阅读说明：本技术 一种高炉并罐布料残余煤气环保回收工艺方法 (Environment-friendly recovery process method for residual gas generated in material distribution of blast furnace in parallel tanks ) 是由 魏红超 常李 李超想 杜友尧 陆益飞 项旭江 黄军 王加林 于 2021-07-02 设计创作，主要内容包括：本发明涉及煤气环保回收工艺领域,公开了一种高炉并罐布料残余煤气环保回收工艺方法,所述的高炉并罐布料残余煤气环保回收工艺方法包括首先对高炉均压放散出的煤气进行旋风一次除尘,其次再经过布袋除尘器后进行二次除尘,净煤气进入煤气管网,实现了对高炉煤气均压放散过程中所有高炉煤气的全部回收。本发明的环保回收工艺方法解决了高炉煤气在均压放散过程中不能全部回收的技术问题,成功使得整个过程煤气不再进行外排,将高炉布料时对均压放散过程中的煤气实现全部回收进入煤气管网,改变了几十年来残余煤气自然放散的方式,大大降低了环境污染,实现了企业的节能减排和能源的回收再利用。(The invention relates to the field of a coal gas environment-friendly recovery process, and discloses a blast furnace tank-connected distribution residual coal gas environment-friendly recovery process method. The environment-friendly recovery process method solves the technical problem that the blast furnace gas cannot be completely recovered in the pressure-equalizing and bleeding process, successfully prevents the gas from being discharged outside in the whole process, realizes the complete recovery of the gas in the pressure-equalizing and bleeding process when the blast furnace is distributed, and enters a gas pipe network, thereby changing the natural bleeding mode of residual gas for decades, greatly reducing the environmental pollution, and realizing the energy conservation and emission reduction of enterprises and the recovery and reutilization of energy.)

1. The environment-friendly recovery process method for the residual gas of the material distribution of the blast furnace and the tank is characterized by comprising the following specific process steps of firstly carrying out cyclone primary dust removal on the gas discharged by the blast furnace under the uniform pressure, secondly carrying out secondary dust removal after the gas passes through a bag-type dust remover, enabling the clean gas to enter a gas pipe network, and realizing the complete recovery of all blast furnace gas in the uniform pressure and discharge process of the blast furnace gas, wherein the environment-friendly recovery process method for the residual gas of the material distribution of the blast furnace and the tank comprises the following specific process steps:

(1) pressure equalizing process

The primary pressure equalizing adopts blast furnace semi-clean gas pressure equalizing, and the secondary pressure equalizing adopts a nitrogen pressure equalizing distribution mode;

(2) dust removal processing mode

Primary dust removal: closing the west butterfly valve (4) and the east butterfly valve (5), isolating the gas from an external discharge pipeline, and carrying out primary coarse dust removal on the gas in the blast furnace side charging bucket (22) through a cyclone dust collector (6);

secondary dust removal: after coarse dust removal, the dust is alternately recycled through the west blow-off valve (2) or the east blow-off valve (3), and then secondary fine dust removal is carried out through a bag-type dust remover (16) through a furnace top recycling blind plate valve (7), a full recycling ejector (10), a bag inlet butterfly valve (11) and a bag inlet blind plate valve (13) in sequence;

(3) gas recovery mode

And (3) at the initial stage of recovery: because the pressure in the blast furnace side charging bucket (22) is higher when the diffusion starts, when the pressure is more than 180KPa, the coal gas can automatically enter a coal gas pipe network (19) for natural recovery;

and (3) in the later recovery stage: when the pressure of the blast furnace side charging bucket (22) is reduced to 180KPa, opening an ejector full-recovery equalizing valve (8), starting a full-recovery ejector (10), under the ejection action of high-pressure working fluid, quickly ejecting residual coal gas of the blast furnace side charging bucket (22) to a blast furnace coal gas pipe network, and stopping ejection to finish the diffusion process when the pressure in the blast furnace side charging bucket (22) is less than 10 KPa;

and (3) during a material loading period: when the gas diffusion is finished, the blast furnace side charging bucket (22) enters a to-be-charged state, the two charging buckets alternately and circularly recover residual gas in a normal state, and when one side charging bucket is in a fault state, the gas recovery of the single side charging bucket can be realized;

(4) fault state handling

When equipment fails in the using process, automatic switching can be performed, the west butterfly valve (4) and the east butterfly valve (5) are opened, and the normal operation of the blast furnace and the safe production are not influenced;

(5) maintenance treatment mode

When the blast furnace stops blowing or a system fails, the connection with an external gas pipe network (19) is isolated by closing a blind valve (18) at the inlet of a clean gas pipe network, so that the gas is prevented from flowing backwards, and the blast furnace can be smoothly overhauled; the bag-type dust remover (16) is isolated from the system by closing the bag inlet blind plate valve (13), the bag outlet blind plate valve (14) and the bag outlet butterfly valve (15), so that secondary bag-type dust removal maintenance is facilitated, and the recovery system is directly in a bypass mode by opening the bag bypass valve (12), so that the normal use of the system is ensured; when the full-recovery ejector (10) needs to be overhauled, the gas replacement purging is qualified after the furnace top recovery blind plate valve (7), the ejector blind plate valve (9) and the clean gas pipe network inlet blind plate valve (18) are closed, and the full-recovery ejector (10) can enter an overhauling mode.

2. The environment-friendly recovery process method of residual gas from parallel distribution and distribution of blast furnace according to claim 1, characterized in that in the primary dust removal process in step (2), the fly ash is gathered at the bottom of the cyclone dust collector, and the fly ash is swept to the side charging bucket (22) of the blast furnace in the process of distributing and pressure equalizing of the blast furnace by periodically and intermittently opening the ash discharge valve (1), and then the fly ash is treated in the distribution process entering the furnace without extra treatment.

3. The environment-friendly recovery process method of the residual gas from the parallel tank material distribution of the blast furnace as claimed in claim 1, wherein in the secondary dust removal process in the step (2), secondary dust removal is performed by a bag-type dust remover (16), and the dust removed is discharged to an ash conveyer (17) of the gravity dust remover of the blast furnace through a bag-type ash discharge valve (21) to be collected, sintered and recycled.

4. The environment-friendly recovery process method of the residual gas from the material distribution in the blast furnace and the material tank of the blast furnace as claimed in claim 1, wherein in the initial recovery stage in the step (3), the primary recovery can be directly carried out when the pressure in the tank is more than 180 KPa.

5. The environment-friendly recovery process method of the residual gas from the parallel distribution of the blast furnace and the distribution of the blast furnace according to claim 1, characterized in that in the recovery later stage in the step (3), the pressure in the side charging bucket (22) of the blast furnace is gradually reduced, when the pressure in the charging bucket is lower than 180KPa, the full recovery ejector (10) is involved, the high-pressure semi-clean gas on the side of the blast furnace is used as the power of the ejector for ejecting and recovering the residual gas by utilizing the ejector principle, and other additional gas media are not needed in the whole recovery process.

Technical Field

The invention belongs to the field of coal gas environment-friendly recovery processes, and particularly relates to a blast furnace charging bucket uniform diffusion, a blast furnace material distribution system and a residual coal gas environment-friendly recovery process method.

Background

The bell-less top equipment of blast furnace consists of material tank, upper sealing valve, lower sealing valve, material flow valve, complete airtight box and material distributor. In the traditional material distribution system and the blast furnace, in the iron-making production process, the blast furnace pressure-equalizing gas bleeding system is switched on and off once when a batch of mineral materials are put into the blast furnace, so that the pressure difference between the inside of the blast furnace and a blast furnace charging bucket is balanced, and the mineral materials can smoothly enter the blast furnace. When the material distribution of the charging bucket is finished, the blast furnace gas in the charging bucket needs to be discharged to be in a normal pressure state, the mineral aggregate in the next batch can be charged again, and the blast furnace gas is directly discharged in a mode of diffusing and discharging.

Blast furnace gas is a byproduct of iron and steel metallurgy enterprises and also an indispensable energy source in the production of the iron and steel enterprises, and the blast furnace pressure-equalizing and bleeding directly causes environmental pollution and is also a waste of energy sources in an air discharge mode, thereby being not beneficial to energy conservation and emission reduction of the enterprises. In the face of the current trends of environmental protection, energy conservation, emission reduction, cost reduction and efficiency improvement, the original mode that the pressure-equalizing coal gas in the furnace top charging bucket is directly discharged into the atmosphere after passing through a silencer in the material distribution process of the blast furnace has been under great pressure in practical application. A2680 blast furnace adopted in an enterprise uses a material tank and tank combination mode, two material tanks are circularly and alternately carried out, the volume of a single material tank is 45m, and the air discharge is about empty every shift (8 hours)The blast furnace gas with the pressure of 220KPa in the 110 tanks is dispersed, and the blast furnace gas contains a great deal of dust, CO and CO in the dispersion process₂And moisture and the like directly cause pollution of a blast furnace production area and stable operation of equipment in a furnace top area, and the original air discharge mode is difficult to adapt to the current production situation.

The invention discloses an environment-friendly recovery process method for residual gas generated by material distribution of a blast furnace in a parallel tank, wherein the gas is not discharged in the whole process, so that the gas is completely recovered and enters a gas pipe network in the uniform pressure diffusion process when the blast furnace is distributed, the natural diffusion mode of the residual gas for decades is changed, the environmental pollution is greatly reduced, and the energy conservation and emission reduction of enterprises and the recovery and reutilization of energy are realized.

Disclosure of Invention

The invention provides an environment-friendly recovery process method of residual gas from the material distribution of a blast furnace, which comprises the steps of performing cyclone primary dust removal on the gas discharged from the blast furnace under the uniform pressure, performing secondary dust removal after the gas passes through a bag-type dust remover, and enabling the purified gas to enter a gas pipe network. The technical problem that the blast furnace gas can not be completely recovered in the pressure-equalizing and diffusing process is solved, and the resource recovery and the cyclic utilization of the blast furnace gas are realized, so that the gas is not discharged outside any more.

In order to solve the technical problems, the invention provides an environment-friendly recovery process method of residual gas generated in the process of material distribution of a blast furnace, which comprises the steps of performing cyclone primary dust removal on the gas discharged from the blast furnace under the uniform pressure, performing secondary dust removal after the gas passes through a bag-type dust remover, and enabling the clean gas to enter a gas pipe network to realize the complete recovery of all blast furnace gas in the uniform pressure discharge process of the blast furnace gas.

The environment-friendly recovery process method for the residual gas from the material distribution of the parallel tanks of the blast furnace comprises the following specific process steps:

(1) pressure equalizing process

The primary pressure equalizing adopts blast furnace semi-clean gas pressure equalizing, and the secondary pressure equalizing adopts a nitrogen pressure equalizing distribution mode;

(2) dust removal processing mode

Primary dust removal: closing the west butterfly valve and the east butterfly valve, isolating the gas from an external discharge pipeline, and carrying out primary coarse dust removal on the gas in the charging bucket on the side of the blast furnace through a cyclone dust collector;

secondary dust removal: after coarse dust removal, alternately and circularly recovering the dust through two sides of a west blow-off valve or an east blow-off valve, and then sequentially performing secondary fine dust removal through a furnace top recovery blind plate valve, a full recovery ejector, a cloth bag inlet butterfly valve and a cloth bag inlet blind plate valve by a cloth bag dust remover;

(3) gas recovery mode

And (3) at the initial stage of recovery: because the diffusion is started, the pressure in the charging bucket at the side of the blast furnace is higher, and when the pressure is more than 180KPa, the coal gas can automatically enter a coal gas pipe network for natural recovery;

and (3) in the later recovery stage: when the pressure of the blast furnace side charging bucket is reduced to 180KPa, opening an ejector full-recovery equalizing valve, starting a full-recovery ejector, rapidly ejecting residual coal gas of the blast furnace side charging bucket to a blast furnace gas pipe network under the ejection action of high-pressure working fluid, and stopping ejection to finish the diffusion process when the pressure in the blast furnace side charging bucket is less than 10 KPa;

and (3) during a material loading period: when the gas diffusion is finished, the blast furnace side charging bucket enters a to-be-charged state, the two charging buckets alternately and circularly recover residual gas in a normal state, and when one side charging bucket is in a fault state, the gas recovery of a single side charging bucket can be realized;

(4) fault state handling

When equipment fails in the using process, automatic switching can be performed, the west butterfly valve and the east butterfly valve are opened, and the normal operation of the blast furnace and the safe production are not influenced;

(5) maintenance treatment mode

When the blast furnace stops blowing or a system fails, the connection with an external gas pipe network is isolated by closing a blind plate valve at the inlet of a clean gas pipe network, so that the gas is prevented from flowing backwards, and the blast furnace can be smoothly overhauled; the bag-type dust remover is isolated from the system by closing the bag inlet blind plate valve, the bag outlet blind plate valve and the bag outlet butterfly valve, so that secondary bag-type dust removal maintenance is facilitated, and the recovery system is directly in a bypass mode by opening the bag bypass valve, so that the normal use of the system is ensured; when the full-recovery ejector needs to be overhauled, the furnace top recovery blind plate valve, the ejector blind plate valve and the clean gas pipe network inlet blind plate valve are closed, gas replacement purging is qualified, and the full-recovery ejector can enter an overhauling mode.

Further, step (2) in the dust removal process, the dust removal ash gathers in cyclone bottom, through setting up periodic intermittent type nature and opening the unloading valve, sweeps the dust removal ash to blast furnace side material jar at blast furnace cloth pressure-sharing in-process, and the cloth process gets into the stove and need not additionally to handle the dust removal ash thereupon.

Further, in the secondary dust removal process in the step (2), secondary dust removal is carried out through a bag-type dust remover, and the dust removal ash is discharged to an ash conveying machine of the blast furnace gravity dust remover through a bag-type ash discharge valve to be collected, sintered and recycled.

Further, in the early stage of the recovery in the step (3), the primary recovery can be directly carried out when the pressure in the tank is more than 180 KPa.

Further, in the later stage of recovery in the step (3), the pressure in the blast furnace side charging bucket is gradually reduced, when the pressure in the charging bucket is lower than 180KPa, a full-recovery ejector is involved, the high-pressure semi-clean coal gas on the blast furnace side is used as ejector power to eject for complete recovery by utilizing the ejector principle, and other additional gas media are not needed in the whole recovery process.

Compared with the prior art, the invention has the following beneficial effects:

the environment-friendly recovery process method can completely recover all blast furnace gas in the pressure-equalizing and diffusing process of the blast furnace gas, successfully prevents the gas from being discharged outside in the whole process, realizes that the gas in the pressure-equalizing and diffusing process is completely recovered and enters a gas pipe network when the blast furnace is distributed, changes the natural diffusing mode of residual gas for decades, greatly reduces the environmental pollution, and realizes the energy conservation and emission reduction of enterprises and the recycling of energy.

Drawings

FIG. 1 is a schematic system flow chart of a blast furnace parallel tank material distribution residual gas environment-friendly recovery process.

Description of reference numerals: 1. an ash discharge valve; 2. a west bleed valve; 3. an east bleed valve; 4. a western disc valve; 5. a east butterfly valve; 6. a cyclone dust collector; 7. recovering a blind plate valve from the furnace top; 8. a full recovery pressure equalizing valve; 9. an injector blind plate valve; 10. a full recovery ejector; 11. a cloth bag inlet butterfly valve; 12. a cloth bag bypass valve; 13. a bag inlet blind plate valve; 14. a bag outlet blind plate valve; 15. a cloth bag outlet butterfly valve; 16. a bag-type dust collector; 17. a blast furnace gravity dust collector ash conveyer; 18. a blind plate valve at the inlet of the clean gas pipe network; 19. a gas pipe network; 20. a primary pressure-equalizing semi-clean gas pipe; 21. a cloth bag dust discharge valve; 22. a blast furnace side charging bucket.

Detailed Description

The embodiments of the present invention will be described in further detail with reference to the accompanying drawings. The specific processes and flows described in this example are only some, but not all, examples of the invention.

The embodiment provides an environment-friendly recovery process method of residual gas generated in material distribution of a blast furnace, which comprises the steps of firstly carrying out cyclone primary dust removal on gas discharged by blast furnace pressure equalization, secondly carrying out secondary dust removal after the gas passes through a bag-type dust remover, and enabling clean gas to enter a gas pipe network to realize the complete recovery of all blast furnace gas in the pressure equalization and discharge process of the blast furnace gas. The specific process steps are as follows:

(1) pressure equalizing process

The primary pressure equalizing adopts blast furnace semi-clean gas pressure equalizing, and the secondary pressure equalizing adopts a nitrogen pressure equalizing distribution mode;

(2) dust removal processing mode

Primary dust removal: closing the west butterfly valve 4 and the east butterfly valve 5, isolating the gas from an external discharge pipeline, and carrying out primary coarse dust removal on the gas in the blast furnace side charging bucket 22 through the cyclone dust collector 6;

secondary dust removal: after coarse dust removal, alternately and circularly recovering the dust through the two sides of the west blow-off valve 2 or the east blow-off valve 3, and then sequentially performing secondary fine dust removal through a furnace top recovery blind plate valve 7, a full recovery ejector 10, a cloth bag inlet butterfly valve 11 and a cloth bag inlet blind plate valve 13 through a cloth bag dust remover 16;

(3) gas recovery mode

And (3) at the initial stage of recovery: because the pressure in the blast furnace side charging bucket 22 is higher when the diffusion starts, when the pressure is more than 180KPa, the coal gas can automatically enter a coal gas pipe network 19 for natural recovery;

and (3) in the later recovery stage: when the pressure of the blast furnace side charging bucket 22 is reduced to 180KPa, opening the ejector full-recovery equalizing valve 8, starting the full-recovery ejector 10, under the ejection action of high-pressure working fluid, quickly ejecting the residual coal gas of the blast furnace side charging bucket 22 to a blast furnace coal gas pipe network, and stopping ejection to end the diffusion process when the pressure in the blast furnace side charging bucket 22 is less than 10 KPa;

and (3) during a material loading period: when the gas diffusion is finished, the blast furnace side charging bucket 22 enters a to-be-charged state, the two charging buckets alternately and circularly recover residual gas in a normal state, and when one side charging bucket is in a fault state, the gas recovery of a single side charging bucket can be realized;

(4) fault state handling

When equipment fails in the using process, automatic switching can be performed, the west butterfly valve 4 and the east butterfly valve 5 are opened, and the normal operation and the safe production of the blast furnace are not influenced;

(5) maintenance treatment mode

When the blast furnace stops blowing or a system fails, the connection with an external gas pipe network 19 is isolated by closing a blind valve 18 at the inlet of a clean gas pipe network, so that the gas is prevented from flowing backwards, and the blast furnace can be smoothly overhauled; the bag-type dust remover 16 is isolated from the system by closing the bag inlet blind plate valve 13, the bag outlet blind plate valve 14 and the bag outlet butterfly valve 15, so that secondary bag-type dust removal maintenance is facilitated, and the recovery system is directly in a bypass mode by opening the bag bypass valve 12, so that normal use of the system is ensured; when the full-recovery injector 10 needs to be overhauled, the full-recovery injector 10 can enter an overhauling mode after the furnace top recovery blind plate valve 7, the injector blind plate valve 9 and the clean gas pipe network inlet blind plate valve 18 are closed and gas replacement purging is qualified.

Wherein, at a dust removal in-process, the dust removal ash gathering is in cyclone bottom, through setting up periodic intermittence nature and opening dust discharge valve 1, sweeps the dust removal ash to blast furnace side material jar 22 at blast furnace cloth pressure-sharing in-process, and the cloth process gets into the stove thereupon and need not additionally to handle the dust removal ash.

Further, in the secondary dust removal process, secondary dust removal is carried out through the bag-type dust remover 16, and the dust removed is discharged to the blast furnace gravity dust remover ash conveyor 17 through the bag-type ash discharge valve 21 to be collected, sintered and recycled.

Further, in the early stage of recovery, when the pressure in the tank is more than 180KPa, the primary recovery can be directly carried out.

Further, in the later stage of recovery, the pressure in the blast furnace side charging bucket 22 is gradually reduced, when the pressure in the charging bucket is lower than 180KPa, the full-recovery ejector 10 is involved, the ejector principle is utilized, high-pressure semi-clean coal gas at the blast furnace side is used as ejector power to eject for full recovery, and other additional gas media are not needed in the whole recovery process.