[go: up one dir, main page]

CN115751318A - Gas heating device and method - Google Patents

Gas heating device and method Download PDF

Info

Publication number
CN115751318A
CN115751318A CN202211502195.0A CN202211502195A CN115751318A CN 115751318 A CN115751318 A CN 115751318A CN 202211502195 A CN202211502195 A CN 202211502195A CN 115751318 A CN115751318 A CN 115751318A
Authority
CN
China
Prior art keywords
valve
pipeline
furnace
gas
delivery
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
CN202211502195.0A
Other languages
Chinese (zh)
Inventor
魏翠萍
朱进峰
殷欢
欧阳龙
张开钧
刘颖辉
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.)
Sinosteel Equipment and Engineering Co Ltd
Original Assignee
Sinosteel Equipment and Engineering Co Ltd
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 Sinosteel Equipment and Engineering Co Ltd filed Critical Sinosteel Equipment and Engineering Co Ltd
Priority to CN202211502195.0A priority Critical patent/CN115751318A/en
Publication of CN115751318A publication Critical patent/CN115751318A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • 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

Landscapes

  • Air Supply (AREA)

Abstract

本发明公开了一种煤气加热装置及方法,其中煤气加热装置包括蓄热式加热炉、换热机构、烧炉煤气输送机构、助燃空气输送机构、烟气输送机构,烧炉煤气输送机构、助燃空气输送机构和烟气输送机构均与蓄热式加热炉相连通,且烧炉煤气输送机构、助燃空气输送机构和烟气输送机构均并联;烧炉煤气输送机构用于将烧炉煤气输送至蓄热式加热炉内,助燃空气输送机构用于将助燃空气输送至蓄热式加热炉内,烟气输送机构用于将蓄热式加热炉内流出的烟气输出;换热机构串联在烧炉煤气输送机构、助燃空气输送机构和烟气输送机构上,换热机构能够将烟气的温度降低,且换热机构将烧炉煤气和助燃空气的温度升高。如此设置,可以大大提高蓄热式加热炉的燃烧效率。

Figure 202211502195

The invention discloses a gas heating device and method, wherein the gas heating device includes a heat storage type heating furnace, a heat exchange mechanism, a furnace gas conveying mechanism, a combustion-supporting air conveying mechanism, a flue gas conveying mechanism, a furnace gas conveying mechanism, a combustion-supporting Both the air conveying mechanism and the flue gas conveying mechanism are connected with the regenerative heating furnace, and the furnace gas conveying mechanism, the combustion air conveying mechanism and the flue gas conveying mechanism are connected in parallel; the furnace gas conveying mechanism is used to convey the furnace gas to In the regenerative heating furnace, the combustion-supporting air delivery mechanism is used to deliver the combustion-supporting air to the regenerative heating furnace, and the flue gas delivery mechanism is used to output the flue gas flowing out of the regenerative heating furnace; the heat exchange mechanism is connected in series On the furnace gas conveying mechanism, the combustion air conveying mechanism and the flue gas conveying mechanism, the heat exchange mechanism can reduce the temperature of the flue gas, and the heat exchange mechanism can raise the temperature of the furnace gas and the combustion air. Such setting can greatly improve the combustion efficiency of the regenerative heating furnace.

Figure 202211502195

Description

一种煤气加热装置及方法Gas heating device and method

技术领域technical field

本发明涉及煤气加热技术领域,特别涉及一种煤气加热装置及方法。The invention relates to the technical field of gas heating, in particular to a gas heating device and method.

背景技术Background technique

当前,一般通过换热器式加热炉对高压强爆炸性煤气进行加热,但是通过上述加热炉进行加热,煤气的温度一般只能达到200℃左右,不能满足生产需求,因此,部分企业开始尝试采用蓄热式加热炉对高压强爆炸性煤气进行加热,但是,在采用蓄热式加热炉对高压强爆炸性煤气进行加热时,通常是将高压强爆炸性煤气直接通入加热炉内,从而导致加热炉的加热效率降低。At present, high-pressure and highly explosive gas is generally heated through a heat exchanger type heating furnace, but the temperature of the gas can only reach about 200°C when heated by the above-mentioned heating furnace, which cannot meet the production needs. Therefore, some enterprises have begun to try to use storage The thermal heating furnace heats the high-pressure and explosive gas, but when the regenerative heating furnace is used to heat the high-pressure and explosive gas, the high-pressure and explosive gas is usually directly passed into the heating furnace, resulting in the heating of the heating furnace. Reduced efficiency.

因此,如何能够有效提高加热炉的燃烧效率是本领域技术人员亟需解决的技术问题。Therefore, how to effectively improve the combustion efficiency of the heating furnace is a technical problem urgently needed to be solved by those skilled in the art.

发明内容Contents of the invention

有鉴于此,本发明的目的在于提供一种煤气加热装置,能够有效提高加热炉的加热效率。In view of this, the object of the present invention is to provide a gas heating device, which can effectively improve the heating efficiency of the heating furnace.

本发明的另一目的还在于提供一种煤气加热方法。Another object of the present invention is to provide a gas heating method.

为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:

一种煤气加热装置,包括蓄热式加热炉、换热机构、烧炉煤气输送机构、助燃空气输送机构、烟气输送机构,所述烧炉煤气输送机构、所述助燃空气输送机构和所述烟气输送机构均与所述蓄热式加热炉相连通,且所述烧炉煤气输送机构、所述助燃空气输送机构和所述烟气输送机构均并联;A gas heating device, comprising a regenerative heating furnace, a heat exchange mechanism, a furnace gas delivery mechanism, a combustion air delivery mechanism, a flue gas delivery mechanism, the furnace gas delivery mechanism, the combustion air delivery mechanism and the The flue gas conveying mechanism is connected with the regenerative heating furnace, and the furnace gas conveying mechanism, the combustion air conveying mechanism and the flue gas conveying mechanism are connected in parallel;

所述烧炉煤气输送机构用于将烧炉煤气输送至所述蓄热式加热炉内,所述助燃空气输送机构用于将助燃空气输送至所述蓄热式加热炉内,所述烟气输送机构用于将所述蓄热式加热炉内流出的烟气输出;The furnace gas conveying mechanism is used to convey the furnace gas to the regenerative heating furnace, the combustion-supporting air conveying mechanism is used to convey the combustion-supporting air to the regenerative heating furnace, and the flue gas The conveying mechanism is used to output the flue gas flowing out of the regenerative heating furnace;

所述换热机构串联在所述烧炉煤气输送机构、所述助燃空气输送机构和所述烟气输送机构上,所述换热机构能够将所述烟气的温度降低,且所述换热机构将所述烧炉煤气和所述助燃空气的温度升高。The heat exchange mechanism is connected in series to the furnace gas delivery mechanism, the combustion air delivery mechanism and the flue gas delivery mechanism, the heat exchange mechanism can reduce the temperature of the flue gas, and the heat exchange A mechanism increases the temperature of the furnace gas and the combustion air.

优选的,还包括高压强爆炸性低温煤气输送机构和高压强爆炸性高温煤气输送机构,所述高压强爆炸性低温煤气输送机构和所述高压强爆炸性高温煤气输送机构均与所述蓄热式加热炉相连通;Preferably, it also includes a high-pressure, high-explosive, low-temperature gas delivery mechanism and a high-pressure, high-explosive, high-temperature gas delivery mechanism, both of which are connected to the regenerative heating furnace Pass;

所述高压强爆炸性低温煤气输送机构用于将高压强爆炸性低温煤气输送至所述蓄热式加热炉内,所述高压强爆炸性高温煤气输送机构用于将所述蓄热式加热内的高压强爆炸性高温煤气输出。The high-pressure explosive low-temperature gas delivery mechanism is used to deliver the high-pressure explosive low-temperature gas to the regenerative heating furnace, and the high-pressure explosive high-temperature gas delivery mechanism is used to transport the high-pressure explosive low-temperature gas inside the regenerative heating furnace. Explosive hot gas output.

优选的,所述烧炉煤气输送机构包括烧炉煤气输送总管路,烧炉煤气输送支管路、第一双闸板闸阀、第一切断阀和第一调节阀,所述烧炉煤气输送总管路的一端与烧炉煤气相连通,所述烧炉煤气输送总管路的另一端与所述烧炉煤气输送支管路的一端相连通,所述烧炉煤气输送支管路的另一端与所述蓄热式加热炉相连通,所述第一双闸板闸阀、所述第一切断阀和所述第一调节阀均设置于所述烧炉煤气输送支管路上。Preferably, the furnace gas conveying mechanism includes a main furnace gas conveying pipeline, a furnace gas conveying branch pipeline, a first double gate valve, a first shut-off valve and a first regulating valve, and the furnace gas conveying main pipeline One end of the furnace gas is connected with the furnace gas, the other end of the furnace gas delivery main pipeline is connected with one end of the furnace gas delivery branch pipeline, and the other end of the furnace gas delivery branch pipeline is connected with the heat storage The heating furnace is connected to each other, and the first double gate valve, the first cut-off valve and the first regulating valve are all arranged on the branch pipeline for conveying the furnace gas.

优选的,所述烧炉煤气输送机构还包括第一氮气保护组件和第一放散组件;Preferably, the furnace gas delivery mechanism further includes a first nitrogen protection component and a first release component;

所述第一氮气保护组件包括第一氮气输送管路和第一氮气吹扫阀,所述第一氮气输送管路设置于所述第一双闸板闸阀和所述第一切断阀之间,且与所述烧炉煤气输送管路相连通,所述第一氮气吹扫阀设置于所述第一氮气输送管路上;The first nitrogen protection component includes a first nitrogen delivery pipeline and a first nitrogen purge valve, and the first nitrogen delivery pipeline is arranged between the first double gate valve and the first cut-off valve, And communicated with the furnace gas delivery pipeline, the first nitrogen purge valve is set on the first nitrogen delivery pipeline;

所述第一放散组件包括第一放散管路和第一放散阀,所述第一放散管路设置于所述第一双闸板闸阀和所述第一切断阀之间,且与所述烧炉煤气输送管路相连通,所述第一放散阀设置于所述第一放散管路上。The first relief assembly includes a first relief pipeline and a first relief valve, and the first relief pipeline is arranged between the first double gate valve and the first shut-off valve, and is connected to the burner The furnace gas delivery pipeline is connected, and the first relief valve is arranged on the first relief pipeline.

优选的,所述助燃空气输送机构包括助燃空气输送总管路、助燃空气输送支管路、第二双闸板闸阀、第二切断阀和第二调节阀,所述助燃空气输送总管路的一端与助燃空气相连通,所述助燃空气输送总管路的另一端与所述助燃空气支管路相连通,所述助燃空气输送支管路的另一端与所述蓄热式加热炉相连通,所述第二双闸板闸阀、所述第二切断阀和所述第二调节阀均设置于所述助燃空气输送支管路上。Preferably, the combustion-supporting air delivery mechanism includes a main combustion-supporting air delivery pipeline, a combustion-supporting air delivery branch pipeline, a second double gate valve, a second cut-off valve and a second regulating valve, one end of the combustion-supporting air delivery main pipeline is connected to the The other end of the combustion-supporting air delivery main pipeline is connected with the combustion-supporting air branch pipeline, the other end of the combustion-supporting air delivery branch pipeline is connected with the regenerative heating furnace, and the second double The gate valve, the second cut-off valve and the second regulating valve are all arranged on the branch pipeline for conveying combustion-supporting air.

优选的,所述助燃空气输送机构还包括第二氮气保护组件,第二放散组件和氧气输送组件;Preferably, the combustion air delivery mechanism further includes a second nitrogen protection component, a second release component and an oxygen delivery component;

所述第二氮气保护组件包括第二氮气输送管路和第二氮气吹扫阀,所述第二氮气输送管路设置于所述第二双闸板闸阀和所述第二切断阀之间,且与所述助燃空气输送支管路相连通,所述第二氮气吹扫阀设置于所述第二氮气输送管路上;The second nitrogen protection component includes a second nitrogen delivery pipeline and a second nitrogen purge valve, and the second nitrogen delivery pipeline is arranged between the second double gate valve and the second cut-off valve, And communicated with the combustion-supporting air delivery branch pipeline, the second nitrogen purge valve is arranged on the second nitrogen delivery pipeline;

所述第二放散组件包括第二放散管路和第二放散阀,所述第二散管路设置于所述第一双闸板闸阀和所述第一切断阀之间,且与所述助燃空气输送管路相连通,所述第二放散阀设置于所述第二放散管路上;The second release assembly includes a second release line and a second release valve, the second release line is arranged between the first double gate valve and the first cut-off valve, and is connected to the combustion-supporting The air delivery pipelines are connected, and the second release valve is arranged on the second release pipeline;

所述氧气输送组件包括氧气输送管路和氧气调节阀,所述氧气调节阀设置于所述氧气输送路上,所述氧气输送管路与所述助燃空气输送支管路相连通,且所述氧气输送管路设置于所述换热机构与所述第二调节阀之间。The oxygen delivery assembly includes an oxygen delivery pipeline and an oxygen regulating valve, the oxygen regulating valve is arranged on the oxygen delivery path, the oxygen delivery pipeline communicates with the combustion air delivery branch pipeline, and the oxygen delivery The pipeline is arranged between the heat exchange mechanism and the second regulating valve.

优选的,所述烟气输送机构包括烟气输送总管路、烟气输送支管路和第三双闸板闸阀,所述烟气输送总管路的一端与外界大气相连通,所述烟气输送总管路的另一端与所述烟气输送支管路相连通,所述烟气输送支管路的另一端与所述蓄热式加热炉相连通,所述第三双闸板闸阀设置于所述烟气输送支管路上。Preferably, the flue gas conveying mechanism includes a flue gas conveying main pipeline, a flue gas conveying branch pipeline and a third double gate valve, one end of the flue gas conveying main pipeline communicates with the outside atmosphere, and the flue gas conveying main pipe The other end of the pipeline is connected with the flue gas conveying branch pipeline, the other end of the flue gas conveying branch pipeline is connected with the regenerative heating furnace, and the third double gate valve is arranged on the flue gas On the delivery branch pipeline.

优选的,所述烟气输送机构还包括废气缓冲输出组件,所述废气缓冲罐输出组件包括废气输送管路、废气阀、废气调节阀和缓冲罐,所述废气阀和所述废气调节阀均设置于所述废气输送管路上,所述废气输送管路的一端与所述烟气输送支管路相连通,所述废气输送管路的另一端与所述缓冲罐相连通。Preferably, the flue gas conveying mechanism further includes an exhaust gas buffer output assembly, and the exhaust gas buffer tank output assembly includes an exhaust gas delivery pipeline, an exhaust gas valve, an exhaust gas regulating valve and a buffer tank, and the exhaust gas valve and the exhaust gas regulating valve are both It is arranged on the exhaust gas delivery pipeline, one end of the exhaust gas delivery pipeline communicates with the flue gas delivery branch pipeline, and the other end of the exhaust gas delivery pipeline communicates with the buffer tank.

优选的,所述烟气输送机构还包括废气回收组件,所述废气回收组件包括废气输送管路、废气阀、废气调节阀和回收罐,所述废气阀和所述废气调节阀均设置于所述废气输送管路上,所述废气输送管路的一端与所述烟气输送支管路相连通,所述废气输送管路的另一端与所述回收罐相连通。Preferably, the flue gas delivery mechanism further includes an exhaust gas recovery assembly, the exhaust gas recovery assembly includes an exhaust gas delivery pipeline, an exhaust gas valve, an exhaust gas regulating valve and a recovery tank, and the exhaust gas valve and the exhaust gas regulating valve are both arranged on the On the exhaust gas delivery pipeline, one end of the exhaust gas delivery pipeline communicates with the flue gas delivery branch pipeline, and the other end of the exhaust gas delivery pipeline communicates with the recovery tank.

优选的,所述高压强爆炸性低温煤气输送机构包括高压强爆炸性低温煤气输送管路、第四双闸板闸阀和第三切断阀,所述第四双闸板闸阀和第三切断阀均设置于所述高压强爆炸性低温煤气输送管路上,所述高压强爆炸性低温煤气输送管路的一端与高压强爆炸性低温煤气相连通,所述高压强爆炸性低温煤气输送管路的另一端与所述蓄热式加热炉相连通。Preferably, the high-pressure strong explosive low-temperature gas delivery mechanism includes a high-pressure strong explosive low-temperature gas delivery pipeline, a fourth double-ram gate valve and a third shut-off valve, and the fourth double-ram gate valve and the third shut-off valve are both arranged at On the high-pressure, explosive, low-temperature gas delivery pipeline, one end of the high-pressure, explosive, low-temperature gas delivery pipeline communicates with the high-pressure, explosive, low-temperature gas delivery pipeline, and the other end of the high-pressure, explosive, low-temperature gas delivery pipeline communicates with the heat storage connected to the heating furnace.

优选的,所述高压强爆炸性低温煤气输送机构还包括第三氮气保护组件、均压组件和蒸汽输送组件;Preferably, the high-pressure, explosive, low-temperature gas delivery mechanism also includes a third nitrogen protection component, a pressure equalization component, and a steam delivery component;

所述第三氮气保护组件包括第三氮气吹扫管路,和设置于所述氮气吹扫管路上的第三氮气吹扫阀,所述第三氮气吹扫管路设置于所述第四双闸板闸阀和第三切断阀,且所述第三氮气吹扫管路与所述高压强爆炸性低温煤气输送管路相连通;The third nitrogen protection component includes a third nitrogen purge pipeline, and a third nitrogen purge valve arranged on the nitrogen purge pipeline, and the third nitrogen purge pipeline is set on the fourth double A gate valve and a third shut-off valve, and the third nitrogen purge pipeline communicates with the high-pressure, high-explosive, low-temperature gas delivery pipeline;

所述均压组件包括均压管路和均压阀,所述均压阀设于所述均压管路上,所述均压管路的两端分别设置于所述第四双闸板闸阀的两侧;The pressure equalization assembly includes a pressure equalization pipeline and a pressure equalization valve, the pressure equalization valve is arranged on the pressure equalization pipeline, and the two ends of the pressure equalization pipeline are respectively arranged on the ends of the fourth double gate valve. both sides;

所述蒸汽输送组件包括蒸汽输送管路和蒸汽调节阀,所述蒸汽调节阀设置于所述蒸汽输送管路上,所述蒸汽输送管路与所述高压强爆炸性低温煤气管路相连通。The steam conveying assembly includes a steam conveying pipeline and a steam regulating valve, the steam regulating valve is arranged on the steam conveying pipeline, and the steam conveying pipeline communicates with the high-pressure, high-explosive, low-temperature gas pipeline.

优选的,所述高压强爆炸性高温煤气输送机构包括所述高压强爆炸性高温煤气输送管路和高压强爆炸性高温煤气阀,所述高压强爆炸性高温煤气阀设置于所述高压强爆炸性高温煤气输送管路上,所述高压强爆炸性高温煤气输送管路的一端与高压强爆炸性高温煤气相连通,所述高压强爆炸性高温煤气输送管路的另一端与所述蓄热式加热炉相连通。Preferably, the high-pressure explosive high-temperature gas delivery mechanism includes the high-pressure explosive high-temperature gas delivery pipeline and a high-pressure explosive high-temperature gas valve, and the high-pressure explosive high-temperature gas valve is arranged on the high-pressure explosive high-temperature gas delivery pipe On the road, one end of the high-pressure and explosive high-temperature gas delivery pipeline is connected to the high-pressure and explosive high-temperature gas, and the other end of the high-pressure and explosive high-temperature gas delivery pipeline is connected to the regenerative heating furnace.

优选的,所述换热机构包括第一换热器和第二换热器,所述第一换热器串联于所述烧炉煤气输送总管路与所述烟气输送总管路上,所述第二换热器串联于所述助燃空气输送总管路与所述烟气输送总管路上。Preferably, the heat exchange mechanism includes a first heat exchanger and a second heat exchanger, the first heat exchanger is connected in series to the main pipeline for conveying the furnace gas and the main pipeline for conveying the flue gas, and the first heat exchanger is Two heat exchangers are connected in series on the main combustion air delivery pipeline and the flue gas delivery main pipeline.

优选的,所述蓄热式加热炉为2-4座。Preferably, there are 2-4 regenerative heating furnaces.

一种煤气加热方法,应用于如上述任意一项所述的煤气加热装置中,包括闷炉转烧炉模式、烧炉转闷炉模式、闷炉转送风模式和送风转闷炉模式,所述闷炉转烧炉模式、所述烧炉转闷炉模式、所述闷炉转送风模式和所述送风转闷炉模式之间能够相互切换;A coal gas heating method, which is applied to the gas heating device described in any one of the above, including the mode of converting the furnace to the furnace, the mode of burning the furnace to the furnace, the mode of the furnace to the air supply, and the mode of the air supply to the furnace, The furnace-to-steel furnace mode, the furnace-to-steel furnace mode, the furnace-to-air mode, and the air-to-steel furnace mode can be switched;

所述闷炉转烧炉模式为:The mode of the smoldering furnace-to-sintering furnace is:

S100:开启废气调节阀,开启废气阀,使得蓄热式加热炉内的高压强爆炸性高温煤气放散,直至所述蓄热式加热炉内的压力达到预设压力值;S100: Open the waste gas regulating valve, open the waste gas valve, so that the high-pressure strong explosive high-temperature gas in the regenerative heating furnace is released until the pressure in the regenerative heating furnace reaches a preset pressure value;

S200:关闭第一氮气吹扫阀,开启第一放散阀,将所述蓄热式加热炉内的压力进行卸载;S200: closing the first nitrogen purge valve, opening the first relief valve, and unloading the pressure in the regenerative heating furnace;

S300:开启烧炉煤气输送支管路上的第一双闸板闸阀,保持第一切断阀关闭,开启第一氮气吹扫阀,对所述蓄热式加热炉内的高压强爆炸性高温煤气吹扫置换,直至所述烟气输送支管路内的一氧化碳含量达标,放散完成;S300: Open the first double gate valve on the furnace gas delivery branch pipeline, keep the first cut-off valve closed, open the first nitrogen purge valve, and purge and replace the high-pressure, explosive, and high-temperature gas in the regenerative heating furnace , until the carbon monoxide content in the flue gas conveying branch pipeline reaches the standard, and the emission is completed;

S400:开启烧炉煤气输送支管路第一双闸板闸阀,开启第一切断阀,开启第一调节阀,关闭第一氮气吹扫阀,关闭第一放散阀,同时开启助燃空气支管路上的第二双闸板闸阀,开启第二切断阀,开启第二调节阀,关闭第二氮气吹扫阀,关闭第二放散阀,使得烧炉煤气通过第一换热器进入蓄热式加热炉,使得助燃空气通过第二换热器进入蓄热式加热炉,使得所述蓄热式加热炉进入燃烧状态;S400: Open the first double gate valve of the furnace gas delivery branch pipeline, open the first cut-off valve, open the first regulating valve, close the first nitrogen purge valve, close the first relief valve, and open the first combustion air branch pipeline at the same time Two double gate valves, open the second cut-off valve, open the second regulating valve, close the second nitrogen purge valve, close the second relief valve, so that the furnace gas enters the regenerative heating furnace through the first heat exchanger, so that Combustion-supporting air enters the regenerative heating furnace through the second heat exchanger, so that the regenerative heating furnace enters a combustion state;

所述烧炉转闷炉模式为:The mode of turning the furnace into a furnace is as follows:

关闭第一调节阀、关闭第一切断阀,关闭第二调节阀,关闭第二切断阀,保持第一双闸板闸阀开启,保持第二双闸板闸阀开启,开启第一氮气吹扫阀,开启第二氮气吹扫阀,对所述烧炉煤气输送支管路和所述助燃空气支管路进行吹扫,同时开启第四氮气吹扫阀和第五氮气吹扫阀,当第一预设时间后,所述关闭第一双闸板闸板和所述第二双闸板闸阀,当第二预设时间后,关闭烧炉煤气输送支管路第一氮气吹扫阀,开启第一放散阀;关闭助燃空气支管路第二氮气吹扫阀,开启第二放散阀,同时关闭烟气输送支管路上的双闸板闸阀,所述蓄热式加热炉由烧炉转为闷炉;Close the first regulating valve, close the first shut-off valve, close the second regulating valve, close the second shut-off valve, keep the first double gate valve open, keep the second double gate valve open, open the first nitrogen purge valve, Open the second nitrogen purge valve to purge the furnace gas delivery branch pipeline and the combustion air branch pipeline, and open the fourth nitrogen purge valve and the fifth nitrogen purge valve at the same time, when the first preset time Afterwards, the first double gate gate valve and the second double gate gate valve are closed, and after the second preset time, the first nitrogen purge valve of the furnace gas delivery branch pipeline is closed, and the first relief valve is opened; Close the second nitrogen purge valve of the combustion-supporting air branch pipeline, open the second relief valve, and close the double gate valve on the flue gas delivery branch pipeline at the same time, and the regenerative heating furnace is converted from a burning furnace to a stuffy furnace;

所述闷炉转送风工作模式为:The working mode of the stuffy furnace transfer air supply is:

开启第三切断阀,开启第三氮气吹扫阀,对高压强爆炸性低温煤气输送管路进行氮气吹扫,吹扫完毕后,关闭第三氮气吹扫阀;Open the third cut-off valve, open the third nitrogen purge valve, and carry out nitrogen purge on the high-pressure strong explosive low-temperature gas delivery pipeline. After the purge is completed, close the third nitrogen purge valve;

开启均压阀,当所述蓄热式加热炉内的压力达到预设压力值时,关闭均压阀,开启第四双闸板闸阀,将高压强爆炸性高温煤气输送管路送入所述蓄热式加热炉内。Open the pressure equalizing valve, when the pressure in the regenerative heating furnace reaches the preset pressure value, close the pressure equalizing valve, open the fourth double gate valve, and send the high-pressure, explosive and high-temperature gas pipeline into the storage In the heating furnace.

所述送风转闷炉的工作模式为:The working mode of described air-supply rotary furnace is:

关闭高压强爆炸性高温煤气阀,第四双闸板闸阀和第三切断阀,开启第三氮气吹扫阀,所述蓄热式加热炉由送风转为闷炉模式。Close the high-pressure strong explosive high-temperature gas valve, the fourth double gate valve and the third cut-off valve, open the third nitrogen purge valve, and the regenerative heating furnace changes from air supply to stuffy furnace mode.

所述送风转闷炉的工作模式为:The working mode of described air-supply rotary furnace is:

关闭高压强爆炸性高温煤气阀,第四双闸板闸阀和第三切断阀,开启第三氮气吹扫阀,所述蓄热式加热炉由送风转为闷炉模式。Close the high-pressure strong explosive high-temperature gas valve, the fourth double gate valve and the third cut-off valve, open the third nitrogen purge valve, and the regenerative heating furnace changes from air supply to stuffy furnace mode.

由以上技术方案可以看出,和现有技术相比,本发明实施例所公开的煤气加热装置中设置了换热机构,换热机构可以将进入蓄热式加热炉内的烧炉煤气与从蓄热式加热炉内的流出的烟气进行换热,同时换热机构还可以将进入蓄热式加热炉内的助燃空气与从蓄热式加热炉内流出的烟气进行换热,如此设置,可以使得进入蓄热式加热炉内的烧炉煤气与助燃空气能够首先通过换热机构将温度升高后再进入蓄热式加热炉,如此设置,可以大大提高蓄热式加热炉的加热效率,同时也可以降低排到外界大气中的烟气的温度,从而进一步降低了环境污染。It can be seen from the above technical solutions that, compared with the prior art, the gas heating device disclosed in the embodiment of the present invention is provided with a heat exchange mechanism, which can convert the furnace gas entering the regenerative heating furnace from the The flue gas flowing out of the regenerative heating furnace performs heat exchange, and the heat exchange mechanism can also exchange heat between the combustion air entering the regenerative heating furnace and the flue gas flowing out of the regenerative heating furnace, so set , so that the furnace gas and combustion-supporting air entering the regenerative heating furnace can first increase the temperature through the heat exchange mechanism and then enter the regenerative heating furnace. This setting can greatly improve the heating efficiency of the regenerative heating furnace , At the same time, it can also reduce the temperature of the flue gas discharged into the outside atmosphere, thereby further reducing environmental pollution.

附图说明Description of drawings

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见的,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following briefly introduces the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only It is an embodiment of the present invention, and those skilled in the art can also obtain other drawings according to the provided drawings without creative work.

图1为本发明第一实施例所公开的煤气加热装置的结构示意图;Fig. 1 is a schematic structural view of a gas heating device disclosed in the first embodiment of the present invention;

图2为本发明第二实施例所公开的煤气加热装置的结构示意图。Fig. 2 is a schematic structural view of the gas heating device disclosed in the second embodiment of the present invention.

其中,各部件名称如下:Among them, the names of the components are as follows:

100-蓄热式加热炉;200-烧炉煤气输送总管路;201-烧炉煤气输送支管路;2011-第一双闸板闸阀;2012-第一切断阀;2013-第一调节阀;202-第一氮气输送管路;2021-第一氮气吹扫阀;203-第一放散管路;2031-第一放散阀;300-助燃空气输送总管路;301-助燃空气输送支管路;3011-第二双闸板闸阀;3012-第二切断阀;3013-第二调节阀;302-第二氮气输送管路;3021-第二氮气吹扫阀;303-氧气输送管路;3031-氧气调节阀;304-第二放散管路;3041-第二放散阀;400-烟气输送总管路;401-烟气输送支管路;4011-第三双闸板闸阀;500-高压强爆炸性低温煤气输送管路;501-第四双闸板闸阀;502-第三切断阀;503-第三氮气吹扫管路;5031-第三氮气吹扫阀;504-均压管路;5041-均压阀;505-蒸汽输送管路;5051-蒸汽调节阀;600-高压强爆炸性高温煤气输送管路;601-高压强爆炸性高温煤气阀;700-废气输送管路;701-废气阀;702-废气调节阀;703-缓冲罐,704-回收罐;800-第四氮气吹扫管路;801-第四氮气吹扫阀;802-第五氮气吹扫阀;803-第六氮气吹扫阀;900-第一换热器;1000-第二换热器。100-regenerative heating furnace; 200-the main pipeline for burning furnace gas; 201-the branch pipeline for burning furnace gas; 2011-the first double gate valve; 2012-the first shut-off valve; 2013-the first regulating valve; 202 -The first nitrogen delivery pipeline; 2021-the first nitrogen purge valve; 203-the first release pipeline; 2031-the first release valve; 300-combustion air delivery main pipeline; 301-combustion air delivery branch pipeline; 3011- The second double gate valve; 3012-the second cut-off valve; 3013-the second regulating valve; 302-the second nitrogen delivery pipeline; 3021-the second nitrogen purge valve; 303-oxygen delivery pipeline; 3031-oxygen adjustment Valve; 304-the second release pipeline; 3041-the second release valve; 400-the main pipeline for flue gas transmission; 401-the branch pipeline for flue gas transmission; 4011-the third double gate valve; Pipeline; 501-the fourth double gate valve; 502-the third cut-off valve; 503-the third nitrogen purge pipeline; 5031-the third nitrogen purge valve; 504-pressure equalization pipeline; 5041-pressure equalization valve ;505-steam delivery pipeline; 5051-steam regulating valve; 600-high pressure strong explosive high temperature gas delivery pipeline; 601-high pressure strong explosive high temperature gas valve; 700-exhaust gas delivery pipeline; 701-exhaust gas valve; 702-exhaust gas regulation Valve; 703-buffer tank, 704-recovery tank; 800-fourth nitrogen purge pipeline; 801-fourth nitrogen purge valve; 802-fifth nitrogen purge valve; 803-sixth nitrogen purge valve; 900 - first heat exchanger; 1000 - second heat exchanger.

具体实施方式Detailed ways

有鉴于此,本发明的核心在于提供一种煤气加热装置,能够有效提高加热炉的燃烧效率。In view of this, the core of the present invention is to provide a gas heating device, which can effectively improve the combustion efficiency of the heating furnace.

本发明的另一核心还在于提供一种煤气加热方法。Another core of the present invention is to provide a gas heating method.

为了使本技术领域的人员更好地理解本发明方案,下面接合附图和具体实施方式对本发明作进一步的详细说明,请参考图1至图2。In order to enable those skilled in the art to better understand the solution of the present invention, the present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments, please refer to FIG. 1 to FIG. 2 .

本发明实施例所公开的煤气加热装置,包括蓄热式加热炉100、换热机构、烧炉煤气输送机构、助燃空气输送机构、烟气输送机构,烧炉煤气输送机构、助燃空气输送机构和烟气输送机构均与蓄热式加热炉100相连通,且烧炉煤气输送机构、助燃空气输送机构和烟气输送机构均并联。The gas heating device disclosed in the embodiment of the present invention includes a regenerative heating furnace 100, a heat exchange mechanism, a furnace gas conveying mechanism, a combustion air conveying mechanism, a flue gas conveying mechanism, a furnace gas conveying mechanism, a combustion air conveying mechanism and The flue gas conveying mechanisms are all connected to the regenerative heating furnace 100, and the furnace gas conveying mechanism, the combustion-supporting air conveying mechanism and the flue gas conveying mechanism are all connected in parallel.

其中,烧炉煤气输送机构用于将烧炉煤气输送至蓄热式加热炉100内,助燃空气输送机构用于将助燃空气输送至蓄热式加热炉100内,烟气输送机构用于将蓄热式加热炉100内流出的烟气输出。Among them, the furnace gas conveying mechanism is used to convey the furnace gas to the regenerative heating furnace 100, the combustion-supporting air conveying mechanism is used to convey the combustion-supporting air to the regenerative heating furnace 100, and the flue gas conveying mechanism is used to transfer the The flue gas flowing out of the thermal heating furnace 100 is output.

需要说明的是,换热机构串联在烧炉煤气输送机构、助燃空气输送机构和烟气输送机构上,换热机构能够将烟气的温度降低,且换热机构将烧炉煤气和助燃空气的温度升高。It should be noted that the heat exchange mechanism is connected in series to the furnace gas conveying mechanism, the combustion air conveying mechanism and the flue gas conveying mechanism. The temperature rises.

和现有技术相比,本发明实施例所公开的煤气加热装置中设置了换热机构,换热机构可以将进入蓄热式加热炉100内的烧炉煤气与从蓄热式加热炉100内的流出的烟气进行换热,同时换热机构还可以将进入蓄热式加热炉100内的助燃空气与从蓄热式加热炉100内流出的烟气进行换热,如此设置,可以使得进入蓄热式加热炉100内的烧炉煤气与助燃空气能够首先通过换热机构将温度升高后再进入蓄热式加热炉100,如此设置,可以大大提高蓄热式加热炉100的加热效率,同时也可以降低排到外界大气中的烟气的温度,从而进一步降低了环境污染。Compared with the prior art, a heat exchange mechanism is provided in the gas heating device disclosed in the embodiment of the present invention, and the heat exchange mechanism can transfer the furnace gas entering the regenerative heating furnace 100 to the gas from the regenerative heating furnace 100 The flue gas flowing out of the regenerative heating furnace 100 is used for heat exchange. At the same time, the heat exchange mechanism can also exchange heat between the combustion air entering the regenerative heating furnace 100 and the flue gas flowing out of the regenerative heating furnace 100. The furnace gas and combustion-supporting air in the regenerative heating furnace 100 can firstly pass through the heat exchange mechanism to raise the temperature before entering the regenerative heating furnace 100. Such setting can greatly improve the heating efficiency of the regenerative heating furnace 100. At the same time, the temperature of the flue gas discharged into the outside atmosphere can also be reduced, thereby further reducing environmental pollution.

作为优选实施例,本发明实施例所公开的煤气加热装置,还包括高压强爆炸性低温煤气输送机构和高压强爆炸性高温煤气输送机构,高压强爆炸性低温煤气输送机构和高压强爆炸性高温煤气输送机构均与蓄热式加热炉100相连通。As a preferred embodiment, the gas heating device disclosed in the embodiment of the present invention also includes a high-pressure explosive low-temperature gas delivery mechanism and a high-pressure explosive high-temperature gas delivery mechanism, both of which are high-pressure explosive low-temperature gas delivery mechanisms and high-pressure explosive high-temperature gas delivery mechanisms. It communicates with the regenerative heating furnace 100 .

其中,高压强爆炸性低温煤气输送机构用于将高压强爆炸性低温煤气输送至蓄热式加热炉100内,高压强爆炸性高温煤气输送机构用于将蓄热式加热炉100内的高压强爆炸性高温煤气输出。Among them, the high-pressure strong explosive low-temperature gas delivery mechanism is used to deliver the high-pressure strong explosive low-temperature gas to the regenerative heating furnace 100, and the high-pressure strong explosive high-temperature gas delivery mechanism is used to transport the high-pressure strong explosive high-temperature gas inside the regenerative heating furnace 100 output.

本发明实施例对烧炉煤气输送机构的具体结构不进行限定,只要满足本发明使用要求的结构均在本发明的保护范围之内。The embodiment of the present invention does not limit the specific structure of the furnace gas delivery mechanism, as long as the structure meets the requirements of the present invention, it is within the protection scope of the present invention.

作为优选实施例,本发明实施例所公开的烧炉煤气输送机构包括烧炉煤气输送总管路200,烧炉煤气输送支管路201、第一双闸板闸阀2011、第一切断阀2012和第一调节阀2013,其中,烧炉煤气输送总管路200的一端与烧炉煤气相连通,烧炉煤气输送总管路200的另一端与烧炉煤气输送支管路201的一端相连通,烧炉煤气输送支管路201的另一端与蓄热式加热炉100相连通,第一双闸板闸阀2011、第一切断阀2012和第一调节阀2013均设置于烧炉煤气输送支管路201上。As a preferred embodiment, the furnace gas conveying mechanism disclosed in the embodiment of the present invention includes a furnace gas conveying main pipeline 200, a furnace gas conveying branch pipeline 201, a first double gate valve 2011, a first shut-off valve 2012 and a first Regulating valve 2013, wherein one end of the main furnace gas delivery pipeline 200 is connected with the furnace gas, the other end of the main furnace gas delivery pipeline 200 is connected with one end of the furnace gas delivery branch pipeline 201, and the furnace gas delivery branch pipe The other end of the road 201 communicates with the regenerative heating furnace 100 , and the first double gate valve 2011 , the first cut-off valve 2012 and the first regulating valve 2013 are all set on the furnace gas delivery branch pipeline 201 .

其中,第一调节阀2013用于调节烧炉煤气支管路的气体流量,当第一双闸板闸阀2011、第一切断阀2012和第一调节阀2013均开启时,烧炉煤气可以从烧炉煤气输送总管路200进入,通过烧炉煤气输送支管路201进入蓄热式加热炉100内。Among them, the first regulating valve 2013 is used to regulate the gas flow of the furnace gas branch pipeline. When the first double gate valve 2011, the first shut-off valve 2012 and the first regulating valve 2013 are all opened, the furnace gas can flow from the furnace The main gas delivery pipeline 200 enters, and enters the regenerative heating furnace 100 through the furnace gas delivery branch pipeline 201 .

为了对烧炉煤气输送支管路201和蓄热式加热炉100进行保护,本发明实施例所公开的烧炉煤气输送机构还包括第一氮气保护组件和第一放散组件。In order to protect the furnace gas delivery branch pipeline 201 and the regenerative heating furnace 100, the furnace gas delivery mechanism disclosed in the embodiment of the present invention further includes a first nitrogen protection component and a first release component.

其中,第一氮气保护组件包括第一氮气输送管路202和第一氮气吹扫阀2021,第一氮气输送管路202设置于第一双闸板闸阀2011和第一切断阀2012之间,且与烧炉煤气输送管路相连通,第一氮气吹扫阀2021设置于第一氮气输送管路202上;Wherein, the first nitrogen protection component includes a first nitrogen delivery pipeline 202 and a first nitrogen purge valve 2021, and the first nitrogen delivery pipeline 202 is arranged between the first double gate valve 2011 and the first cut-off valve 2012, and Connected with the furnace gas delivery pipeline, the first nitrogen purge valve 2021 is set on the first nitrogen delivery pipeline 202;

第一放散组件包括第一放散管路203和第一放散阀2031,第一放散管路203设置于第一双闸板闸阀2011和第一切断阀2012之间,且与烧炉煤气输送管路相连通,第一放散阀2031设置于第一放散管路203上。The first relief assembly includes a first relief pipeline 203 and a first relief valve 2031. The first relief pipeline 203 is arranged between the first double gate valve 2011 and the first cut-off valve 2012, and is connected to the furnace gas delivery pipeline. In communication with each other, the first relief valve 2031 is disposed on the first relief pipeline 203 .

当第一双闸板闸阀2011、第一切断阀2012和第一调节阀2013均关闭时,开启第一放散阀2031,将烧炉煤气输送支管路201内的漏入的煤气进行放散。When the first double gate valve 2011, the first cut-off valve 2012 and the first regulating valve 2013 are all closed, the first release valve 2031 is opened to release the leaked gas in the furnace gas delivery branch pipeline 201.

本发明实施例对助燃空气输送机构的具体结构不进行限定只要满足本发明使用要求的结构均在本发明的保护范围之内。The embodiment of the present invention does not limit the specific structure of the combustion air delivery mechanism, as long as the structure meets the requirements of the present invention, it is within the protection scope of the present invention.

作为优选实施例,本发明实施例所公开的助燃空气输送机构包括助燃空气输送总管路300、助燃空气输送支管路301、第二双闸板闸阀3011、第二切断阀3012和第二调节阀3013,其中,助燃空气输送总管路300的一端与助燃空气相连通,助燃空气输送总管路300的另一端与助燃空气输送支管路301相连通,助燃空气输送支管路301的另一端与蓄热式加热炉100相连通,第二双闸板闸阀3011、第二切断阀3012和第二调节阀3013均设置于助燃空气输送支管路301上。As a preferred embodiment, the combustion air delivery mechanism disclosed in the embodiment of the present invention includes a main combustion air delivery pipeline 300, a combustion air delivery branch pipeline 301, a second double gate valve 3011, a second shut-off valve 3012 and a second regulating valve 3013 , wherein, one end of the main combustion air delivery pipeline 300 is connected with the combustion air, the other end of the main combustion air delivery pipeline 300 is connected with the combustion air delivery branch pipeline 301, and the other end of the combustion air delivery branch pipeline 301 is connected with the regenerative heating The furnaces 100 are connected to each other, and the second double gate valve 3011 , the second cut-off valve 3012 and the second regulating valve 3013 are all arranged on the combustion air delivery branch pipeline 301 .

其中,第二调节阀3013用于调节助燃空气的气体流量,当第二双闸板闸阀3011、第二切断阀3012和第二调节阀3013均开启时,助燃空气可以从助燃空气输送总管路300进入助燃空气输送支管路301,再从助燃空气输送支管路301进入蓄热式加热炉100内。Wherein, the second regulating valve 3013 is used to regulate the gas flow rate of the combustion-supporting air. When the second double gate valve 3011, the second cut-off valve 3012 and the second regulating valve 3013 are all opened, the combustion-supporting air can be transported from the combustion-supporting air main pipeline 300 Enter the combustion-supporting air delivery branch pipeline 301, and then enter the regenerative heating furnace 100 from the combustion-supporting air delivery branch pipeline 301.

为了对助燃空气输送支管路301和和蓄热式加热炉100进行保护,本发明实施例所公开的助燃空气输送机构还包括第二氮气保护组件,第二放散组件和氧气输送组件。In order to protect the combustion air delivery branch pipeline 301 and the regenerative heating furnace 100, the combustion air delivery mechanism disclosed in the embodiment of the present invention further includes a second nitrogen protection component, a second release component and an oxygen delivery component.

第二放散组件包括第二放散管路304和第二放散阀3041,第二放散管路304设置于第二双闸板闸阀3011和第二切断阀3012之间,且与助燃空气输送管路301相连通,第二放散阀3041设置于第二放散管路304上。The second release assembly includes a second release line 304 and a second release valve 3041, the second release line 304 is arranged between the second double gate valve 3011 and the second cut-off valve 3012, and is connected to the combustion air delivery line 301 In communication with each other, the second relief valve 3041 is disposed on the second relief pipeline 304 .

其中,第二氮气保护组件包括第二氮气输送管路302和第二氮气吹扫阀3021,第二氮气输送管路302设置于第二双闸板闸阀3011和第二切断阀3012之间,且与助燃空气输送支管路301相连通,第二氮气吹扫阀3021设置于第二氮气输送管路302上。Wherein, the second nitrogen protection assembly includes a second nitrogen delivery pipeline 302 and a second nitrogen purge valve 3021, and the second nitrogen delivery pipeline 302 is arranged between the second double gate valve 3011 and the second shut-off valve 3012, and It communicates with the combustion air delivery branch pipeline 301 , and the second nitrogen purge valve 3021 is arranged on the second nitrogen delivery pipeline 302 .

其中,氧气输送组件包括氧气输送管路303和氧气调节阀3031,氧气调节阀3031设置于氧气输送管路303上,氧气输送管路303与助燃空气输送支管路301相连通,且氧气输送管路303设置于换热机构与第二调节阀3013之间。Wherein, the oxygen delivery assembly includes an oxygen delivery pipeline 303 and an oxygen regulating valve 3031, the oxygen regulating valve 3031 is arranged on the oxygen delivery pipeline 303, the oxygen delivery pipeline 303 is connected with the combustion air delivery branch pipeline 301, and the oxygen delivery pipeline 303 is disposed between the heat exchange mechanism and the second regulating valve 3013 .

当第二双闸板闸阀3011、第二切断阀3012和第二调节阀3013均关闭时,开启第二放散阀3041,将助燃空气支管路301内的漏入的煤气进行放散。When the second double gate valve 3011, the second cut-off valve 3012 and the second regulating valve 3013 are all closed, the second release valve 3041 is opened to release the leaked gas in the combustion air branch pipeline 301.

当第二双闸板闸阀3011、第二切断阀3012和第二调节阀3013均开启时,开启氧气调节阀3031,将氧气输入助燃空气输送支管路301内以进一步起到除积碳的作用。When the second double gate valve 3011, the second cut-off valve 3012 and the second regulating valve 3013 are all opened, the oxygen regulating valve 3031 is opened, and oxygen is input into the combustion air delivery branch pipeline 301 to further remove carbon deposits.

本发明实施例对烟气输送机构的具体结构不进行限定,只要满足本发明要求的结构均在本发明的保护范围之内。The embodiment of the present invention does not limit the specific structure of the flue gas conveying mechanism, as long as the structure meets the requirements of the present invention, it is within the protection scope of the present invention.

作为优选实施例,本发明实施例所公开的烟气输送机构包括烟气输送总管路400、烟气输送支管路401和第三双闸板闸阀4011,其中,烟气输送总管路400的一端与外界大气相连通,烟气输送总管路400的另一端与烟气输送支管路401相连通,烟气输送支管路401的另一端与蓄热式加热炉100相连通,第三双闸板闸阀4011设置于烟气输送支管路401上。As a preferred embodiment, the flue gas conveying mechanism disclosed in the embodiment of the present invention includes a flue gas conveying main pipeline 400, a flue gas conveying branch pipeline 401 and a third double gate valve 4011, wherein one end of the flue gas conveying main pipeline 400 is connected to The outside atmosphere is connected, the other end of the main flue gas delivery pipeline 400 is connected with the flue gas delivery branch pipeline 401, the other end of the flue gas delivery branch pipeline 401 is connected with the regenerative heating furnace 100, and the third double gate valve 4011 Set on the flue gas conveying branch pipeline 401.

其中,开启第三双闸板闸阀4011,蓄热式加热炉100内的烟气可以从蓄热式加热炉100内依次从烟气输送支管路401、烟气输送总管路400内排出到外界大气中。Wherein, open the third double gate valve 4011, the flue gas in the regenerative heating furnace 100 can be discharged from the regenerative heating furnace 100 through the flue gas conveying branch pipeline 401 and the flue gas conveying main pipeline 400 to the outside atmosphere middle.

其中,从蓄热式加热炉100内排出的烟气可以直接排放到大气中,也可以为进行回收利用。Wherein, the flue gas discharged from the regenerative heating furnace 100 may be directly discharged into the atmosphere, or may be recycled.

作为本发明的第一优选实施例,具体请参考图1,本发明实施例所公开的烟气输送机构还包括废气缓冲输出组件,其中,废气缓冲罐703输出组件包括废气输送管路700、废气阀701、废气调节阀702和缓冲罐703,废气阀701和废气调节阀702均设置于废气输送管路700上,废气输送管路700的一端与烟气输送支管路401相连通,废气输送管路700的另一端与缓冲罐703相连通。As the first preferred embodiment of the present invention, please refer to FIG. 1 for details. The flue gas delivery mechanism disclosed in the embodiment of the present invention also includes an exhaust gas buffer output assembly, wherein the output assembly of the exhaust gas buffer tank 703 includes an exhaust gas delivery pipeline 700, an exhaust gas The valve 701, the waste gas regulating valve 702 and the buffer tank 703, the waste gas valve 701 and the waste gas regulating valve 702 are all arranged on the waste gas conveying pipeline 700, and one end of the waste gas conveying pipeline 700 is connected with the flue gas conveying branch pipeline 401, and the waste gas conveying pipe The other end of the path 700 communicates with a buffer tank 703 .

需要说明的是,废气调节阀702可以调节废气输送管路700的流量,当开启废气阀701、废气调节阀702,烟气可以依次从烟气输送支管路401、废气阀701、废气调节阀702进入缓冲罐703内,在缓冲罐703内缓冲后排到外界大气中。It should be noted that the waste gas regulating valve 702 can adjust the flow rate of the waste gas conveying pipeline 700. When the waste gas valve 701 and the waste gas regulating valve 702 are opened, the flue gas can be transported from the flue gas conveying branch pipe 401, the waste gas valve 701, and the waste gas regulating valve 702 in sequence. Enter the buffer tank 703, and discharge into the outside atmosphere after being buffered in the buffer tank 703.

作为本发明的第二优选实施例,具体请参考图2,本发明实施例所公开的烟气输送机构还包括废气回收组件,废气回收组件包括废气输送管路700、废气阀701、废气调节阀702和回收罐704,废气阀701和废气调节阀702均设置于废气输送管路700上,废气输送管路700的一端与烟气输送支管路401相连通,废气输送管路700的另一端与回收罐704相连通。As the second preferred embodiment of the present invention, please refer to FIG. 2 for details. The flue gas delivery mechanism disclosed in the embodiment of the present invention also includes an exhaust gas recovery assembly, which includes an exhaust gas delivery pipeline 700, an exhaust gas valve 701, and an exhaust gas regulating valve. 702 and the recovery tank 704, the waste gas valve 701 and the waste gas regulating valve 702 are all arranged on the waste gas delivery pipeline 700, one end of the waste gas delivery pipeline 700 is connected with the flue gas delivery branch pipeline 401, and the other end of the waste gas delivery pipeline 700 is connected with the The recovery tank 704 is connected.

需要说明的是,废气调节阀702可以调节废气输送管路700的流量,当开启废气阀701、废气调节阀702,烟气可以依次从烟气输送支管路401、废气阀701、废气调节阀702进入回收罐704内被回收利用。It should be noted that the waste gas regulating valve 702 can adjust the flow rate of the waste gas conveying pipeline 700. When the waste gas valve 701 and the waste gas regulating valve 702 are opened, the flue gas can be transported from the flue gas conveying branch pipe 401, the waste gas valve 701, and the waste gas regulating valve 702 in sequence. Enter the recycling tank 704 to be recycled.

本发明实施例对高压强爆炸性低温煤气输送机构的具体机构不进行限定,只要满足本发明使用要求的结构均在本发明的保护范围之内。The embodiment of the present invention does not limit the specific mechanism of the high-pressure, high-explosive, low-temperature gas delivery mechanism, as long as the structure meets the requirements of the present invention, it is within the protection scope of the present invention.

作为优选实施例,本发明实施例所公开的高压强爆炸性低温煤气输送机构包括高压强爆炸性低温煤气输送管路500、第四双闸板闸阀501和第三切断阀502,第四双闸板闸阀501和第三切断阀502均设置于高压强爆炸性低温煤气输送管路500上,高压强爆炸性低温煤气输送管路500的一端与高压强爆炸性低温煤气相连通,高压强爆炸性低温煤气输送管路500的另一端与蓄热式加热炉100相连通。As a preferred embodiment, the high-pressure strong explosive low-temperature gas delivery mechanism disclosed in the embodiment of the present invention includes a high-pressure strong explosive low-temperature gas delivery pipeline 500, a fourth double gate valve 501 and a third shut-off valve 502, the fourth double gate valve 501 and the third cut-off valve 502 are both arranged on the high-pressure and high-explosive low-temperature gas delivery pipeline 500, one end of the high-pressure and high-explosive low-temperature gas delivery pipeline 500 communicates with the high-pressure and high-explosive low-temperature gas delivery pipeline 500 The other end communicates with the regenerative heating furnace 100.

作为优选实施例,本发明实施例所公开的高压强爆炸性低温煤气输送机构还包括第三氮气保护组件、均压组件和蒸汽输送组件。As a preferred embodiment, the high-pressure, high-strength, explosive, and low-temperature gas delivery mechanism disclosed in the embodiment of the present invention further includes a third nitrogen protection component, a pressure equalization component, and a steam delivery component.

其中,第三氮气保护组件包括第三氮气吹扫管路503,和设置于氮气吹扫管路上的第三氮气吹扫阀5031,第三氮气吹扫管路503设置于第四双闸板闸阀501和第三切断阀502,且第三氮气吹扫管路503与高压强爆炸性低温煤气输送管路500相连通。Wherein, the third nitrogen protection component includes a third nitrogen purge pipeline 503, and a third nitrogen purge valve 5031 arranged on the nitrogen purge pipeline, and the third nitrogen purge pipeline 503 is set on the fourth double-disc gate valve 501 and the third shut-off valve 502, and the third nitrogen purge pipeline 503 is in communication with the high-pressure strong explosive low-temperature gas delivery pipeline 500.

其中,均压组件包括均压管路504和均压阀5041,均压阀5041设于均压管路504上,均压管路504的两端分别设置于第四双闸板闸阀501的两侧。Wherein, the pressure equalizing component includes a pressure equalizing pipeline 504 and a pressure equalizing valve 5041, the pressure equalizing valve 5041 is arranged on the pressure equalizing pipeline 504, and the two ends of the pressure equalizing pipeline 504 are respectively arranged on the two ends of the fourth double gate valve 501. side.

其中,蒸汽输送组件包括蒸汽输送管路505和蒸汽调节阀5051,蒸汽调节阀5051设置于蒸汽输送管路505上,蒸汽输送管路505与高压强爆炸性低温煤气管路相连通。Wherein, the steam conveying assembly includes a steam conveying pipeline 505 and a steam regulating valve 5051, the steam regulating valve 5051 is arranged on the steam conveying pipeline 505, and the steam conveying pipeline 505 is connected with a high-pressure strong explosive low-temperature gas pipeline.

需要说明的是,均压阀5041能够平衡高压强爆炸性低温煤气输送管路500内的压力,当开启第四双闸板闸阀501和第三切断阀502,高压强爆炸性低温煤气可以进入蓄热式加热炉100内进行燃烧。It should be noted that the pressure equalizing valve 5041 can balance the pressure in the high-pressure strong explosive low-temperature gas pipeline 500. When the fourth double gate valve 501 and the third shut-off valve 502 are opened, the high-pressure strong explosive low-temperature gas can enter the regenerative Combustion is carried out in the heating furnace 100 .

当关闭第四双闸板闸阀501,开启第三切断阀502,开启第三氮气吹扫阀5031,可以对第四双闸板闸阀501和蓄热式加热炉100之间的高压强爆炸性低温煤气输送管路500进行吹扫。When the fourth double gate valve 501 is closed, the third cut-off valve 502 is opened, and the third nitrogen purge valve 5031 is opened, the high pressure strong explosive low temperature gas between the fourth double gate valve 501 and the regenerative heating furnace 100 can be The delivery line 500 is purged.

当高压强爆炸性低温煤气进入蓄热式加热炉100内时,可以开启蒸汽调节阀5051,使得蒸汽进入高压强爆炸性低温煤气输送管路500上,从而抑制积碳形成。When high-pressure strong explosive low-temperature gas enters the regenerative heating furnace 100, the steam regulating valve 5051 can be opened to allow steam to enter the high-pressure strong explosive low-temperature gas delivery pipeline 500, thereby inhibiting the formation of carbon deposits.

本发明实施例对高压强爆炸性高温煤气输送机构的具体结构不进行限定,只要满足本发明使用要求的结构均在本发明的保护范围内。The embodiment of the present invention does not limit the specific structure of the high-pressure, high-explosive, high-temperature gas delivery mechanism, as long as the structure meets the requirements of the present invention, it is within the protection scope of the present invention.

作为优选实施例,本发明实施例所公开的高压强爆炸性高温煤气输送机构包括高压强爆炸性高温煤气输送管路600和高压强爆炸性高温煤气阀601,高压强爆炸性高温煤气阀601设置于高压强爆炸性高温煤气输送管路600上,高压强爆炸性高温煤气输送管路600的一端与高压强爆炸性高温煤气相连通,高压强爆炸性高温煤气输送管路600的另一端与蓄热式加热炉100相连通。As a preferred embodiment, the high-pressure and explosive high-temperature gas delivery mechanism disclosed in the embodiment of the present invention includes a high-pressure and explosive high-temperature gas delivery pipeline 600 and a high-pressure and explosive high-temperature gas valve 601. On the high-temperature gas pipeline 600 , one end of the high-pressure and explosive high-temperature gas pipeline 600 is connected to the high-pressure and explosive high-temperature gas, and the other end of the high-pressure and explosive high-temperature gas pipeline 600 is connected to the regenerative heating furnace 100 .

高压强爆炸性低温煤气在蓄热式加热炉100内加热燃烧形成高压强爆炸性高温煤气,打开高压强爆炸性高温煤气阀601,蓄热式加热炉100内的高温煤气可以进入高压强爆炸性高温煤气输送管路600内。The high-pressure and explosive low-temperature gas is heated and burned in the regenerative heating furnace 100 to form high-pressure and explosive high-temperature gas, and the high-pressure and explosive high-temperature gas valve 601 is opened, and the high-temperature gas in the regenerative heating furnace 100 can enter the high-pressure and explosive high-temperature gas delivery pipe Inside the road 600.

需要说明的是,本发明实施例还在高压强爆炸性高温煤气输送管路600上还设置有波纹补偿器及拉紧装置,如此设置,可以避免高压强爆炸性高温煤气输送管路因膨胀所导致的管道开裂和煤气泄露。It should be noted that in the embodiment of the present invention, a corrugated compensator and a tensioning device are also provided on the high-pressure, high-temperature, explosive, and high-temperature gas delivery pipeline 600, so that the expansion of the high-pressure, high-pressure, and high-temperature gas delivery pipeline can be avoided. Cracked pipes and gas leaks.

同时,在波纹补偿器的波纹管的夹层中还设置有压力检测点以监控补偿器是否发生泄露。At the same time, a pressure detection point is also set in the interlayer of the bellows of the corrugated compensator to monitor whether the compensator leaks.

本发明实施例所公开的蓄热式加热炉100可以设置两座,可以设置多座,本发明实施例对此不进行限定,本领域技术人员可以根据实际情况进行选择。The regenerative heating furnace 100 disclosed in the embodiment of the present invention can be provided with two or more, which is not limited in the embodiment of the present invention, and those skilled in the art can choose according to the actual situation.

作为优选,本发明实施例所公开的蓄热式加热炉100优选设置2-4座,当设置2-4座,可以设置多条烧炉煤气输送支管路201、助燃空气输送支管路301和烟气输送支管路401,其中多条烧炉煤气输送支管路201的两端分别连通烧炉煤气输送总管路200和蓄热式加热炉100,助燃空气输送支管路301的两端分别连通烟气输送总管路400和蓄热式加热炉100,烟气输送支管路401的两端分别连通外界大气和蓄热式加热炉100。As a preference, the regenerative heating furnace 100 disclosed in the embodiment of the present invention is preferably provided with 2-4 seats. When 2-4 seats are provided, multiple furnace gas delivery branch pipelines 201, combustion-supporting air delivery branch pipelines 301 and smoke Gas delivery branch pipeline 401, in which the two ends of a plurality of furnace gas delivery branch pipelines 201 are respectively connected to the furnace gas delivery main pipeline 200 and the regenerative heating furnace 100, and the two ends of the combustion-supporting air delivery branch pipeline 301 are respectively connected to flue gas delivery Both ends of the main pipeline 400 and the regenerative heating furnace 100 , and the flue gas delivery branch pipeline 401 are respectively connected to the external atmosphere and the regenerative heating furnace 100 .

本发明实施例对换热机构的具体结构不进行限定,只要满足本发明使用要求的结构均在本发明的保护范围之内。The embodiment of the present invention does not limit the specific structure of the heat exchange mechanism, as long as the structure meets the requirements of the present invention, it is within the protection scope of the present invention.

作为优选实施例,本发明实施例所公开的换热机构包括第一换热器900和第二换热器1000,其中,第一换热器900串联于烧炉煤气输送总管路200与烟气输送总管路400上,第二换热器1000串联于助燃空气输送总管路300与烟气输送总管路400上。As a preferred embodiment, the heat exchange mechanism disclosed in the embodiment of the present invention includes a first heat exchanger 900 and a second heat exchanger 1000, wherein the first heat exchanger 900 is connected in series with the main furnace gas delivery pipeline 200 and the flue gas On the main delivery pipeline 400 , the second heat exchanger 1000 is connected in series with the main combustion air delivery pipeline 300 and the main flue gas delivery pipeline 400 .

如此设置,可以通过第一换热器900将烟气与烧炉煤气进行换热,使得烟气的温度降低,烧炉煤气的温度升高,同时也可以通过第二换热器1000将烟气与助燃空气进行换热,使得烟气的温度降低,助燃空气的温度升高。With such an arrangement, the flue gas can exchange heat with the furnace gas through the first heat exchanger 900, so that the temperature of the flue gas decreases and the temperature of the furnace gas increases, and the flue gas can also be transferred through the second heat exchanger 1000 The heat exchange with the combustion-supporting air reduces the temperature of the flue gas and increases the temperature of the combustion-supporting air.

作为优选实施例,本发明实施例所公开的煤气加热装置还包括第四氮气吹扫管路800和设置于第四氮气吹扫管路800上的第四氮气吹扫阀801,第五氮气吹扫阀802和第六氮气吹扫阀803,其中,第四氮气吹扫阀801,第五氮气吹扫阀802和第六氮气吹扫阀803可以分别对蓄热式加热炉100进行氮气吹扫,以进一步提升蓄热式加热炉100的安全性。As a preferred embodiment, the gas heating device disclosed in the embodiment of the present invention also includes a fourth nitrogen purge pipeline 800 and a fourth nitrogen purge valve 801 arranged on the fourth nitrogen purge pipeline 800, and the fifth nitrogen purge The purge valve 802 and the sixth nitrogen purge valve 803, wherein the fourth nitrogen purge valve 801, the fifth nitrogen purge valve 802 and the sixth nitrogen purge valve 803 can carry out nitrogen purge to the regenerative heating furnace 100 respectively , to further enhance the safety of the regenerative heating furnace 100.

需要说明的是,本发明实施例所公开的煤气加热装置还包括多个泄爆阀和泄爆膜,在发生意外爆炸时,可进行定向有组织泄爆;It should be noted that the gas heating device disclosed in the embodiment of the present invention also includes a plurality of explosion relief valves and explosion relief membranes, which can perform directional and organized explosion relief in the event of an accidental explosion;

本发明实施例还公开了一种煤气加热方法,应用于如上述任意一项实施例所公开的的煤气加热装置中,包括闷炉转烧炉模式、烧炉转闷炉模式、闷炉转送风模式和送风转闷炉模式,闷炉转烧炉模式、烧炉转闷炉模式、闷炉转送风模式和送风转闷炉模式之间能够相互切换。The embodiment of the present invention also discloses a gas heating method, which is applied to the gas heating device disclosed in any one of the above embodiments, including the mode of turning the furnace into a furnace, the mode of turning a furnace into a furnace, and the mode of transferring a furnace into a furnace. Wind mode and air supply to furnace mode, furnace to furnace mode, furnace to furnace mode, furnace to air mode and air supply to furnace mode can be switched to each other.

其中,闷炉转烧炉模式为:Among them, the mode of the smoldering furnace to the firing furnace is:

S100:开启废气调节阀702,开启废气阀701,使得蓄热式加热炉100内的高压强爆炸性高温煤气放散,直至蓄热式加热炉100内的压力达到预设压力值;S100: Open the waste gas regulating valve 702 and the waste gas valve 701, so that the high-pressure, explosive and high-temperature gas in the regenerative heating furnace 100 is released until the pressure in the regenerative heating furnace 100 reaches a preset pressure value;

S200:关闭第一氮气吹扫阀2021,开启第一放散阀2031,将蓄热式加热炉100内的压力进行卸载;S200: close the first nitrogen purge valve 2021, open the first relief valve 2031, and unload the pressure in the regenerative heating furnace 100;

S300:开启烧炉煤气输送支管路201上第一双闸板闸阀2011,保持第一切断阀2012关闭,开启第一氮气吹扫阀2021,对蓄热式加热炉100内的高压强爆炸性高温煤气吹扫置换,直至烟气输送支管路401内的一氧化碳含量达标,放散完成;S300: Open the first double-gate gate valve 2011 on the furnace gas delivery branch pipeline 201, keep the first cut-off valve 2012 closed, open the first nitrogen purge valve 2021, and clean the high-pressure strong explosive high-temperature gas in the regenerative heating furnace 100 Purging and replacement until the carbon monoxide content in the flue gas delivery branch pipeline 401 reaches the standard, and the release is completed;

S400:开启烧炉煤气输送支管路201上的第一双闸板闸阀2011,开启第一切断阀2012,开启第一调节阀2013,关闭第一氮气吹扫阀2021,关闭第一放散阀2031,同时开启助燃空气支管路上301的第二双闸板闸阀3011,开启第二切断阀3012,开启第二调节阀3013,关闭第二氮气吹扫阀3021,关闭第二放散阀3041,使得烧炉煤气通过第一换热器900进入蓄热式加热炉100,使得助燃空气通过第二换热器1000进入蓄热式加热炉100,使得蓄热式加热炉100进入燃烧状态;S400: Open the first double gate valve 2011 on the furnace gas delivery branch pipeline 201, open the first cut-off valve 2012, open the first regulating valve 2013, close the first nitrogen purge valve 2021, close the first release valve 2031, Simultaneously open the second double gate valve 3011 of 301 on the combustion air branch pipeline, open the second cut-off valve 3012, open the second regulating valve 3013, close the second nitrogen purge valve 3021, close the second release valve 3041, so that the furnace gas Enter the regenerative heating furnace 100 through the first heat exchanger 900, so that the combustion air enters the regenerative heating furnace 100 through the second heat exchanger 1000, so that the regenerative heating furnace 100 enters a combustion state;

烧炉转闷炉模式为:The furnace-to-steel furnace mode is:

关闭第一调节阀2013、关闭第一切断阀2012,关闭第二调节阀3013,关闭第二切断阀3012,保持第一双闸板闸阀2011开启,保持第二双闸板闸阀3011开启,开启第一氮气吹扫阀2021,开启第二氮气吹扫阀3021,对烧炉煤气输送支管路和助燃空气输送支管路301进行吹扫,同时开启第四氮气吹扫阀801和第五氮气吹扫阀802,当第一预设时间后,关闭第一双闸板闸板和第二双闸板闸阀3011,当第二预设时间后,关闭烧炉煤气输送支管路201上的第一氮气吹扫阀2021,开启第一放散阀2031,关闭第二氮气吹扫阀3021,开启第二放散阀3041,同时关闭烟气输送支管路401双闸板闸阀4011,蓄热式加热炉100由烧炉转为闷炉。Close the first regulating valve 2013, close the first shut-off valve 2012, close the second regulating valve 3013, close the second shut-off valve 3012, keep the first double gate valve 2011 open, keep the second double gate valve 3011 open, open the second A nitrogen purge valve 2021, open the second nitrogen purge valve 3021, purge the furnace gas delivery branch pipeline and combustion-supporting air delivery branch pipeline 301, and open the fourth nitrogen purge valve 801 and the fifth nitrogen purge valve at the same time 802. After the first preset time, close the first double gate gate valve and the second double gate gate valve 3011, and after the second preset time, close the first nitrogen purge on the furnace gas delivery branch pipeline 201 Valve 2021, open the first relief valve 2031, close the second nitrogen purge valve 3021, open the second relief valve 3041, and close the flue gas delivery branch pipeline 401 and double gate valve 4011 at the same time, the regenerative heating furnace 100 is converted from the furnace For the stuffy furnace.

闷炉转送风工作模式为:The working mode of the stuffy furnace transfer air supply is:

开启第三切断阀502,开启第三氮气吹扫阀5031,对高压强爆炸性低温煤气输送管路500进行氮气吹扫,吹扫完毕后,关闭第三氮气吹扫阀5031;Open the third cut-off valve 502, open the third nitrogen purge valve 5031, and carry out nitrogen purge on the high-pressure strong explosive low-temperature gas delivery pipeline 500, and close the third nitrogen purge valve 5031 after the purge is completed;

开启均压阀5041,当蓄热式加热炉100内的压力达到预设压力值时,关闭均压阀5041,开启第四双闸板闸阀501,将高压强爆炸性高温煤气输送管路600送入蓄热式加热炉100内。Open the pressure equalizing valve 5041, when the pressure in the regenerative heating furnace 100 reaches the preset pressure value, close the pressure equalizing valve 5041, open the fourth double gate valve 501, and send the high-pressure strong explosive high-temperature gas pipeline 600 into the Inside the regenerative heating furnace 100.

送风转闷炉的工作模式为:The working mode of the air-supply rotary furnace is:

关闭高压强爆炸性高温煤气阀601,第四双闸板闸阀501和第三切断阀502,开启第三氮气吹扫阀5031,蓄热式加热炉100由送风转为闷炉模式。Close the high-pressure strong explosive high-temperature gas valve 601, the fourth double gate valve 501 and the third cut-off valve 502, open the third nitrogen purge valve 5031, and the regenerative heating furnace 100 changes from air supply to stuffy furnace mode.

和现有技术相比,本发明实施例所公开的煤气加热装置设置了第一换热器900和第二换热器1000,第一换热器900可以将进入蓄热式加热炉100内的烧炉煤气与从蓄热式加热炉100内的流出的烟气进行换热,第二换热器1000可以将进入蓄热式加热炉100内的助燃空气与从蓄热式加热炉100内流出的烟气进行换热,如此设置,可以使得进入蓄热式加热炉100内的烧炉煤气与助燃空气能够首先通过第一换热器和第二换热器将温度升高后再进入蓄热式加热炉100,如此设置,可以大大提高蓄热式加热炉100的燃烧效率,同时也可以降低流到外界大气中的烟气的温度,从而进一步降低环境污染。Compared with the prior art, the gas heating device disclosed in the embodiment of the present invention is provided with a first heat exchanger 900 and a second heat exchanger 1000, and the first heat exchanger 900 can transfer the gas entering the regenerative heating furnace 100 The furnace gas exchanges heat with the flue gas flowing out from the regenerative heating furnace 100, and the second heat exchanger 1000 can exchange the combustion-supporting air entering the regenerative heating furnace 100 with the flue gas flowing out from the regenerative heating furnace 100. The flue gas is heat-exchanged, so that the furnace gas and combustion-supporting air entering the regenerative heating furnace 100 can first pass through the first heat exchanger and the second heat exchanger to raise the temperature before entering the heat storage Type heating furnace 100, so set, can greatly improve the combustion efficiency of regenerative heating furnace 100, can also reduce the temperature of flue gas flowing into the outside atmosphere, thereby further reducing environmental pollution.

本发明实施例对第一预设时间和第二预设时间不进行限定,本领域技术人员可以根据实际情况进行选择。The embodiment of the present invention does not limit the first preset time and the second preset time, and those skilled in the art may select according to actual conditions.

在本申请的描述中,需要说明的是,术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。此外,术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of this application, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer" etc. The indicated orientation or positional relationship is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present application and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, use a specific orientation construction and operation, therefore should not be construed as limiting the application. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.

除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本申请中的具体含义。Unless otherwise clearly specified and limited, the terms "installation", "connection" and "connection" should be interpreted in a broad sense, for example, it may be a fixed connection, a detachable connection, or an integral connection; it may be a mechanical connection, It can also be an electrical connection; it can be a direct connection, or an indirect connection through an intermediary, or an internal communication between two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in this application in specific situations.

对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下,在其它实施例中实现。因此,本发明将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.

Claims (15)

1.一种煤气加热装置,其特征在于,包括蓄热式加热炉、换热机构、烧炉煤气输送机构、助燃空气输送机构、烟气输送机构,所述烧炉煤气输送机构、所述助燃空气输送机构和所述烟气输送机构均与所述蓄热式加热炉相连通,且所述烧炉煤气输送机构、所述助燃空气输送机构和所述烟气输送机构均并联;1. A gas heating device, characterized in that it comprises a regenerative heating furnace, a heat exchange mechanism, a furnace gas conveying mechanism, a combustion-supporting air conveying mechanism, a flue gas conveying mechanism, the furnace gas conveying mechanism, the combustion-supporting Both the air conveying mechanism and the flue gas conveying mechanism are connected to the regenerative heating furnace, and the furnace gas conveying mechanism, the combustion air conveying mechanism and the flue gas conveying mechanism are all connected in parallel; 所述烧炉煤气输送机构用于将烧炉煤气输送至所述蓄热式加热炉内,所述助燃空气输送机构用于将助燃空气输送至所述蓄热式加热炉内,所述烟气输送机构用于将所述蓄热式加热炉内流出的烟气输出;The furnace gas conveying mechanism is used to convey the furnace gas to the regenerative heating furnace, the combustion-supporting air conveying mechanism is used to convey the combustion-supporting air to the regenerative heating furnace, and the flue gas The conveying mechanism is used to output the flue gas flowing out of the regenerative heating furnace; 所述换热机构串联在所述烧炉煤气输送机构、所述助燃空气输送机构和所述烟气输送机构上,所述换热机构能够将所述烟气的温度降低,且所述换热机构将所述烧炉煤气和所述助燃空气的温度升高。The heat exchange mechanism is connected in series to the furnace gas delivery mechanism, the combustion air delivery mechanism and the flue gas delivery mechanism, the heat exchange mechanism can reduce the temperature of the flue gas, and the heat exchange A mechanism increases the temperature of the furnace gas and the combustion air. 2.根据权利要求1所述的煤气加热装置,其特征在于,还包括高压强爆炸性低温煤气输送机构和高压强爆炸性高温煤气输送机构,所述高压强爆炸性低温煤气输送机构和所述高压强爆炸性高温煤气输送机构均与所述蓄热式加热炉相连通;2. The gas heating device according to claim 1, characterized in that it also includes a high-pressure explosive low-temperature gas delivery mechanism and a high-pressure explosive high-temperature gas delivery mechanism, the high-pressure explosive low-temperature gas delivery mechanism and the high-pressure explosive low-temperature gas delivery mechanism The high-temperature gas conveying mechanisms are all connected to the regenerative heating furnace; 所述高压强爆炸性低温煤气输送机构用于将高压强爆炸性低温煤气输送至所述蓄热式加热炉内,所述高压强爆炸性高温煤气输送机构用于将所述蓄热式加热内的高压强爆炸性高温煤气输出。The high-pressure explosive low-temperature gas delivery mechanism is used to deliver the high-pressure explosive low-temperature gas to the regenerative heating furnace, and the high-pressure explosive high-temperature gas delivery mechanism is used to transport the high-pressure explosive low-temperature gas inside the regenerative heating furnace. Explosive hot gas output. 3.根据权利要求1所述的煤气加热装置,其特征在于,所述烧炉煤气输送机构包括烧炉煤气输送总管路,烧炉煤气输送支管路、第一双闸板闸阀、第一切断阀和第一调节阀,所述烧炉煤气输送总管路的一端与烧炉煤气相连通,所述烧炉煤气输送总管路的另一端与所述烧炉煤气输送支管路的一端相连通,所述烧炉煤气输送支管路的另一端与所述蓄热式加热炉相连通,所述第一双闸板闸阀、所述第一切断阀和所述第一调节阀均设置于所述烧炉煤气输送支管路上。3. The gas heating device according to claim 1, characterized in that, the furnace gas conveying mechanism comprises a main furnace gas conveying pipeline, a furnace gas conveying branch pipeline, a first double gate valve, and a first shut-off valve and the first regulating valve, one end of the main furnace gas delivery pipeline communicates with the furnace gas, the other end of the main furnace gas delivery pipeline communicates with one end of the furnace gas delivery branch pipeline, and the The other end of the furnace gas delivery branch pipeline is connected to the regenerative heating furnace, and the first double gate valve, the first shut-off valve and the first regulating valve are all set at the On the delivery branch pipeline. 4.根据权利要求3所述的煤气加热装置,其特征在于,所述烧炉煤气输送机构还包括第一氮气保护组件和第一放散组件;4. The gas heating device according to claim 3, characterized in that, the furnace gas delivery mechanism further comprises a first nitrogen protection component and a first release component; 所述第一氮气保护组件包括第一氮气输送管路和第一氮气吹扫阀,所述第一氮气输送管路设置于所述第一双闸板闸阀和所述第一切断阀之间,且与所述烧炉煤气输送管路相连通,所述第一氮气吹扫阀设置于所述第一氮气输送管路上;The first nitrogen protection component includes a first nitrogen delivery pipeline and a first nitrogen purge valve, and the first nitrogen delivery pipeline is arranged between the first double gate valve and the first cut-off valve, And communicated with the furnace gas delivery pipeline, the first nitrogen purge valve is set on the first nitrogen delivery pipeline; 所述第一放散组件包括第一放散管路和第一放散阀,所述第一放散管路设置于所述第一双闸板闸阀和所述第一切断阀之间,且与所述烧炉煤气输送管路相连通,所述第一放散阀设置于所述第一放散管路上。The first relief assembly includes a first relief pipeline and a first relief valve, and the first relief pipeline is arranged between the first double gate valve and the first shut-off valve, and is connected to the burner The furnace gas delivery pipeline is connected, and the first relief valve is arranged on the first relief pipeline. 5.根据权利要求1所述的煤气加热装置,其特征在于,所述助燃空气输送机构包括助燃空气输送总管路、助燃空气输送支管路、第二双闸板闸阀、第二切断阀和第二调节阀,所述助燃空气输送总管路的一端与助燃空气相连通,所述助燃空气输送总管路的另一端与所述助燃空气支管路相连通,所述助燃空气输送支管路的另一端与所述蓄热式加热炉相连通,所述第二双闸板闸阀、所述第二切断阀和所述第二调节阀均设置于所述助燃空气输送支管路上。5. The gas heating device according to claim 1, characterized in that, the combustion air delivery mechanism comprises a main combustion air delivery pipeline, a combustion air delivery branch pipeline, a second double gate valve, a second cut-off valve and a second Regulating valve, one end of the main combustion air delivery pipeline communicates with the combustion air, the other end of the main combustion air delivery pipeline communicates with the combustion air branch pipeline, and the other end of the combustion air delivery branch pipeline communicates with the The regenerative heating furnace is connected, and the second double gate valve, the second cut-off valve and the second regulating valve are all arranged on the combustion air delivery branch pipeline. 6.根据权利要求5所述的煤气加热装置,其特征在于,所述助燃空气输送机构还包括第二氮气保护组件、第二放散组件和氧气输送组件;6. The gas heating device according to claim 5, wherein the combustion air delivery mechanism further comprises a second nitrogen protection component, a second release component and an oxygen delivery component; 所述第二氮气保护组件包括第二氮气输送管路和第二氮气吹扫阀,所述第二氮气输送管路设置于所述第二双闸板闸阀和所述第二切断阀之间,且与所述烧炉煤气输送支管路相连通,所述第二氮气吹扫阀设置于所述第二氮气输送管路上;The second nitrogen protection component includes a second nitrogen delivery pipeline and a second nitrogen purge valve, and the second nitrogen delivery pipeline is arranged between the second double gate valve and the second cut-off valve, And communicated with the furnace gas delivery branch pipeline, the second nitrogen purge valve is arranged on the second nitrogen delivery pipeline; 所述第二放散组件包括第二放散管路和第二放散阀,所述第二放散管路设置于所述第二双闸板闸阀和所述第二切断阀之间,且与所述烧炉煤气输送管路相连通,所述第二放散阀设置于所述第二放散管路上;The second relief assembly includes a second relief pipeline and a second relief valve, the second relief pipeline is arranged between the second double-disc gate valve and the second shut-off valve, and is connected to the burner The furnace gas delivery pipeline is connected, and the second relief valve is arranged on the second relief pipeline; 所述氧气输送组件包括氧气输送管路和氧气调节阀,所述氧气调节阀设置于所述氧气输送路上,所述氧气输送管路与所述助燃空气输送支管路相连通,且所述氧气输送管路设置于所述换热机构与所述第二调节阀之间。The oxygen delivery assembly includes an oxygen delivery pipeline and an oxygen regulating valve, the oxygen regulating valve is arranged on the oxygen delivery path, the oxygen delivery pipeline communicates with the combustion air delivery branch pipeline, and the oxygen delivery The pipeline is arranged between the heat exchange mechanism and the second regulating valve. 7.根据权利要求1所述的煤气加热装置,其特征在于,所述烟气输送机构包括烟气输送总管路、烟气输送支管路和第三双闸板闸阀,所述烟气输送总管路的一端与外界大气相连通,所述烟气输送总管路的另一端与所述烟气输送支管路相连通,所述烟气输送支管路的另一端与所述蓄热式加热炉相连通,所述第三双闸板闸阀设置于所述烟气输送支管路上。7. The gas heating device according to claim 1, characterized in that, the flue gas conveying mechanism comprises a flue gas conveying main pipeline, a flue gas conveying branch pipeline and a third double gate valve, and the flue gas conveying main pipeline One end of the flue gas delivery pipeline is connected with the outside atmosphere, the other end of the flue gas delivery main pipeline is connected with the flue gas delivery branch pipeline, and the other end of the flue gas delivery branch pipeline is connected with the regenerative heating furnace, The third double gate valve is arranged on the flue gas conveying branch pipeline. 8.根据权利要求7所述的煤气加热装置,其特征在于,所述烟气输送机构还包括废气缓冲输出组件,所述废气缓冲罐输出组件包括废气输送管路、废气阀、废气调节阀和缓冲罐,所述废气阀和所述废气调节阀均设置于所述废气输送管路上,所述废气输送管路的一端与所述烟气输送支管路相连通,所述废气输送管路的另一端与所述缓冲罐相连通。8. The gas heating device according to claim 7, characterized in that, the flue gas conveying mechanism further includes an exhaust gas buffer output assembly, and the exhaust gas buffer tank output assembly includes an exhaust gas delivery pipeline, an exhaust gas valve, an exhaust gas regulating valve and The buffer tank, the waste gas valve and the waste gas regulating valve are all arranged on the waste gas conveying pipeline, one end of the waste gas conveying pipeline communicates with the flue gas conveying branch pipeline, and the other end of the waste gas conveying pipeline One end communicates with the buffer tank. 9.根据权利要求7所述的煤气加热装置,其特征在于,所述烟气输送机构还包括废气回收组件,所述废气回收组件包括废气输送管路、废气阀、废气调节阀和回收罐,所述废气阀和所述废气调节阀均设置于所述废气输送管路上,所述废气输送管路的一端与所述烟气输送支管路相连通,所述废气输送管路的另一端与所述回收罐相连通。9. The gas heating device according to claim 7, characterized in that, the flue gas conveying mechanism further includes a waste gas recovery assembly, and the waste gas recovery component includes a waste gas conveying pipeline, a waste gas valve, a waste gas regulating valve and a recovery tank, Both the waste gas valve and the waste gas regulating valve are arranged on the waste gas conveying pipeline, one end of the waste gas conveying pipeline communicates with the flue gas conveying branch pipeline, and the other end of the waste gas conveying pipeline communicates with the exhaust gas conveying pipeline. The recovery tank is connected. 10.根据权利要求2所述的煤气加热装置,其特征在于,所述高压强爆炸性低温煤气输送机构包括高压强爆炸性低温煤气输送管路、第四双闸板闸阀和第三切断阀,所述第四双闸板闸阀和第三切断阀均设置于所述高压强爆炸性低温煤气输送管路上,所述高压强爆炸性低温煤气输送管路的一端与高压强爆炸性低温煤气相连通,所述高压强爆炸性低温煤气输送管路的另一端与所述蓄热式加热炉相连通。10. The gas heating device according to claim 2, characterized in that, the high-pressure explosive low-temperature gas delivery mechanism comprises a high-pressure explosive low-temperature gas delivery pipeline, a fourth double gate valve and a third shut-off valve, the Both the fourth double gate valve and the third cut-off valve are arranged on the high-pressure, high-explosive, low-temperature gas delivery pipeline, one end of the high-pressure, high-explosive, low-temperature gas delivery pipeline communicates with the high-pressure, high-explosive, low-temperature gas, and the high-pressure, high-pressure, low-temperature gas delivery pipeline The other end of the explosive low-temperature gas delivery pipeline communicates with the regenerative heating furnace. 11.根据权利要求10所述的煤气加热装置,其特征在于,所述高压强爆炸性低温煤气输送机构还包括第三氮气保护组件、均压组件和蒸汽输送组件;11. The gas heating device according to claim 10, characterized in that, the high-pressure explosive low-temperature gas delivery mechanism further comprises a third nitrogen protection component, a pressure equalization component and a steam delivery component; 所述第三氮气保护组件包括第三氮气吹扫管路,和设置于所述氮气吹扫管路上的第三氮气吹扫阀,所述第三氮气吹扫管路设置于所述第四双闸板闸阀和第三切断阀,且所述第三氮气吹扫管路与所述高压强爆炸性低温煤气输送管路相连通;The third nitrogen protection component includes a third nitrogen purge pipeline, and a third nitrogen purge valve arranged on the nitrogen purge pipeline, and the third nitrogen purge pipeline is set on the fourth double A gate valve and a third shut-off valve, and the third nitrogen purge pipeline communicates with the high-pressure, high-explosive, low-temperature gas delivery pipeline; 所述均压组件包括均压管路和均压阀,所述均压阀设于所述均压管路上,所述均压管路的两端分别设置于所述第四双闸板闸阀的两侧;The pressure equalization assembly includes a pressure equalization pipeline and a pressure equalization valve, the pressure equalization valve is arranged on the pressure equalization pipeline, and the two ends of the pressure equalization pipeline are respectively arranged on the ends of the fourth double gate valve. both sides; 所述蒸汽输送组件包括蒸汽输送管路和蒸汽调节阀,所述蒸汽调节阀设置于所述蒸汽输送管路上,所述蒸汽输送管路与所述高压强爆炸性低温煤气管路相连通。The steam conveying assembly includes a steam conveying pipeline and a steam regulating valve, the steam regulating valve is arranged on the steam conveying pipeline, and the steam conveying pipeline communicates with the high-pressure, high-explosive, low-temperature gas pipeline. 12.根据权利要求2所述的煤气加热装置,其特征在于,所述高压强爆炸性高温煤气输送机构包括所述高压强爆炸性高温煤气输送管路和高压强爆炸性高温煤气阀,所述高压强爆炸性高温煤气阀设置于所述高压强爆炸性高温煤气输送管路上,所述高压强爆炸性高温煤气输送管路的一端与高压强爆炸性高温煤气相连通,所述高压强爆炸性高温煤气输送管路的另一端与所述蓄热式加热炉相连通。12. The gas heating device according to claim 2, characterized in that, the high-pressure explosive high-temperature gas delivery mechanism comprises the high-pressure explosive high-temperature gas delivery pipeline and a high-pressure explosive high-temperature gas valve, and the high-pressure explosive high-temperature gas valve The high-temperature gas valve is set on the high-pressure and explosive high-temperature gas delivery pipeline, one end of the high-pressure and explosive high-temperature gas delivery pipeline communicates with the high-pressure and high-temperature explosive gas delivery pipeline, and the other end of the high-pressure and explosive high-temperature gas delivery pipeline It communicates with the regenerative heating furnace. 13.根据权利要求1所述的煤气加热装置,其特征在于,所述换热机构包括第一换热器和第二换热器,所述第一换热器串联于所述烧炉煤气输送总管路与所述烟气输送总管路上,所述第二换热器串联于所述助燃空气输送总管路与所述烟气输送总管路上。13. The gas heating device according to claim 1, characterized in that the heat exchange mechanism includes a first heat exchanger and a second heat exchanger, and the first heat exchanger is connected in series to the furnace gas delivery The main pipeline is connected to the main flue gas delivery pipeline, and the second heat exchanger is connected in series to the main combustion air delivery pipeline and the main flue gas delivery pipeline. 14.根据权利要求1所述的煤气加热装置,其特征在于,所述蓄热式加热炉为2-4座。14. The gas heating device according to claim 1, characterized in that there are 2-4 regenerative heating furnaces. 15.一种煤气加热方法,应用于如权利要求1-14任意一项所述的煤气加热装置中,其特征在于,包括闷炉转烧炉模式、烧炉转闷炉模式、闷炉转送风模式和送风转闷炉模式,所述闷炉转烧炉模式、所述烧炉转闷炉模式、所述闷炉转送风模式和所述送风转闷炉模式之间能够相互切换;15. A coal gas heating method, which is applied to the gas heating device as claimed in any one of claims 1-14, characterized in that it includes the mode of turning the furnace into a furnace, the mode of turning a furnace into a furnace, and the mode of transferring a furnace into a furnace. Wind mode and air supply to furnace mode, the furnace to furnace mode, the furnace to furnace mode, the furnace to air mode and the air supply to furnace mode can be switched to each other ; 所述闷炉转烧炉模式为:The mode of the smoldering furnace-to-sintering furnace is: S100:开启废气调节阀,开启废气阀,使得蓄热式加热炉内的高压强爆炸性高温煤气放散,直至所述蓄热式加热炉内的压力达到预设压力值;S100: Open the waste gas regulating valve, open the waste gas valve, so that the high-pressure strong explosive high-temperature gas in the regenerative heating furnace is released until the pressure in the regenerative heating furnace reaches a preset pressure value; S200:关闭第一氮气吹扫阀,开启第一放散阀,将所述蓄热式加热炉内的压力进行卸载;S200: closing the first nitrogen purge valve, opening the first relief valve, and unloading the pressure in the regenerative heating furnace; S300:开启烧炉煤气输送支管路上的第一双闸板闸阀,保持第一切断阀关闭,开启第一氮气吹扫阀,对所述蓄热式加热炉内的高压强爆炸性高温煤气吹扫置换,直至所述烟气输送支管路内的一氧化碳含量达标,放散完成;S300: Open the first double gate valve on the furnace gas delivery branch pipeline, keep the first cut-off valve closed, open the first nitrogen purge valve, and purge and replace the high-pressure, explosive, and high-temperature gas in the regenerative heating furnace , until the carbon monoxide content in the flue gas conveying branch pipeline reaches the standard, and the emission is completed; S400:开启烧炉煤气输送支管路第一双闸板闸阀,开启第一切断阀,开启第一调节阀,关闭第一氮气吹扫阀,关闭第一放散阀,同时开启助燃空气支管路上的第二双闸板闸阀,开启第二切断阀,开启第二调节阀,关闭第二氮气吹扫阀,关闭第二放散阀,使得烧炉煤气通过第一换热器进入蓄热式加热炉,使得助燃空气通过第二换热器进入蓄热式加热炉,使得所述蓄热式加热炉进入燃烧状态;S400: Open the first double gate valve of the furnace gas delivery branch pipeline, open the first cut-off valve, open the first regulating valve, close the first nitrogen purge valve, close the first relief valve, and open the first combustion air branch pipeline at the same time Two double gate valves, open the second cut-off valve, open the second regulating valve, close the second nitrogen purge valve, close the second relief valve, so that the furnace gas enters the regenerative heating furnace through the first heat exchanger, so that Combustion-supporting air enters the regenerative heating furnace through the second heat exchanger, so that the regenerative heating furnace enters a combustion state; 所述烧炉转闷炉模式为:The mode of turning the furnace into a furnace is as follows: 关闭第一调节阀、关闭第一切断阀,关闭第二调节阀,关闭第二切断阀,保持第一双闸板闸阀开启,保持第二双闸板闸阀开启,开启第一氮气吹扫阀,开启第二氮气吹扫阀,对所述烧炉煤气输送支管路和所述助燃空气支管路进行吹扫,同时开启第四氮气吹扫阀和第五氮气吹扫阀,当第一预设时间后,所述关闭第一双闸板闸板和所述第二双闸板闸阀,当第二预设时间后,关闭烧炉煤气输送支管路第一氮气吹扫阀,开启第一放散阀;关闭助燃空气支管路第二氮气吹扫阀,开启第二放散阀,同时关闭烟气输送支管路上的双闸板闸阀,所述蓄热式加热炉由烧炉转为闷炉;Close the first regulating valve, close the first shut-off valve, close the second regulating valve, close the second shut-off valve, keep the first double gate valve open, keep the second double gate valve open, open the first nitrogen purge valve, Open the second nitrogen purge valve to purge the furnace gas delivery branch pipeline and the combustion air branch pipeline, and open the fourth nitrogen purge valve and the fifth nitrogen purge valve at the same time, when the first preset time Afterwards, the first double gate gate valve and the second double gate gate valve are closed, and after the second preset time, the first nitrogen purge valve of the furnace gas delivery branch pipeline is closed, and the first relief valve is opened; Close the second nitrogen purge valve of the combustion-supporting air branch pipeline, open the second relief valve, and close the double gate valve on the flue gas delivery branch pipeline at the same time, and the regenerative heating furnace is converted from a burning furnace to a stuffy furnace; 所述闷炉转送风工作模式为:The working mode of the stuffy furnace transfer air supply is: 开启第三切断阀,开启第三氮气吹扫阀,对高压强爆炸性低温煤气输送管路进行氮气吹扫,吹扫完毕后,关闭第三氮气吹扫阀;Open the third cut-off valve, open the third nitrogen purge valve, and carry out nitrogen purge on the high-pressure strong explosive low-temperature gas delivery pipeline. After the purge is completed, close the third nitrogen purge valve; 开启均压阀,当所述蓄热式加热炉内的压力达到预设压力值时,关闭均压阀,开启第四双闸板闸阀,将高压强爆炸性高温煤气输送管路送入所述蓄热式加热炉内;Open the pressure equalizing valve, when the pressure in the regenerative heating furnace reaches the preset pressure value, close the pressure equalizing valve, open the fourth double gate valve, and send the high-pressure, explosive and high-temperature gas pipeline into the storage In a heating furnace; 所述送风转闷炉的工作模式为:The working mode of described air-supply rotary furnace is: 关闭高压强爆炸性高温煤气阀,第四双闸板闸阀和第三切断阀,开启第三氮气吹扫阀,所述蓄热式加热炉由送风转为闷炉模式。Close the high-pressure strong explosive high-temperature gas valve, the fourth double gate valve and the third cut-off valve, open the third nitrogen purge valve, and the regenerative heating furnace changes from air supply to stuffy furnace mode.
CN202211502195.0A 2022-11-28 2022-11-28 Gas heating device and method Pending CN115751318A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202211502195.0A CN115751318A (en) 2022-11-28 2022-11-28 Gas heating device and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202211502195.0A CN115751318A (en) 2022-11-28 2022-11-28 Gas heating device and method

Publications (1)

Publication Number Publication Date
CN115751318A true CN115751318A (en) 2023-03-07

Family

ID=85339378

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202211502195.0A Pending CN115751318A (en) 2022-11-28 2022-11-28 Gas heating device and method

Country Status (1)

Country Link
CN (1) CN115751318A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1088245A (en) * 1996-09-06 1998-04-07 Kawasaki Steel Corp Continuous heat treatment apparatus of metallic strip
CN102784605A (en) * 2012-08-09 2012-11-21 攀钢集团攀枝花钢铁研究院有限公司 Method for preventing coal gas from being coked during preheating
CN102952913A (en) * 2012-11-12 2013-03-06 鞍钢集团工程技术有限公司 Dual-preheating method and device for preheating blast furnace gas by using heat-storage-type preheating furnace
CN106967861A (en) * 2017-05-26 2017-07-21 中冶京诚工程技术有限公司 Time-sharing preheating system for combustion air of hot blast stove
CN112342332A (en) * 2020-10-22 2021-02-09 马鞍山钢铁股份有限公司 Ignition heat preservation and inverse air supply integrated system for hot blast stove and operation method
CN213113384U (en) * 2020-07-03 2021-05-04 中钢设备有限公司 Blast furnace damping down coal gas recovery system
CN114317853A (en) * 2022-01-17 2022-04-12 新疆八一钢铁股份有限公司 Based on 2500m3Heating method for high-temperature gas by carbon circulation injection of blast furnace gas

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1088245A (en) * 1996-09-06 1998-04-07 Kawasaki Steel Corp Continuous heat treatment apparatus of metallic strip
CN102784605A (en) * 2012-08-09 2012-11-21 攀钢集团攀枝花钢铁研究院有限公司 Method for preventing coal gas from being coked during preheating
CN102952913A (en) * 2012-11-12 2013-03-06 鞍钢集团工程技术有限公司 Dual-preheating method and device for preheating blast furnace gas by using heat-storage-type preheating furnace
CN106967861A (en) * 2017-05-26 2017-07-21 中冶京诚工程技术有限公司 Time-sharing preheating system for combustion air of hot blast stove
CN213113384U (en) * 2020-07-03 2021-05-04 中钢设备有限公司 Blast furnace damping down coal gas recovery system
CN112342332A (en) * 2020-10-22 2021-02-09 马鞍山钢铁股份有限公司 Ignition heat preservation and inverse air supply integrated system for hot blast stove and operation method
CN114317853A (en) * 2022-01-17 2022-04-12 新疆八一钢铁股份有限公司 Based on 2500m3Heating method for high-temperature gas by carbon circulation injection of blast furnace gas

Similar Documents

Publication Publication Date Title
CN110513687A (en) Biomass high temperature gasification and low nitrogen combustion comprehensive utilization system
CN102563857A (en) Process and device for heating gas by using a heat accumulation type heating furnace
CN102952913A (en) Dual-preheating method and device for preheating blast furnace gas by using heat-storage-type preheating furnace
CN101285576A (en) Low calorific value gas high temperature air combustion system and method
CN106051774A (en) Intelligent continuous heat-accumulating combustion device and control method thereof
CN112342332B (en) Ignition heat preservation and inverse air supply integrated system for hot blast stove and operation method
CN201305608Y (en) Hot stove cascade preheating system
CN115094179B (en) A system and method for recycling waste gas from hot blast stove replacement
CN202066197U (en) Heat accumulating type heating furnace capable of heating methane gas
CN115751318A (en) Gas heating device and method
WO2024198434A1 (en) Multi-fuel quick-switch regenerative combustion system and operation method therefor
CN218620905U (en) Hot-blast furnace trades stove waste gas recycle system
CN201237219Y (en) Pre-heating combustion device of torpedo tank truck
CN104988266B (en) Shared hot-air furnace system for blast furnace and use method thereof
CN204648986U (en) A kind of board-like pair of preheater process system for gas burning lime kiln
CN209782692U (en) A kind of biomass fuel split type baking equipment
CN106016269A (en) Continuous regenerative combustion device
CN221217826U (en) Blast furnace heating system
CN215864638U (en) Sintering system
CN202056884U (en) Air preheating type burner
CN205979792U (en) Continuous heat accumulation burner
CN206736291U (en) Time-sharing preheating system for combustion air of hot blast stove
CN206280959U (en) A kind of heat accumulating type multitubular bundles radiant tube combustion device
CN114777334B (en) Combined gas heating system and heating method
CN221611602U (en) High-temperature preheating device for coal gas

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20230307