CN114149829A - Carbide slag powder slurrying and exhausting device and application method thereof - Google Patents
Carbide slag powder slurrying and exhausting device and application method thereof Download PDFInfo
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- CN114149829A CN114149829A CN202111403463.9A CN202111403463A CN114149829A CN 114149829 A CN114149829 A CN 114149829A CN 202111403463 A CN202111403463 A CN 202111403463A CN 114149829 A CN114149829 A CN 114149829A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10H—PRODUCTION OF ACETYLENE BY WET METHODS
- C10H15/00—Acetylene gas generators with carbide feed, with or without regulation by the gas pressure
- C10H15/14—Acetylene gas generators with carbide feed, with or without regulation by the gas pressure with feed worm or feed conveyors
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10H—PRODUCTION OF ACETYLENE BY WET METHODS
- C10H21/00—Details of acetylene generators; Accessory equipment for, or features of, the wet production of acetylene
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10H—PRODUCTION OF ACETYLENE BY WET METHODS
- C10H21/00—Details of acetylene generators; Accessory equipment for, or features of, the wet production of acetylene
- C10H21/08—Safety devices for acetylene generators
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10H—PRODUCTION OF ACETYLENE BY WET METHODS
- C10H21/00—Details of acetylene generators; Accessory equipment for, or features of, the wet production of acetylene
- C10H21/14—Ventilation means; Cooling devices
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Abstract
The invention provides a slurry melting and exhausting device for carbide slag powder and an application method thereof, wherein the slurry melting and exhausting device comprises a slurry melting device, a feeding unit and an air extracting and exhausting device; the slurry melting device comprises a shell and a stirring device arranged in the shell; the feeding unit comprises a screw feeding device and a dust removal device; the screw feeding device is arranged on the side wall of the shell, a feed opening of the screw feeding device is arranged in the shell, and the dust removal device is arranged above the feed opening; the top of the slurry melting device is provided with an inlet of an air exhaust device. The pulping and exhausting device can prevent the problems of dust dispersion, acetylene gas enrichment and the like in the pulping process, improve the production safety, and can obtain the pulp with ideal ratio by the application method; the pulping and exhausting device is simple and convenient, has low cost and has good industrial application prospect.
Description
Technical Field
The invention belongs to the technical field of environmental protection, and particularly relates to a carbide slag powder slurrying and exhausting device and an application method thereof.
Background
The carbide slag is industrial solid waste formed in the acetylene production process, the discharge amount is large, and the annual production amount of the carbide slag exceeds 3000 ten thousand tons. The chemical components of the carbide slag are mainly calcium hydroxide, and the carbide slag contains impurities such as coke particles, ferrosilicon, aluminum silicon minerals and the like, and a small amount of reducing impurities such as sulfides, phosphide and the like. Acetylene in the dry acetylene sludge exists in the forms of adsorbed acetylene, acetylene wrapped by the acetylene sludge, dissolved acetylene and the like. The calcium content in the carbide slag is high, the carbide slag can replace limestone to carry out flue gas desulfurization, acetylene in the carbide slag can escape and be enriched in the slurry melting process, and if the acetylene is excessively accumulated in a closed/semi-closed space, a large potential safety hazard can be brought to the production process; meanwhile, the carbide slag powder is scattered in the slurry melting process, so that the environmental pollution is caused. Acetylene dissipated in the slurry melting process can be collected by additionally arranging a fan, and the concentration of the acetylene in the slurry melting tank is controlled. However, in the exhaust process of the fan, the scattered carbide slag powder mixed water vapor can adhere to the pipeline and the fan impeller, and the normal operation of the equipment is seriously influenced.
CN210233453U discloses a slurry pulping machine, which comprises a feeder bin, wherein a bin vibrating device is connected to the side wall of the feeder bin, and a double-helix variable frequency feeder is arranged below the feeder bin; the device comprises a double-screw variable-frequency feeder, and is characterized in that a weighing belt feeder is arranged below the double-screw variable-frequency feeder and is connected with a weighing belt feeder motor, a pulping machine is arranged below the weighing belt feeder, and a water replenishing pipe and a liquid outlet pipe are arranged on the pulping machine. The vibration device of the pulping machine can meet the requirement of normal discharging of moisture-containing materials; the water replenishing pipe can adjust the water flow entering the pulping machine, and can ensure that the pulp with ideal ratio is obtained. However, the pulping machine does not consider the problem of the dissipation of dust and acetylene gas in the pulping process, and is not beneficial to the resource utilization of the carbide slag.
Therefore, how to provide a novel carbide slag powder slurrying and exhausting device with high safety, environmental protection and excellent dust removal and exhaust effects becomes a problem which needs to be solved by technical personnel in the field at present.
Disclosure of Invention
In view of the problems in the prior art, the invention provides a slurry dissolving and exhausting device for carbide slag powder and an application method thereof.
In order to achieve the technical effect, the invention adopts the following technical scheme:
the invention aims to provide a slurry melting and exhausting device for carbide slag powder, which comprises a slurry melting device, a feeding unit and an air exhaust device;
the slurry melting device comprises a shell and a stirring device arranged in the shell;
the feeding unit comprises a screw feeding device and a dust removal device;
the screw feeding device is arranged on the side wall of the shell, a feed opening of the screw feeding device is arranged in the shell, and the dust removal device is arranged above the feed opening;
the top of the slurry melting device is provided with an inlet of an air exhaust device.
According to the invention, the screw feeding device is used for feeding materials to prevent the materials from being blocked, and the air extracting and exhausting device is used for absorbing gas generated in the slurry melting process to avoid the enrichment of acetylene gas in the slurry melting process; the dust removal device is used for simultaneously solving the problems of dust dispersion and acetylene gas dissipation in the pulping process.
As a preferable technical scheme of the invention, the screw feeding device comprises the feed opening and a feed inlet.
Preferably, the screw feed is at 30 to 60 ° to the horizontal, for example 30 °, 35 °, 40 °, 45 °, 50 °, 55 ° or 60 °, but not limited to the values listed, and other values within the range of values are equally applicable.
As a preferable technical scheme, the dust removal device comprises a dust removal cover, and the feed opening is positioned in the dust removal cover.
In the invention, the feed opening is positioned below the liquid level in the slurry melting device, so that a large amount of dust can be prevented from floating in the slurry melting device.
Preferably, the top of the dust hood is provided with an exhaust hole.
According to the invention, the exhaust holes are uniformly formed in the top of the dust hood, and the arrangement of the exhaust holes can discharge acetylene gas in the slurry melting process in time.
Preferably, the bottom of the dust hood is positioned below the liquid level in the slurry device.
Preferably, the height below the liquid level of the dust hood is 1/6-1/3, such as 1/6, 1/5, 1/4 or 1/3, but the invention is not limited to the listed values, and other values in the range of values are also applicable.
Preferably, a slurry stirring device is arranged inside the dust hood.
According to the invention, the slurry stirring device arranged in the dust hood can prevent the carbide slag powder from depositing and is beneficial to homogenizing the carbide slag powder.
As a preferable technical solution of the present invention, the dust removing device includes a first spraying device and a second spraying device.
Preferably, the first spraying device is arranged inside the dust hood and below the exhaust hole.
Preferably, the second spraying device is arranged outside the dust hood and above the exhaust hole.
In the invention, the first spraying device and the second spraying device are used for removing dust floating in the slurry melting process.
Preferably, the distance between the axis of the dust collector and the axis of the pulping device is 1/6-1/4 of the length of the pulping device, such as 1/6, 1/5 or 1/4, but not limited to the enumerated values, and other values in the numerical range are also applicable.
As the preferable technical scheme of the invention, the top of the pulping device is provided with an air inlet hole.
In the invention, the air inlets are uniformly arranged at the top of the slurry melting device.
Preferably, the bottom of the pulping device is provided with a pulp outlet.
Preferably, the air extracting and exhausting device comprises an axial flow fan.
The invention also provides an application method of the pulping and exhausting device, which comprises the following steps: carbide slag powder enters the slurry melting device through the screw feeding device, slurry melting treatment is carried out through the stirring device in the slurry melting device, the dust removal device is used for removing dust generated in the slurry melting process, and the air exhaust device is used for absorbing gas generated in the slurry melting treatment.
As a preferred technical solution of the present invention, the application method further includes: carbide slag powder enters into through screw rod feed arrangement in the dust excluding hood, carry out the chemical pulp processing through chemical pulp agitating unit and agitating unit, open first spray set and second spray set, the gaseous exhaust vent of following of production is discharged in the chemical pulp processing, and the gaseous mixture that the combustion gas got into with the inlet port, through axial fan discharges from the chemical pulp device.
In a preferred embodiment of the present invention, the gas generated in the slurry treatment includes acetylene.
Preferably, the gas entering the gas inlet hole comprises air.
Preferably, the time of the pulping treatment is 1 to 10 hours, for example, 1 hour, 2 hours, 3 hours, 4 hours, 5 hours, 6 hours, 7 hours, 8 hours, 9 hours or 10 hours, etc., but the pulping treatment is not limited to the enumerated values, and other values in the numerical range are also applicable.
Preferably, the rotation speed of the slurry stirring device is 100-300rpm, such as 100rpm, 150rpm, 200rpm, 250rpm or 300rpm, but not limited to the enumerated values, and other values in the numerical range are also applicable.
Preferably, the rotation speed of the stirring device is 200-400rpm, such as 200rpm, 250rpm, 300rpm, 350rpm, 400rpm, etc., but not limited to the enumerated values, and other values within the range of values are also applicable.
As a preferable aspect of the present invention, the total water flow rate of spraying includes a water flow rate of the first spraying device and a water flow rate of the second spraying device.
Preferably, the volume ratio of the water flow rate of the first spraying device to the water flow rate of the second spraying device is (1-10):1, for example, 1:1, 2:1, 3:1, 4:1, 5:1, 6:1, 7:1, 8:1, 9:1 or 10:1, but not limited to the enumerated values, and other values within the range of values are equally applicable.
Preferably, the volume-mass ratio of the total spray water flow to the carbide slag powder is (4-10):1m3The value of/t may be, for example, 4:1, 5:1, 6:1, 7:1, 8:1, 9:1 or 10:1, but is not limited to the values listed, and other values within the range of values are also applicable.
As the preferable technical scheme of the invention, the air volume of the axial flow fan is 10000-50000m3H may be, for example, 10000m3/h、20000m3/h、30000m3/h、40000m3H or 50000m3And/h, etc., but are not limited to the recited values, other values within the numerical range are equally applicable.
Preferably, the wind pressure of the axial flow fan is 50-2000Pa, such as 50Pa, 100Pa, 200Pa, 400Pa, 600Pa, 800Pa, 1000Pa, 1200Pa, 1400Pa, 1600Pa, 1800Pa or 2000Pa, but not limited to the listed values, and other values in the range of values are also applicable.
Compared with the prior art, the invention has the following beneficial effects:
according to the slurry dissolving and exhausting device for carbide slag powder and the application method thereof, the problems of dust dispersion, acetylene gas enrichment and the like in the slurry dissolving process can be prevented by arranging the air extracting and exhausting device and arranging the dust hood, the exhaust hole and the spraying device on the dust removing device, the production safety is improved, slurry with ideal ratio can be obtained by the application method, and the slurry dissolving and exhausting device is simple and convenient, is low in cost and has good industrial application prospect.
Drawings
Fig. 1 is a schematic structural view of a carbide slag powder slurrying and exhausting apparatus provided in embodiment 1;
wherein: 1-a pulping device, 2-a stirring device, 3-an axial flow fan, 4-a screw feeding device, 5-a feeding port, 6-a discharging port, 7-a dust hood, 8-an exhaust hole, 9-a first spraying device, 10-a second spraying device, 11-a pulping stirring device, 12-an air inlet hole and 13-a pulp outlet hole.
Detailed Description
It should be noted that, unless otherwise explicitly stated or limited, the terms "disposed," "connected," and "connected" in the description of the present invention are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally connected: can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art through specific situations.
The technical scheme of the invention is further explained by the specific implementation mode in combination with the attached drawings. The following examples are merely illustrative of the present invention and do not represent or limit the scope of the claims, which are defined by the claims.
Example 1
The present embodiment provides a slurry dissolving and exhausting device for carbide slag powder, as shown in fig. 1, the slurry dissolving and exhausting device includes a slurry dissolving device 1, a screw feeding device 4, a dust removing device and an air exhausting device;
the pulping device 1 comprises a shell and a stirring device 2 arranged in the shell;
the screw feeding device 4 comprises a feeding hole 5 and a discharging hole 6; the dust removal device comprises a dust removal cover 7, a first spraying device 9 and a second spraying device 10;
the air extracting and exhausting device is an axial flow fan 3;
the screw feeding device 4 is arranged on the side wall of the shell, the screw feeding device 4 is 30 degrees to the horizontal line, and a feed opening 6 of the screw feeding device 4 is arranged in the dust hood 7; the feed opening 6 is positioned below the liquid level in the slurry melting device 1;
the dust removal device is arranged in the shell, the top of the dust hood 7 is provided with an exhaust hole 8, the inside of the dust hood 7 is provided with a slurry stirring device 11, the bottom of the dust hood 7 is positioned below the liquid level in the slurry melting device 1, the height below the liquid level of the dust hood 7 is 1/3 of the total height of the dust hood 7, and the distance between the axis of the dust removal device and the axis of the slurry melting device 1 is 1/4 of the length of the slurry melting device 1;
the first spraying device 9 is arranged inside the dust hood 7 and below the exhaust holes 8, and the second spraying device 10 is arranged outside the dust hood 7 and above the exhaust holes 8;
the top of the slurry melting device 1 is provided with an air inlet 12 and an inlet of an air exhaust device, and the bottom of the slurry melting device 1 is provided with a slurry outlet 13.
Example 2
The present embodiment provides a slurry-forming and gas-discharging device for carbide slag powder, which is not provided with the second spraying device 10; the rest is the same as in example 1.
Example 3
The present embodiment provides a slurry-forming and exhausting device for carbide slag powder, which is not provided with an exhaust hole 8; the rest is the same as in example 1.
Comparative example 1
The comparative example provides a slurrying and exhausting device for carbide slag powder, which is not provided with a dust removal device; the rest is the same as in example 1.
Comparative example 2
The comparative example provides a slurry dissolving and exhausting device for carbide slag powder, and the slurry dissolving and exhausting device is not provided with an air extracting and exhausting device; the rest is the same as in example 1.
Application example 1
The application example applies the slurry forming and exhausting device provided in embodiment 1 to the slurry forming and exhausting of the carbide slag powder, and the application includes the following steps: the carbide slag powder enters a dust hood 7 through a screw feeding device 4, is slurried for 5 hours under the stirring of a slurry stirring device 11 with the rotating speed of 200rpm and a stirring device 2 with the rotating speed of 300rpm, a first spraying device 9 and a second spraying device 10 are opened for spraying, the volume ratio of the water flow of the first spraying device 9 to the water flow of the second spraying device 10 is 5:1, and the volume mass ratio of the total water flow sprayed per hour to the carbide slag powder is 5:1m3T, acetylene gas generated in the pulping process is discharged from the exhaust hole 8, the discharged acetylene gas is mixed with air entering the air inlet hole 12, and the passing air volume is 20000m3And h, discharging the axial flow fan 3 with the wind pressure of 1000Pa from the pulping device 1.
Application example 2
The application example applies the slurry forming and exhausting device provided in embodiment 1 to the slurry forming and exhausting of the carbide slag powder, and the application includes the following steps: the carbide slag powder enters a dust hood 7 through a screw feeding device 4, is slurried for 1h under the stirring of a slurry stirring device 11 with the rotating speed of 100rpm and a stirring device 2 with the rotating speed of 400rpm, a first spraying device 9 and a second spraying device 10 are opened for spraying, the volume ratio of the water flow of the first spraying device 9 to the water flow of the second spraying device 10 is 1:1, and the volume mass ratio of the total water flow sprayed per hour to the carbide slag powder is 4:1m3T, acetylene gas generated in the pulping process is discharged from the exhaust hole 8, the discharged acetylene gas is mixed with air entering the air inlet hole 12, and the passing air volume is 10000m3And h, discharging the slurry from the slurry device 1 by using an axial flow fan 3 with the wind pressure of 50 Pa.
Application example 3
The application example applies the slurry forming and exhausting device provided in embodiment 1 to the slurry forming and exhausting of the carbide slag powder, and the application includes the following steps: feeding device for carbide slag powder through screw4 entering a dust hood 7, pulping for 10 hours under the stirring of a pulping stirring device 11 with the rotating speed of 300rpm and a stirring device 2 with the rotating speed of 200rpm, opening a first spraying device 9 and a second spraying device 10 for spraying, wherein the volume ratio of the water flow of the first spraying device 9 to the water flow of the second spraying device 10 is 10:1, and the volume mass ratio of the total water flow sprayed per hour to the calcium carbide slag powder is 10:1m3T, acetylene gas generated in the pulping process is discharged from the exhaust hole 8, the discharged acetylene gas is mixed with air entering the air inlet hole 12, and the passing air volume is 50000m3And h, discharging the axial flow fan 3 with the wind pressure of 2000Pa from the pulping device 1.
Application example 4
The application example applies the slurry forming and exhausting device provided in embodiment 2 to the slurry forming and exhausting of the carbide slag powder, and the application comprises the following steps: the carbide slag powder enters a dust hood 7 through a screw feeding device 4, is slurried for 5 hours under the stirring of a slurry stirring device 11 with the rotating speed of 200rpm and a stirring device 2 with the rotating speed of 300rpm, a first spraying device 9 is opened for spraying, and the volume-mass ratio of the spraying water flow per hour to the carbide slag powder is 5:1m3T, acetylene gas generated in the pulping process is discharged from the exhaust hole 8, the discharged acetylene gas is mixed with air entering the air inlet hole 12, and the passing air volume is 20000m3And h, discharging the axial flow fan 3 with the wind pressure of 1000Pa from the pulping device 1.
Application example 5
The application example applies the slurry forming and exhausting device provided in embodiment 3 to the slurry forming and exhausting of the carbide slag powder, and the application includes the following steps: the carbide slag powder enters a dust hood 7 through a screw feeding device 4, is slurried for 5 hours under the stirring of a slurry stirring device 11 with the rotating speed of 200rpm and a stirring device 2 with the rotating speed of 300rpm, a first spraying device 9 and a second spraying device 10 are opened for spraying, the volume ratio of the water flow of the first spraying device 9 to the water flow of the second spraying device 10 is 5:1, and the volume mass ratio of the total water flow sprayed per hour to the carbide slag powder is 5:1m3T, the air passing quantity of the gas generated in the pulping process is 20000m3And h, discharging the axial flow fan 3 with the wind pressure of 1000Pa from the pulping device 1.
Comparative application example 1
The comparative application example applies the slurry forming and exhausting device provided in comparative example 1 to perform slurry forming and exhausting of the carbide slag powder, and the application comprises the following steps: the carbide slag powder enters the slurry melting device 1 through the screw feeding device 4, the slurry melting device 2 is stirred for 5 hours at the rotating speed of 300rpm, and the air flow of the gas generated in the slurry melting process is 20000m3The axial flow fan 3 with the wind pressure of 1000Pa discharges the gas from the pulping device 1.
Comparative application example 2
The comparative application example applies the slurry forming and exhausting device provided in comparative example 2 to perform slurry forming and exhausting of the carbide slag powder, and the application comprises the following steps: the carbide slag powder enters a dust hood 7 through a screw feeding device 4, is slurried for 5 hours under the stirring of a slurry stirring device 11 with the rotating speed of 200rpm and a stirring device 2 with the rotating speed of 300rpm, a first spraying device 9 and a second spraying device 10 are opened for spraying, the volume ratio of the water flow of the first spraying device 9 to the water flow of the second spraying device 10 is 5:1, and the volume mass ratio of the total water flow sprayed per hour to the carbide slag powder is 5:1m3And/t, discharging acetylene gas generated in the pulping process from the exhaust hole 8.
The exhaust gases of application examples 1 to 5 and comparative application examples 1 to 2 were analyzed, the acetylene gas concentration in the exhaust gas was analyzed by an acetylene analyzer, and the carbide slag particle concentration in the exhaust gas was analyzed by a particle concentration detector, with the results shown in table 1.
TABLE 1
The following points can be derived from table 1: the carbide slag powder slurrying and exhausting device provided by the invention is applied to carbide slag powder slurrying, and acetylene gas and carbide slag particles contained in exhausted gas are less; the slurry melting and exhausting device of the application example 4 is not provided with the second spraying device, so that the scattered dust in the slurry melting process cannot be completely removed, and the exhausted gas contains more carbide slag particles; the slurry melting and exhausting device in application example 5 is not provided with an exhaust hole, so that the second spraying device cannot play a corresponding role, gas in the slurry melting process cannot be completely exhausted, and exhausted gas contains more acetylene gas and carbide slag particles.
Compared with the slurry dissolving and exhausting device in the application example 1, the dust removing device is not arranged, so that the carbide slag powder floats on the water surface and cannot be subjected to slurry dissolving treatment; compared with the slurry melting and exhausting device in application example 2, the slurry melting and exhausting device is not provided with an air exhaust device, so that gas generated in the slurry melting process cannot be completely exhausted, and the exhausted gas contains a large amount of acetylene gas and carbide slag particles.
The applicant declares that the above description is only a specific embodiment of the present invention, but the scope of the present invention is not limited thereto, and it should be understood by those skilled in the art that any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope of the present invention are within the scope and disclosure of the present invention.
Claims (10)
1. The slurry melting and exhausting device for the carbide slag powder is characterized by comprising a slurry melting device, a feeding unit and an air extracting and exhausting device;
the slurry melting device comprises a shell and a stirring device arranged in the shell;
the feeding unit comprises a screw feeding device and a dust removal device;
the screw feeding device is arranged on the side wall of the shell, a feed opening of the screw feeding device is arranged in the shell, and the dust removal device is arranged above the feed opening;
the top of the slurry melting device is provided with an inlet of an air exhaust device.
2. The slurrying and venting device of claim 1, wherein the screw feed device comprises the feed opening and a feed inlet;
preferably, the screw feed is at 30-60 ° to the horizontal.
3. The pulping and exhausting device according to claim 1 or 2, wherein the dust removing device comprises a dust hood, and the feed opening is positioned in the dust hood;
preferably, the top of the dust hood is provided with an exhaust hole;
preferably, the bottom of the dust hood is positioned below the liquid level in the slurry device;
preferably, the height below the liquid level of the dust hood is 1/6-1/3 of the total height of the dust hood;
preferably, a slurry stirring device is arranged inside the dust hood.
4. The pulping and exhausting device according to claim 3, wherein the dust removing device comprises a first spraying device and a second spraying device;
preferably, the first spraying device is arranged in the dust hood and is positioned below the exhaust hole;
preferably, the second spraying device is arranged outside the dust hood and above the exhaust hole;
preferably, the distance between the axis of the dust collector and the axis of the pulping device is 1/6-1/4 of the length of the pulping device.
5. The pulping and exhausting device of any one of claims 1 to 4, wherein an air inlet hole is arranged at the top of the pulping device;
preferably, the bottom of the slurry melting device is provided with a slurry outlet;
preferably, the air extracting and exhausting device comprises an axial flow fan.
6. A method of using the pulping and air-discharging apparatus according to any one of claims 1 to 5, the method comprising: carbide slag powder enters the slurry melting device through the screw feeding device, slurry melting treatment is carried out through the stirring device in the slurry melting device, the dust removal device is used for removing dust generated in the slurry melting process, and the air exhaust device is used for absorbing gas generated in the slurry melting treatment.
7. The application method according to claim 6, further comprising: carbide slag powder enters into through screw rod feed arrangement in the dust excluding hood, carry out the chemical pulp processing through chemical pulp agitating unit and agitating unit, open first spray set and second spray set, the gaseous exhaust vent of following of production is discharged in the chemical pulp processing, and the gaseous mixture that the combustion gas got into with the inlet port, through axial fan discharges from the chemical pulp device.
8. Use according to claim 6 or 7, wherein the gas generated in the slurrying process comprises acetylene;
preferably, the gas entering the gas inlet hole comprises air;
preferably, the time of the pulping treatment is 1-10 h;
preferably, the rotating speed of the slurry stirring device is 100-300 rpm;
preferably, the rotation speed of the stirring device is 200-400 rpm.
9. The application method of claim 7, wherein the total water flow rate of the spray comprises a water flow rate of a first spray device and a water flow rate of a second spray device;
preferably, the volume ratio of the water flow of the first spraying device to the water flow of the second spraying device is (1-10): 1;
preferably, the volume-mass ratio of the total spray water flow to the carbide slag powder is (4-10):1m3/t。
10. The application method as claimed in claim 7, wherein the air volume of the axial flow fan is 10000-50000m3/h；
Preferably, the wind pressure of the axial flow fan is 50-2000 Pa.
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| CN206157102U (en) * | 2016-11-15 | 2017-05-10 | 鹰潭市远大气体有限公司 | Novel separation takes place for acetylene production's carbide slag device |
| WO2018152747A1 (en) * | 2017-02-23 | 2018-08-30 | 深圳市玖创科技有限公司 | Easy-to-clean lithium battery electrode slurry stirring and mixing tank |
| CN108854641A (en) * | 2018-07-02 | 2018-11-23 | 东华工程科技股份有限公司 | A kind of ultralight fines continuous pulping equipment and pulping process |
| CN213471713U (en) * | 2020-09-17 | 2021-06-18 | 金诚信矿山工程设计院有限公司 | Immersed powder feeding device |
| CN214209946U (en) * | 2021-01-07 | 2021-09-17 | 河北承大环保科技有限公司 | Dust removal environment-friendly device for cement production |
| CN113321187A (en) * | 2021-05-24 | 2021-08-31 | 中国成达工程有限公司 | Method and system for producing bleaching powder by using wet-process acetylene waste calcium carbide slurry |
| CN113171632A (en) * | 2021-06-29 | 2021-07-27 | 中国科学院过程工程研究所 | Method for removing impurity gas in carbide slag slurry by micro-nano bubbles |
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