spread into the furnace; the flue gas output by the high-temperature cyclone separator 9 through the flue 16 with the heat exchanger 10 and the economizer 11 enters the medium-temperature cyclone separator 13, and the flue gas output by the first flue gas circulation fan 14 The gas is mixed with part of the oxygen output from the air separation device 15 and used as the primary wind; part of the oxygen output from the air separation device 15 is directly used as the secondary wind; the flue gas output by the high temperature cyclone separator 9 through the flue 18 is circulated through the se...

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Abstract

The invention discloses an oxygen-enriched combustion device and method of a solid fuel circulating fluidized bed and belongs to the field of clean utilization of solid fuel. The device mainly comprises an air chamber, an air distribution device, a furnace hearth, a high-temperature cyclone separator, a return feeder, a heat exchanger, a coal economizer, a medium-temperature cyclone separator and a secondary air distribution pipe, wherein the furnace hearth is composed of a lower dense-phase bubble or turbulence strongly mixing area with a large sectional area and an upper dilute-phase quick or pneumatic conveyed quasi plug-flow area with a small sectional area. According to the method, combustion of solid fuel is achieved by adopting oxygen-enriched combustion zone control and regulation and multi-stage air distribution in the oxygen-enriched combustion device of the circulating fluidized bed, wherein the primary air is oxygen and recycled exhaust gas mixed air, the secondary air is oxygen, and the recycled exhaust gas includes fuel spreading air and vibrating air. The oxygen-enriched combustion device and method can overcome the defects of the prior art; the CO2 concentration of exhaust gas generated after combustion of solid fuel is made to be above 80%, so that storage or utilization after combustion is facilitated; and meanwhile, emission of nitric oxide and sulfur oxide is reduced, and accordingly the oxygen-enriched combustion device and method have the broad application prospect.

Description

technical field [0001] The invention belongs to the field of clean utilization of coal and biomass, and in particular relates to a solid fuel circulating fluidized bed oxygen-enriched combustion device and method. Background technique [0002] The resource endowment of rich coal, lack of oil and little gas determines that coal will remain the most important basic energy in my country in the foreseeable future. Clean, efficient and low-carbon coal-fired power generation is a major strategic demand to ensure the sustainable development of the country. According to statistics from the China Coal Industry Association, the national coal production in 2013 was about 3.7 billion tons, and the consumption was about 3.61 billion tons. According to the statistics of the National Energy Administration, the total national energy consumption in 2013 was 3.76 billion tons of standard coal, of which coal accounted for 65.7%. As of the end of 2013, the total installed capacity of power gene...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F23C10/10F23C10/26F23C10/20F23C10/18
CPCF23C10/10F23C10/18F23C10/20F23C10/26F23C2201/10F23C2202/30F23C2206/101F23C2900/01001Y02E20/32Y02E20/34
Inventor 张锴刘芸张仪张国强徐钢杨勇平张东柯
Owner NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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