Two-step desulfurization technology of coal burning process

A desulfurization process and coal combustion technology, applied in the field of coal combustion desulfurization, can solve the problem of sulfur fixation efficiency lower than 50%, etc., and achieve the effects of inhibiting high temperature decomposition, ensuring combustion and improving desulfurization efficiency

Inactive Publication Date: 2016-03-09
GUANGXI KUONENGBA ENERGY TECH DEV CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in reality, calcium-based desulfurizers use calcium sulfate as the main sulfur-containing ore phase, which will decompose below 1100°C under the combustion condition of pulverized coal, so that the sulfur fixation efficiency is still mostly lower than 50%.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] A two-step desulfurization process in a coal combustion process, comprising the following steps:

[0024] S1. Mix pulverized coal and desulfurizer A evenly, grind them, and pass through a 100-150 mesh sieve to obtain desulfurized coal A. Spray desulfurized coal A into the boiler for combustion; wherein, desulfurizer A is made of the following raw materials Proportion by weight: 25 parts of cinder, 25 parts of calcium oxide, 46 parts of calcium hydroxide and 8 parts of aluminum oxide, the weight ratio of coal powder and desulfurizer A is 50:1;

[0025] S2. Mix the pulverized coal and desulfurizer B evenly to obtain desulfurized coal B, and then spray it into the main combustion zone of the boiler through the spray pipe intersecting with the secondary air pipe; wherein: the desulfurizer B is prepared from the following raw materials in parts by weight Ratio: 11 parts of aluminum sulfate, 11 parts of sodium carbonate, 9 parts of potassium chloride, 12 parts of iron carbona...

Embodiment 2

[0031] A two-step desulfurization process in a coal combustion process, comprising the following steps:

[0032] S1. Mix pulverized coal and desulfurizer A evenly, grind them, and pass through a 100-150 mesh sieve to obtain desulfurized coal A. Spray desulfurized coal A into the boiler for combustion; wherein, desulfurizer A is made of the following raw materials Proportion by weight: 20 parts of cinder, 30 parts of calcium oxide, 52 parts of calcium hydroxide and 6 parts of aluminum oxide, the weight ratio of coal powder and desulfurizer A is 53:1;

[0033] S2. Mix the pulverized coal and desulfurizer B evenly to obtain desulfurized coal B, and then spray it into the main combustion zone of the boiler through the spray pipe intersecting with the secondary air pipe; wherein: the desulfurizer B is prepared from the following raw materials in parts by weight Ratio: 10 parts of aluminum sulfate, 10 parts of sodium carbonate, 8 parts of potassium chloride, 15 parts of iron carbona...

Embodiment 3

[0039] A two-step desulfurization process in a coal combustion process, comprising the following steps:

[0040] S1. Mix pulverized coal and desulfurizer A evenly, grind them, and pass through a 100-150 mesh sieve to obtain desulfurized coal A. Spray desulfurized coal A into the boiler for combustion; wherein, desulfurizer A is made of the following raw materials Proportion by weight: 30 parts of cinder, 20 parts of calcium oxide, 40 parts of calcium hydroxide and 10 parts of aluminum oxide, the weight ratio of coal powder and desulfurizer A is 55:1;

[0041] S2. Mix the pulverized coal and desulfurizer B evenly to obtain desulfurized coal B, and then spray it into the main combustion zone of the boiler through the spray pipe intersecting with the secondary air pipe; wherein: the desulfurizer B is prepared from the following raw materials in parts by weight Ratio: 12 parts of aluminum sulfate, 12 parts of sodium carbonate, 10 parts of potassium chloride, 9 parts of iron carbon...

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PUM

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Abstract

The invention discloses a two-step desulfurization technology of the coal burning process. The technology comprises the following steps that S1, pulverized coal is mixed with a desulfurizing agent A to prepare desulfurized coal A, and the desulfurized coal A is sprayed into a boiler to be burnt, wherein the desulfurized coal A is prepared by mixing coal slags, calcium oxide, calcium hydroxide and aluminum oxide according to proportions; S2, pulverized coal is mixed with a desulfurizing agent B to prepare desulfurized coal B, and then the desulfurized coal B is sprayed into a main burning zone of the boiler through a material spray pipe, wherein the material spray pipe and a secondary air pipe are arranged in a crossed mode, the desulfurizing agent B is prepared by mixing aluminum sulfate, sodium carbonate, potassium chloride, iron carbonate, vanadium pentoxide and zinc borate according to proportions, the desulfurizing agent B is added to water and mixed to be prepared into mixed suspension with the mass percent of 12%-20%, the mixed suspension is mixed with the pulverized coal, standing is conducted till the water content ranges from 3% to 5%, and the desulfurized coal B is prepared. According to the two-step desulfurization technology of the coal burning process, the desulfurizing agents are added in a segmented mode, the effect of calcium-based desulfuration agents is fully exerted, and the desulfurization efficiency is greatly improved.

Description

technical field [0001] The invention relates to coal combustion desulfurization, in particular to a two-step desulfurization process of coal combustion. Background technique [0002] Sulfur in coal includes inorganic sulfur, organic sulfur and elemental sulfur. Inorganic sulfur mainly exists in the form of disulfide and sulfate, most of the disulfide is pyrite, a small part is marcasite, and the sulfate is mainly calcium sulfate CaSO 4 ; The organic sulfur is directly bonded to the coal matrix in the form of mercaptan, sulfide, disulfide and aromatic ring sulfur represented by thiophene series. The use of calcium-based desulfurizers for desulfurization during coal combustion is currently the most widely used desulfurization method. Due to the complexity of the sulfur fixation reaction process and the re-decomposition of sulfate at high temperatures, the effective utilization rate and sulfur fixation efficiency of combustion calcium-based desulfurizers are generally low. I...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/86B01D53/50B01D53/83C10L9/10C10L10/00F23C13/08
CPCB01D53/508B01D53/83B01D53/8609B01D2251/304B01D2251/306B01D2251/404B01D2255/2022B01D2255/2027B01D2255/20723B01D2255/20738B01D2257/302B01D2258/0283B01D2259/128C10L9/10C10L10/00F23C13/08
Inventor 江东黄天梁君祚梁承悍
Owner GUANGXI KUONENGBA ENERGY TECH DEV CO LTD
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