CN113025350A - Air preheating structure arranged in coke oven - Google Patents

Air preheating structure arranged in coke oven Download PDF

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Publication number
CN113025350A
CN113025350A CN202110336133.6A CN202110336133A CN113025350A CN 113025350 A CN113025350 A CN 113025350A CN 202110336133 A CN202110336133 A CN 202110336133A CN 113025350 A CN113025350 A CN 113025350A
Authority
CN
China
Prior art keywords
air
coke oven
air channel
inlet
preheated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202110336133.6A
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Chinese (zh)
Inventor
段衍泉
王明登
于义林
袁朝晖
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Acre Coking and Refractory Engineering Consulting Corp MCC
Original Assignee
Acre Coking and Refractory Engineering Consulting Corp MCC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Acre Coking and Refractory Engineering Consulting Corp MCC filed Critical Acre Coking and Refractory Engineering Consulting Corp MCC
Priority to CN202110336133.6A priority Critical patent/CN113025350A/en
Publication of CN113025350A publication Critical patent/CN113025350A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B29/00Other details of coke ovens
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B45/00Other details
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L15/00Heating of air supplied for combustion
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/004Systems for reclaiming waste heat
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Coke Industry (AREA)

Abstract

The invention relates to an air preheating structure arranged in a coke oven, which comprises an air channel; the air channel and the coke oven branch flue are arranged side by side; an air inlet is arranged at one end of the air channel close to the coke oven chimney and is connected with one end of an air channel inlet pipeline, the other end of the air channel inlet pipeline extends to the upper part of the ground, and the air inlet of the air channel inlet pipeline is communicated with the atmosphere; the other end of the air channel is provided with a preheated air outlet which is connected with a preheated air outlet pipeline. The invention utilizes the waste gas of the coke oven flue to heat the air in the air channel, the heated air is sent to the coal tower bucket mouth by the blower, the hot air is used for preserving the heat of the coal tower bucket mouth and the emptying device, or the air is sent to the air suction inlet in the dry quenching gas circulation system, and the preheated air is used for combusting the combustible components in the circulating gas; the air preheating structure is also beneficial to reducing the temperature of the basement of the coke oven and improving the operating environment of the basement.

Description

Air preheating structure arranged in coke oven
Technical Field
The invention relates to the technical field of energy conservation and consumption reduction of coal coking, in particular to an air preheating structure arranged in a coke oven.
Background
The temperature of the coke oven flue gas is about 230 ℃, and part of the heat can be utilized on the premise of not influencing the emission of a chimney. If the waste gas of the coke oven flue is considered to preheat the air, the temperature of the flue wall can be reduced, the operation environment of the basement of the coke oven can be improved, and the hot air can be further utilized. In the coke oven area, there are two locations where hot air is required, one is the coal tower (northern cold district) and the other is the air intake duct in the dry quenching gas circulation system.
The water content of the blended coal in the coal tower of the coke oven is about 10 percent, and heat insulation measures must be taken for a coal tower bucket mouth in northern cold regions to prevent the coal from freezing. The traditional coal tower hopper mouth adopts heating media such as steam, coal gas, flue waste gas and the like for heat preservation, or adopts modes such as electric heat tracing and the like, but the using effect is not ideal. The steam is easy to freeze after being condensed, the coal gas has potential safety hazard for fire extinguishing, and the heating temperature of the coal gas is high, so that the coal material near the outer wall of the coal tower hopper mouth is easy to be carbonized and hardened; the flue waste gas contains harmful gases such as carbon monoxide and the like, so that potential safety hazards exist; for the coal tower emptying devices with irregular shapes, electric heat tracing is difficult to implement and the heat preservation effect is not good.
An air suction pipe in a dry quenching gas circulation system is generally used for sucking normal temperature air to burn combustible components in dry quenching, and the normal temperature air has a preheating process after entering the dry quenching, so that H in the circulation gas2Can only be controlled to be about 3 percent, CO can only be controlled to be about 6 percent, if preheated air is adopted to be introduced into dry quenching coke, the combustion will be more sufficient, not only H2And the concentration of CO can be effectively reduced, and more steam can be generated by dry quenching.
Disclosure of Invention
The invention provides an air preheating structure arranged in a coke oven, which utilizes coke oven flue waste gas to heat air in an air channel, the heated air is sent to a coal tower bucket mouth by a fan, the hot air is used for preserving the heat of the coal tower bucket mouth and a discharging device, or the heated air is sent to an air suction inlet in a dry quenching gas circulating system, and combustible components in circulating gas are combusted by the preheated air; the air preheating structure is also beneficial to reducing the temperature of the basement of the coke oven and improving the operating environment of the basement.
In order to achieve the purpose, the invention adopts the following technical scheme:
an air preheating structure arranged in a coke oven comprises an air channel; the air channel and the coke oven branch flue are arranged side by side; an air inlet is arranged at one end of the air channel close to the coke oven chimney and is connected with one end of an air channel inlet pipeline, the other end of the air channel inlet pipeline extends to the upper part of the ground, and the air inlet of the air channel inlet pipeline is communicated with the atmosphere; the other end of the air channel is provided with a preheated air outlet which is connected with a preheated air outlet pipeline.
The air channel and the coke oven smoke distributing channel are integrally built and formed when the coke oven body is built.
The top of the air channel is flush with the top of the coke oven branch flue, the part of the air channel above the elevation of the basement of the coke oven is arranged between the pipeline system at the corresponding side of the coke oven and the coke oven branch flue, and the part of the air channel below the elevation of the basement of the coke oven extends to the lower part of the pipeline system at the corresponding side of the coke oven.
A multilayer heat exchange structure is arranged in the air channel along the height direction; each layer of heat exchange structure consists of a plurality of heat exchange fins and a cross brace, the two ends of the cross brace are fixedly connected with the side walls of the two sides of the air channel respectively, and the plurality of heat exchange fins are longitudinally arranged on the upper edge of the cross brace.
The cross braces and the heat exchange fins are all steel components.
The air inlet of the air channel inlet pipeline is horizontally arranged, and a grate is arranged at the air inlet.
And a preheated air outlet of the preheated air outlet pipeline is connected with a coal tower hopper nozzle and a heat preservation gas inlet of the discharging device or connected with an air suction inlet of a dry quenching gas circulating system, and a fan is arranged on the preheated air outlet pipeline.
The fan and the preheated air outlet pipeline are provided with heat insulation structures; the preheated air outlet pipeline is provided with a gas regulating valve, a compensator, a flowmeter, a temperature measuring device and a pressure measuring device.
Compared with the prior art, the invention has the beneficial effects that:
1) the waste heat utilization of the coke oven flue gas is realized.
2) The temperature of the basement of the coke oven is reduced, and the working environment is improved;
3) the preheated air can be used for preserving the heat of the coal tower hopper nozzle and the emptying device, and compared with the conventional heating medium, the preheated air has the advantages that firstly, the hot air is nontoxic and harmless, and no condensed water is generated; secondly, the temperature of the hot air is not high, so that the coal material is not carbonized and hardened;
4) the preheated air can be used for air sucked in a dry quenching gas circulation system, and compared with the air sucked at normal temperature, the air has the advantages that the combustible components in the dry quenching can be combusted more fully; and the amount of steam generated by the dry quenching boiler is increased.
Drawings
FIG. 1 is a schematic structural view of an air preheating structure provided in a coke oven according to the present invention.
Fig. 2 is a rotated view a-a in fig. 1.
In the figure: 1. coke oven branch flue 2, air duct 3, basement pipeline system 4, air duct inlet pipeline 5, preheated air outlet pipeline 6, heat exchange structure
Detailed Description
The following further describes embodiments of the present invention with reference to the accompanying drawings:
as shown in fig. 1 and fig. 2, the air preheating structure provided in the coke oven according to the present invention includes an air duct 2; the air channel 2 and the coke oven sub-flue 1 are arranged side by side; an air inlet is arranged at one end of the air channel 2 close to the coke oven chimney and is connected with one end of an air channel inlet pipeline 4, the other end of the air channel inlet pipeline 4 extends to the upper part of the ground, and the air inlet of the air channel inlet pipeline 4 is communicated with the atmosphere; the other end of the air channel 2 is provided with a preheated air outlet which is connected with a preheated air outlet pipeline 5.
The air channel 2 and the coke oven sub-flue 1 are integrally built and formed when the coke oven body is built.
The top of the air channel 2 is flush with the top of the coke oven sub-flue 1, the part of the air channel 2 above the elevation of the coke oven basement is between the pipeline system at the corresponding side of the coke oven and the coke oven sub-flue 1, and the part of the air channel 2 below the elevation of the coke oven basement extends to the lower part of the pipeline system at the corresponding side of the coke oven.
A multilayer heat exchange structure 6 is arranged in the air channel 2 along the height direction; each layer of heat exchange structure 6 consists of a plurality of heat exchange fins and a cross brace, the two ends of the cross brace are fixedly connected with the side walls at the two sides of the air channel 2 respectively, and the cross brace is longitudinally provided with a plurality of heat exchange fins.
The cross braces and the heat exchange fins are all steel components.
The air inlet of the air channel inlet pipeline 4 is horizontally arranged, and a grate is arranged at the air inlet.
And a preheated air outlet of the preheated air outlet pipeline 5 is connected with a coal tower hopper nozzle and a heat preservation gas inlet of a discharging device or connected with an air suction inlet of a dry quenching gas circulating system, and a fan is arranged on the preheated air outlet pipeline 5.
The fan and the preheated air outlet pipeline 5 are provided with heat insulation structures; the preheated air outlet pipeline 5 is provided with a gas regulating valve, a compensator, a flowmeter, a temperature measuring device and a pressure measuring device.
The design and the working principle of the air preheating structure arranged in the coke oven are as follows:
an air channel is arranged on one side of the coke oven smoke-dividing channel close to the basement of the coke oven, and the part of the air channel above the ground has a small width due to space limitation, thereby not only playing a role in heat exchange, but also playing a role in heat insulation and reducing the temperature of the side wall of the flue of the basement; the section area of the part of the air channel under the ground is larger, the air flow resistance can be reduced, and in order to increase the heat exchange efficiency, a heat exchange device can be arranged in the air channel to increase the heat exchange area. The air inlet of the air channel is arranged at one end close to the coke oven chimney to suck air with higher temperature, and the preheated air outlet of the air channel is arranged at one end far away from the coke oven chimney. The flowing direction of the air in the air channel is opposite to the flowing direction of the waste gas in the coke oven sub-flue, the countercurrent heat exchange is carried out, and the air in the air channel generates flowing power through the fan.
The preheated air heated by the air channel is sent to a coal tower hopper nozzle and a discharge device by a fan through a preheated air outlet pipeline or is sent to an air suction inlet of a dry quenching gas circulation system. The fan and the air channel outlet pipeline need to be subjected to heat preservation treatment, and necessary processes and instrument equipment such as an adjusting valve, a compensator, a flowmeter, a temperature measuring device, a pressure measuring device and the like are arranged on the air channel outlet pipeline.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and the technical solutions and the inventive concepts thereof according to the present invention should be equivalent or changed within the scope of the present invention.

Claims (8)

1. An air preheating structure arranged in a coke oven is characterized by comprising an air channel; the air channel and the coke oven branch flue are arranged side by side; an air inlet is arranged at one end of the air channel close to the coke oven chimney and is connected with one end of an air channel inlet pipeline, the other end of the air channel inlet pipeline extends to the upper part of the ground, and the air inlet of the air channel inlet pipeline is communicated with the atmosphere; the other end of the air channel is provided with a preheated air outlet which is connected with a preheated air outlet pipeline.
2. The air preheating structure in the coke oven according to claim 1, wherein the air duct is integrally formed with the flue of the coke oven when the coke oven body is constructed.
3. The air preheating structure in the coke oven according to claim 1, wherein the top of the air duct is flush with the top of the branch flue of the coke oven, the portion of the air duct above the level of the basement of the coke oven is between the corresponding side piping system of the coke oven and the branch flue of the coke oven, and the portion of the air duct below the level of the basement of the coke oven extends to the lower portion of the corresponding side piping system of the coke oven.
4. The air preheating structure in the coke oven according to claim 1, 2 or 3, wherein a plurality of layers of heat exchange structures are arranged in the air passage along the height direction; each layer of heat exchange structure consists of a plurality of heat exchange fins and a cross brace, the two ends of the cross brace are fixedly connected with the side walls of the two sides of the air channel respectively, and the plurality of heat exchange fins are longitudinally arranged on the upper edge of the cross brace.
5. The air preheating structure in a coke oven according to claim 4, wherein the cross-brace and the heat exchange fin are both steel members.
6. The air preheating structure in a coke oven according to claim 1, wherein the air inlet of the air duct inlet duct is horizontally disposed, and a grate is disposed at the air inlet.
7. The air preheating structure in the coke oven as claimed in claim 1, wherein the preheated air outlet of the preheated air outlet pipeline is connected with the coal tower nozzle and the heat preservation gas inlet of the emptying device, or connected with the air suction inlet of the dry quenching gas circulation system, and the preheated air outlet pipeline is provided with a fan.
8. The air preheating structure in the coke oven according to claim 7, wherein the blower and the preheated air outlet pipeline are provided with a heat insulation structure; the preheated air outlet pipeline is provided with a gas regulating valve, a compensator, a flowmeter, a temperature measuring device and a pressure measuring device.
CN202110336133.6A 2021-03-29 2021-03-29 Air preheating structure arranged in coke oven Pending CN113025350A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110336133.6A CN113025350A (en) 2021-03-29 2021-03-29 Air preheating structure arranged in coke oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110336133.6A CN113025350A (en) 2021-03-29 2021-03-29 Air preheating structure arranged in coke oven

Publications (1)

Publication Number Publication Date
CN113025350A true CN113025350A (en) 2021-06-25

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN205048470U (en) * 2015-08-04 2016-02-24 山东阳光天润化工设备有限公司 Flue gas processing system
CN214781638U (en) * 2021-03-29 2021-11-19 中冶焦耐(大连)工程技术有限公司 Air preheating structure arranged in coke oven

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN205048470U (en) * 2015-08-04 2016-02-24 山东阳光天润化工设备有限公司 Flue gas processing system
CN214781638U (en) * 2021-03-29 2021-11-19 中冶焦耐(大连)工程技术有限公司 Air preheating structure arranged in coke oven

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