CN211425094U - Electric furnace flue gas waste heat utilization system - Google Patents
Electric furnace flue gas waste heat utilization system Download PDFInfo
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- CN211425094U CN211425094U CN201922461217.3U CN201922461217U CN211425094U CN 211425094 U CN211425094 U CN 211425094U CN 201922461217 U CN201922461217 U CN 201922461217U CN 211425094 U CN211425094 U CN 211425094U
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Abstract
The utility model relates to a steelmaking technical field provides an electric stove flue gas waste heat utilization system, including the heating device who is arranged in handling the carbon monoxide in the flue gas, be used for carrying out waste heat recovery's first heat recovery device for the first time, be used for the process flue gas after the cooling of first heat recovery device carries out the flue gas purification device who purifies and is used for the process flue gas purification device purifies carries out waste heat recovery's second heat recovery device for the second time, heating device first heat recovery device flue gas purification device and second heat recovery device communicates through the pipeline in proper order. The utility model discloses a change the processing step to the flue gas among the prior art, can carry out waste heat recovery twice, rationally retrieve the energy of wasting among the current flue gas treatment process, make full use of chemical heat.
Description
Technical Field
The utility model relates to a steelmaking technical field specifically is an electric stove flue gas waste heat utilization system.
Background
The scrap steel is a raw material for electric furnace steel making, and the common scrap steel contains chlorine-containing organic matters such as plastics, grease and the like, and when the scrap steel is put into an electric furnace for scrap steel preheating, smoke containing dioxin is generated.
At present, the technology for preventing and treating dioxin pollution in electric furnace flue gas after waste steel preheating is high-temperature oxidation and flue gas quenching, namely, the flue gas after waste steel preheating is added with fuel gas for combustion, the flue gas is kept to stay for more than 2s at the temperature of more than 850 ℃, dioxin and other organic matters can be decomposed at high temperature, and then the flue gas with the temperature of more than 850 ℃ is rapidly cooled to be below 200 ℃ in 2-3 s, so that the generation of dioxin is reduced to the maximum extent. A certain amount of coal gas is consumed for high-temperature oxidation, water is consumed for flue gas quenching, and flue gas waste heat is not recycled, so that the emission reduction effect is achieved, but energy is not saved.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an electric stove flue gas waste heat utilization system through changing the processing step to the flue gas among the prior art, can carry out waste heat recovery twice, has rationally retrieved the energy of wasting among the current flue gas treatment process, make full use of chemical heat.
In order to achieve the above object, the embodiment of the present invention provides the following technical solutions: the utility model provides an electric stove flue gas waste heat utilization system, is including the heating device that is arranged in handling the carbon monoxide in the flue gas, be used for carrying out the first heat recovery device of waste heat recovery for the first time, be used for the process flue gas after the cooling of first heat recovery device carries out the flue gas purification device that purifies and is used for the process flue gas after the purification device purifies carries out the second heat recovery device of waste heat recovery for the second time, heating device first heat recovery device flue gas purification device and second heat recovery device communicates through the pipeline in proper order.
Further, the heating device is a scrap steel preheating device, and a mixed air valve is installed on the scrap steel preheating device.
Further, first heat reclamation device is waste heat reclamation device, waste heat reclamation device includes horizontally arranged's radiation room and convection chamber, the radiation room with the convection chamber communicates in proper order along the fashion of flue gas.
Furthermore, a membrane type water-cooling wall is arranged in the radiation chamber, a coiled tube evaporation tube bundle is arranged in the convection chamber, and the coiled tube evaporation tube bundle is longitudinally arranged.
Further, the flue gas purification device is a catalyst-carrying flue gas filter, and the catalyst-carrying flue gas filter is provided with catalyst particles capable of performing catalytic degradation on dioxin.
Further, the heat recovery device for the second waste heat recovery is a heat exchanger.
Further, the second heat recovery device is communicated with a fan.
Further, the fan is communicated with a chimney.
Compared with the prior art, the beneficial effects of the utility model are that:
1. by changing the treatment steps of the flue gas in the prior art, the waste heat recovery can be carried out twice, the energy wasted in the existing flue gas treatment process is reasonably recovered, and the waste heat of the flue gas of the electric furnace at 1200-1600 ℃ and the chemical heat of CO in the flue gas are fully utilized.
2. The dioxin in the flue gas can be thoroughly removed through high-temperature combustion and catalytic degradation, no secondary pollution is caused, the catalyst can be used for a long time, and the operation cost is low.
3. The emission reduction of dioxin is realized while the waste heat of the flue gas of the electric furnace is utilized, and the energy conservation and emission reduction are really realized.
Drawings
Fig. 1 is a flow chart of an electric furnace flue gas waste heat utilization system provided by the embodiment of the present invention;
in the reference symbols: 1-an electric furnace; 2-scrap steel preheating device; 3-a waste heat recovery device; 4-a flue gas purification device; 5-a heat exchanger; 6, a fan; 7-chimney.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
The first embodiment is as follows:
referring to fig. 1, an embodiment of the present invention provides an electric furnace flue gas waste heat utilization system, including a heating device for treating carbon monoxide in flue gas, a first heat recovery device for performing first waste heat recovery, a flue gas purification device 4 for purifying flue gas cooled by the first heat recovery device, and a second heat recovery device for performing second waste heat recovery on flue gas purified by the flue gas purification device 4, wherein the heating device, the first heat recovery device, the flue gas purification device 4, and the second heat recovery device are sequentially communicated through a pipeline. In the prior art, high-temperature oxidation and flue gas quenching are mostly adopted for treatment of dioxin, fuel gas combustion needs to be consumed in the high-temperature oxidation process, the rapid cooling process is too late to recover heat, and the waste of energy consumption is very large, so in order to avoid the situation, the embodiment changes the treatment step of the flue gas in the prior art, and the waste heat of the flue gas of the electric furnace is recovered in stages, wherein the waste steel can be preheated by using the heat in a waste steel preheating device, the waste heat is utilized for the second time in a waste heat recovery device, and finally, the waste heat is utilized for the third time in a heat exchanger, so that the energy wasted in the prior flue gas treatment process is reasonably recovered, and the waste heat of the flue gas of the electric furnace at 1200-plus 1600 ℃ and the chemical heat of CO in the flue gas are fully utilized. The specific method comprises the steps of firstly guiding high-temperature flue gas generated by smelting in the electric furnace 1 into a heating device to remove carbon monoxide in the flue gas, then guiding the flue gas with the carbon monoxide removed to a first heat recovery device to carry out first waste heat recovery so as to obtain flue gas with reduced temperature, then guiding the flue gas with the reduced temperature to a flue gas purification device 4 to purify dioxin and obtain clean flue gas, finally guiding the clean flue gas to a second heat recovery device to carry out second waste heat recovery, and discharging the flue gas after the waste heat recovery is finished, so that the dioxin is treated, the waste heat recovery is carried out for multiple times in the whole system, the waste heat in the prior art can be recovered to the maximum extent, the emission reduction effect is achieved, energy is saved, and energy saving and emission reduction is really realized.
As an optimization scheme of the embodiment of the present invention, please refer to fig. 1, the heating device is a scrap steel preheating device 2, and a mixed air valve is installed on the scrap steel preheating device 2. In this embodiment, heating device is scrap steel preheating device 2, adopts scrap steel preheating device 2 preheats the scrap steel to realize the waste heat utilization for the first time, and adopt the air mixing valve on the scrap steel preheating device 2 to mix the air that supplies the carbon monoxide burning in the scrap steel preheating device 2, can handle CO. The scrap steel preheating device 2 is common equipment in the field, waste heat of flue gas is utilized to heat scrap steel in a mode that the flue gas penetrates through the scrap steel, air is mixed in the flue gas by matching with an air mixing valve, and then CO in the flue gas can be combusted.
As the embodiment of the utility model discloses an optimization scheme please refer to fig. 1, first heat recovery unit is waste heat recovery unit 3, waste heat recovery unit 3 includes horizontally arranged's radiation room and convection chamber, the radiation room with the convection chamber communicates in proper order along the popularity of flue gas. In this embodiment, the heat recovery device performing the first waste heat recovery is the waste heat recovery device 3, the waste heat recovery device 3 performs waste heat recovery by using the radiation chamber and the convection chamber which are horizontally arranged, wherein the water cooling wall of the radiation chamber forms a heating surface, and after absorbing most of heat, the flue gas enters the convection chamber again to absorb the residual heat for the second time. Preferably, the water wall in the radiation chamber is a membrane water wall, the coiled tube evaporator tube bundle is arranged in the convection chamber and is longitudinally arranged, and the coiled tube evaporator tube bundle are all of the existing structures, so that the specific structure of the coiled tube evaporator tube bundle is not detailed, and an actual structure diagram is not given.
As an optimization scheme of the embodiment of the present invention, please refer to fig. 1, the flue gas purification device 4 is a flue gas filter with catalyst, and the flue gas filter with catalyst has catalyst particles capable of performing catalytic degradation on dioxin. In this embodiment, the flue gas purification device 4 is a flue gas filter with a catalyst, and catalyst particles in the flue gas filter with the catalyst can catalyze and degrade dioxin in flue gas. The catalyst-containing flue gas filter can be of a filter element type or a filler type, and catalyst particles are mixed in the filter element or the filler, wherein the catalyst particles are oxide powder of elements such as V, Ti or W.
As an optimized solution of the embodiment of the present invention, please refer to fig. 1, the heat recovery device for the second waste heat recovery is a heat exchanger 5. In this embodiment, the heat recovery device for recovering the waste heat for the second time is a heat exchanger 5, and the heat exchanger 5 adopts the mode of heating soft water to exchange heat. The heat exchanger 5 is also a conventional heat exchange method in the field, and the detailed working process thereof will not be described in detail here, and the detailed structural form diagram thereof is also omitted in the drawings.
As an optimization scheme of the embodiment of the present invention, please refer to fig. 1, the second heat recovery device is communicated with a fan 6. Preferably, the fan 6 is communicated with a chimney 7. In this embodiment, the treated flue gas is finally drawn out by a fan 6 and discharged to the atmosphere through a stack 7.
Example two:
the embodiment of the utility model provides a 1 flue gas waste heat utilization method of electric stove, including following step: s1, introducing high-temperature flue gas generated by smelting the electric furnace 1 into a heating device to remove carbon monoxide in the flue gas; s2, guiding the flue gas treated with the carbon monoxide to a heat recovery device for primary waste heat recovery to obtain flue gas with reduced temperature; s3, guiding the flue gas with the reduced temperature to a flue gas purification device 4 for purifying dioxin, and obtaining clean flue gas; and S4, guiding the clean flue gas to a heat recovery device for secondary waste heat recovery, and discharging the flue gas after the waste heat recovery. In the embodiment, the flue gas waste heat of the electric furnace is recycled in a grading manner by changing the treatment steps of the flue gas in the prior art, wherein the waste steel can be preheated by using heat in the waste steel preheating device, the waste heat is recycled for the second time in the waste heat recycling device, and finally the waste heat is recycled for the third time in the heat exchanger, so that the energy wasted in the existing flue gas treatment process is reasonably recycled, and the flue gas waste heat of the electric furnace at 1200-1600 ℃ and the chemical heat of CO in the flue gas are fully utilized.
As an optimization scheme of the embodiment of the present invention, please refer to fig. 1, in the step S1, the heating device is the scrap preheating device 2, the scrap preheating device 2 is adopted to preheat the scrap, and the scrap preheating device 2 is provided with the air mixing valve to mix the air for carbon monoxide combustion into the scrap preheating device 2.
As for other components and methods for using the components of the method, please refer to the first embodiment, which will not be described in detail herein.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (8)
1. The utility model provides an electric stove flue gas waste heat utilization system which characterized in that: including the heating device who is arranged in handling the carbon monoxide in the flue gas, be used for carrying on waste heat recovery's first heat recovery unit for the process flue gas after the cooling of first heat recovery unit carries out the gas cleaning device who purifies and is used for the process flue gas after the gas cleaning device purifies carries out the second heat recovery unit that waste heat recovery carries out the second time, heating device first heat recovery unit gas cleaning device and second heat recovery unit communicates in proper order through the pipeline.
2. The electric furnace flue gas waste heat utilization system of claim 1, characterized in that: the heating device is a scrap steel preheating device, and the scrap steel preheating device is provided with an air mixing valve.
3. The electric furnace flue gas waste heat utilization system of claim 1, characterized in that: the first heat recovery device is a waste heat recovery device, the waste heat recovery device comprises a radiation chamber and a convection chamber which are horizontally arranged, and the radiation chamber and the convection chamber are sequentially communicated along the circulation of flue gas.
4. The electric furnace flue gas waste heat utilization system of claim 3, characterized in that: the indoor membrane water-cooling wall that is equipped with of radiation, be equipped with coiled pipe evaporation tube bank in the convection chamber, coiled pipe evaporation tube bank longitudinal arrangement.
5. The electric furnace flue gas waste heat utilization system of claim 1, characterized in that: the flue gas purification device is a catalyst-carrying flue gas filter, and the catalyst-carrying flue gas filter is provided with catalyst particles capable of performing catalytic degradation on dioxin.
6. The electric furnace flue gas waste heat utilization system of claim 1, characterized in that: the heat recovery device for the secondary waste heat recovery is a heat exchanger.
7. The electric furnace flue gas waste heat utilization system of claim 1, characterized in that: the second heat recovery device is communicated with a fan.
8. The electric furnace flue gas waste heat utilization system of claim 7, characterized in that: the fan is communicated with a chimney.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922461217.3U CN211425094U (en) | 2019-12-31 | 2019-12-31 | Electric furnace flue gas waste heat utilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922461217.3U CN211425094U (en) | 2019-12-31 | 2019-12-31 | Electric furnace flue gas waste heat utilization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211425094U true CN211425094U (en) | 2020-09-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201922461217.3U Active CN211425094U (en) | 2019-12-31 | 2019-12-31 | Electric furnace flue gas waste heat utilization system |
Country Status (1)
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|---|---|
| CN (1) | CN211425094U (en) |
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2019
- 2019-12-31 CN CN201922461217.3U patent/CN211425094U/en active Active
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