Biomass fuel boiler device and working method thereof

A technology of biomass fuel and boiler equipment, which is applied in the direction of combustion methods, safety devices of combustion chambers, combustion chambers, etc., and can solve problems such as low flow, elevated temperature, and reduced heating efficiency

Inactive Publication Date: 2018-05-11
XUZHOU INSTITUTE OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Nowadays, in the process of processing biomass fuel boilers, it is necessary to exhaust air into the furnace body through the airflow disturbance device for heating. However, the flow rate of the current airflow disturbance device is too low to make the temperature in the furnace rise rapidly, resulting in the heating efficiency. reduce

Method used

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  • Biomass fuel boiler device and working method thereof
  • Biomass fuel boiler device and working method thereof
  • Biomass fuel boiler device and working method thereof

Examples

Experimental program
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Effect test

preparation example Construction

[0062] In order to obtain a gas disturbance impeller with high tensile strength, small thermal deformation effect, good corrosion resistance and long service life, the preparation method of the gas disturbance impeller 3-4-4 includes the following steps:

[0063] Step 1: Add 2501 to 4801 parts of ultrapure water with a conductivity of 4.65 μS / cm to 7.75 μS / cm into the reactor, start the stirrer in the reactor at a speed of 86 rpm to 131 rpm, and start the heating pump to make The temperature in the reaction kettle rose to 66 ℃ ~ 96 ℃; 3,4-dimethyl-5-oxopiperazine-1-carboxylate benzyl ester, 4-(3-nitrobenzylidene)piperidine- tert-butyl 1-carboxylate, 1,1-dimethylethyl 4-[2-[(acetylamino)methyl]-4-aminophenyl]-1-piperazinecarboxylate, stirred until completely dissolved , adjust the pH value to 4.6 to 9.6, adjust the agitator speed to 131 rpm to 241 rpm, the temperature to 121 °C to 166 °C, and the esterification reaction for 16 to 31 hours;

[0064] Step 2: Take ethyl 3-((1-met...

Embodiment 1

[0076] Manufacture the gas disturbance impeller 3-4-4 of the present invention according to the following steps, and in parts by weight:

[0077] Step 1: Add 2501 parts of ultrapure water with a conductivity of 4.65 μS / cm into the reactor, start the stirrer in the reactor at a speed of 86 rpm, and start the heating pump to raise the temperature in the reactor to 66°C; Add 31 parts of benzyl 3,4-dimethyl-5-oxopiperazine-1-carboxylate, 89 parts of tert-butyl 4-(3-nitrobenzylidene)piperidine-1-carboxylate, 4 -55 parts of 1,1-dimethylethyl [2-[(acetylamino)methyl]-4-aminophenyl]-1-piperazinecarboxylate, stirred until completely dissolved, and adjusted to pH 4.6, Adjust the rotation speed of the agitator to 131 rpm, the temperature is 121°C, and the esterification reaction is carried out for 16 hours;

[0078] Step 2: Take 29 parts of ethyl 3-((1-methyl-1H-pyrazol-4-yl)methylamino)propionate, 1-benzyl-2,4-dioxopiperidine-3 - 69 parts of methyl carboxylate are pulverized, the powd...

Embodiment 2

[0083] Manufacture the gas disturbance impeller 3-4-4 of the present invention according to the following steps, and in parts by weight:

[0084] Step 1: Add 3651 parts of ultra-pure water with a conductivity of 6.25 μS / cm into the reactor, start the stirrer in the reactor at a speed of 108 rpm, and start the heating pump to raise the temperature in the reactor to 81°C; Add 48 parts of benzyl 3,4-dimethyl-5-oxopiperazine-1-carboxylate, 114 parts of tert-butyl piperidine-1-carboxylate, 4 -75 parts of 1,1-dimethylethyl [2-[(acetylamino)methyl]-4-aminophenyl]-1-piperazinecarboxylate, stirred until completely dissolved, and adjusted to pH 7.3, Adjust the rotation speed of the agitator to 186 rpm, the temperature is 146°C, and the esterification reaction takes 23 hours;

[0085] Step 2: Take 52 parts of ethyl 3-((1-methyl-1H-pyrazol-4-yl)methylamino)propionate, 1-benzyl-2,4-dioxopiperidine-3 - 116 parts of methyl carboxylate are pulverized, and the particle size of the powder is 11...

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Abstract

Provided is a biomass fuel boiler device and a working method of the biomass fuel boiler device. The device is characterized in that a motor in a power chamber drives a transmission shaft to rotate, and the transmission shaft in a transmission chamber is of a cavity structure with through holes in the surface; an inner cavity of the transmission chamber communicates with the outside through a gasinlet pipe, a fresh air path driven by a mixing motor to rotate is arranged in a mixing chamber, and a mixing shaft is rotationally arranged in an inner cavity of the fresh air path; through holes areformed in the surface of the fresh air path, meanwhile the surface of the fresh air path is fixedly connected with gas disturbance blades, and the upper end and the lower end of the mixing shaft arecorrespondingly and fixedly connected with a gas inlet pipe of a rotary spray head and the upper end of the transmission shaft; and through holes are formed in the lower surface of a converging chamber at the upper end of the mixing chamber, a catalyst spray nozzle is connected to the lower portion of the mixing chamber, and the exterior of the gas inlet pipe of the rotary spray head is connectedto the upper opening end of the converging chamber through a bearing. The method comprises the steps that the rotary spray head is controlled to rotate, or meanwhile the gas disturbance blades are controlled to rotate, and a catalyst is introduced. The device and method are good in disturbance effect, and the heating efficiency of a boiler can be improved.

Description

technical field [0001] The invention relates to a biomass fuel boiler device and a working method thereof, belonging to the field of boiler equipment. Background technique [0002] In recent years, with the rapid development of the national economy, the boiler industry using biomass as fuel has achieved rapid development. With the increase in the number of industrial furnaces and the improvement of product processing quality requirements, the matching airflow disturbance device Need to meet the technical requirements of different standards such as large flow. Nowadays, in the process of processing biomass fuel boilers, it is necessary to exhaust air into the furnace body through the airflow disturbance device for heating. However, the flow rate of the current airflow disturbance device is too low to make the temperature in the furnace rise rapidly, resulting in the heating efficiency. reduce. Contents of the invention [0003] Aiming at the problems existing in the above...

Claims

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Application Information

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IPC IPC(8): F23C7/00F23C13/00F23M11/00
Inventor 梁峙梁骁马捷韩宝平刘喜坤许旭张明胜陈兴祥朱雪强
Owner XUZHOU INSTITUTE OF TECHNOLOGY
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