CN112915683A - Efficient carbide slag dust removing device - Google Patents
Efficient carbide slag dust removing device Download PDFInfo
- Publication number
- CN112915683A CN112915683A CN202011597888.3A CN202011597888A CN112915683A CN 112915683 A CN112915683 A CN 112915683A CN 202011597888 A CN202011597888 A CN 202011597888A CN 112915683 A CN112915683 A CN 112915683A
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- Prior art keywords
- carbide slag
- dust
- water
- efficiency
- overflow
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- 239000000428 dust Substances 0.000 title claims abstract description 160
- 239000002893 slag Substances 0.000 title claims abstract description 117
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 108
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 239000013505 freshwater Substances 0.000 claims abstract description 6
- 238000005507 spraying Methods 0.000 claims description 23
- 239000007921 spray Substances 0.000 claims description 18
- 239000005997 Calcium carbide Substances 0.000 claims description 10
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 claims description 10
- 238000009434 installation Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 23
- 238000000034 method Methods 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 4
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 4
- 238000005457 optimization Methods 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 4
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005201 scrubbing Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical group [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention provides a high-efficiency dust removal device for carbide slag dust, which comprises a carbide slag buffer bin, a high-efficiency dust remover for carbide slag dust and an overflow water tank, wherein the overflow water tank is communicated with fresh water outside, an exhaust port of the carbide slag buffer bin is connected with an air inlet of the high-efficiency dust remover for carbide slag dust by a flange, when the high-efficiency dust remover works, gas containing carbide slag and water vapor and gas containing water vapor and carbide slag dust in a high-temperature state are discharged from the periphery of an exhaust hole of the carbide slag buffer bin and enter the high-efficiency dust remover for carbide slag dust in a dispersing and uniform manner through a gas distributor, flow reversely with high-speed droplets atomized by a liquid distributor, the carbide slag particles in an air flow are captured by the contact and collision of the hydrophilicity of the carbide slag dust and the high-speed droplets, and the droplets after the dust are captured fall into a water receiving tank under the action of gravity, so as to achieve the purpose of dust removal, the device has the characteristics of small volume, light weight, stable operation and convenient installation and maintenance.
Description
Technical Field
The invention belongs to the technical field of dry acetylene processes, and particularly relates to a high-efficiency carbide slag dust removing device.
Background
The dry acetylene process is to spray water in a mist state onto calcium carbide powder with a theoretical amount of water for hydrolysis to produce powdered calcium carbide slag with water content of 4-10% and temperature of 90-96 deg.c. When the carbide slag is transported into the carbide slag buffer bin, the moisture in the high-temperature carbide slag absorbs the heat in the carbide slag to be vaporized and is discharged from the vent hole of the carbide slag buffer bin. Because the carbide slag has light weight, small granularity and high temperature, when entering the carbide buffer bin, carbide slag dust is discharged from the exhaust hole along with water vapor flow. The dust-containing gas is required to be discharged in an ultralow way under the current environmental protection pressure, so the application of the dust removal technology is particularly important. The main component of the carbide slag dust is calcium hydroxide, the carbide slag dust has high humidity, and can generate easily caked calcium carbonate by reacting with CO2 in the air, so the traditional gas dust removal equipment is easily blocked due to the characteristics of high humidity, high viscosity, easy caking and the like of the carbide slag dust, and has limitation on long-term stable use. If the problem of discharging carbide slag dust is solved by sealing the vent hole of the carbide slag buffer bin, trace acetylene gas contained in the carbide slag can be gathered in the carbide slag buffer bin, so that explosion risk factors exist.
Disclosure of Invention
The invention aims to provide a high-efficiency carbide slag dust removing device to solve the problems in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme: high-efficient dust collector of carbide slag dust, including carbide slag surge bin, high-efficient dust remover of carbide slag dust and overflow launder, overflow launder and outside fresh water intercommunication, carbide slag surge bin gas vent and the high-efficient dust remover air inlet flange joint of carbide slag dust, overflow launder and the high-efficient dust remover water inlet of carbide slag dust pass through the dust remover water supply line intercommunication, the high-efficient dust remover delivery port of carbide slag dust and overflow launder pass through dust remover water drainage line intercommunication, overflow water pipeline is installed to the high-efficient dust remover overflow mouth of carbide slag dust, the overflow water pipeline other end and dust remover water drainage line intercommunication, install the overflow water pump on the dust remover water supply line.
As optimization, the efficient carbide slag dust collector comprises a barrel body and an upper cap, the upper end face of the barrel body is in flange connection with the lower end face of the upper cap, a gas distributor and a water receiving tank are fixedly mounted on the bottom side of the barrel body respectively, a gas outlet of the gas distributor penetrates through the water receiving tank, a liquid distributor is fixedly mounted on the side face of the barrel body and is located on the upper side of the gas distributor, a water outlet of the efficient carbide slag dust collector and a water overflow port of the efficient carbide slag dust collector are fixedly mounted on the side face of the water receiving tank respectively, the water overflow port of the efficient carbide slag dust collector is located on the upper portion of the water outlet of the efficient carbide slag dust collector, a gas inlet of the gas distributor is in flange connection with the gas outlet of a carbide slag buffering bin, and the liquid.
As optimization, the liquid distributor comprises a spraying component and a spraying supporting plate, the spraying supporting plate is fixedly arranged on the inner side of the barrel, the spraying component is fixedly arranged on the spraying supporting plate, and the water inlet end of the spraying component is communicated with the overflow water tank through a water supply pipeline of the dust remover.
As optimization, the spraying assembly comprises a spraying pipe and a coil pipe, the coil pipe is arranged on the spraying support plate, one side of the coil pipe is connected with a water feeding pipeline of the dust remover through a flange, the spraying pipe is welded on the lower side of the coil pipe, and the coil pipe is communicated with the inside of the spraying pipe.
Preferably, the upper cap is trapezoidal in shape.
Preferably, the bottom side of the cylinder is obliquely arranged.
As an optimization, the inclination angle between the side surface of the cylinder body provided with the water outlet of the carbide slag dust high-efficiency dust remover and the bottom side of the cylinder body is 75 degrees.
Compared with the prior art, the invention has the beneficial effects that: compared with the traditional dust remover, the volume of the dust remover is reduced, the dust removal efficiency is obviously improved, and the technology is mainly suitable for purification treatment of explosive, high-temperature, high-humidity, high-dust-content and easy-caking dust-containing waste gas of the carbide slag buffer bin for exhausting. The device has the characteristics of small volume, light weight, stable operation and convenient installation and maintenance, and solves the problem of dust caking and blockage in the purification process.
The technology can replace the traditional wet dedusting washing tower, reduce the volume of the tower and obviously improve the dedusting efficiency; the method is suitable for purifying high-temperature, high-humidity, high-dust-content and easy-caking dust-containing waste gas; the technology can completely meet the requirement of waste gas purification treatment in the processes of carbide slag production, transportation and storage. The breakthrough of key technology and the purification of high-humidity easy-caking dust and waste gas in industrial production not only provide a new process method, but also take the 2000Nm3/h air volume dust removal of a buffer bin as an example: the dust removal efficiency is more than or equal to 99 percent; the resistance of the device is less than 10 Pa.
Adopt "high-efficient dust remover of carbide slag dust" to replace "traditional water spray scrubbing tower" and get rid of the carbide slag dust and can greatly improve purification efficiency, under the same processing amount of wind and purification efficiency condition, "the volume of high-efficient dust remover of carbide slag dust" is far less than "traditional water spray scrubbing tower" volume, the installation and the maintenance of being convenient for, and area is little, is particularly suitable for old workshop to reform transform.
Drawings
FIG. 1 is a schematic view of the overall structure of the efficient carbide slag dust collector of the invention;
FIG. 2 is a schematic structural view of the efficient carbide slag dust collector of the present invention;
FIG. 3 is a top view of the structure of FIG. 2A-A according to the present invention;
FIG. 4 is a schematic view of a gas distributor according to the present invention;
FIG. 5 is a top view of B-B of FIG. 4 according to the present invention;
FIG. 6 is a schematic view of the upper cap structure of the present invention.
In the figure: 1-a gas distributor, 2-a liquid distributor, 3-a cylinder, 4-a spray assembly, 5-a spray support plate, 6-a water receiving tank, 7-an upper cap cover, 8-an overflow water tank, 9-an overflow water pump, 10-a carbide slag buffer bin, 11-a dust remover drainage pipeline, 12-a dust remover water supply pipeline, 13-an overflow water pipeline and 14-a high-efficiency carbide slag dust remover.
Detailed Description
The present invention will be further illustrated with reference to the accompanying drawings and specific embodiments, which are to be understood as merely illustrative of the invention and not as limiting the scope of the invention. It should be noted that the terms "front," "back," "left," "right," "upper" and "lower" used in the following description refer to directions in the drawings, and the terms "inner" and "outer" refer to directions toward and away from, respectively, the geometric center of a particular component.
Referring to fig. 1-6, the efficient dust removing device for carbide slag dust comprises a carbide slag buffer bin 10, a high-efficiency dust remover 14 for carbide slag dust and an overflow water tank 8, wherein the overflow water tank 8 is communicated with fresh water outside, an exhaust port of the carbide slag buffer bin 10 is in flange connection with an air inlet of the high-efficiency dust remover 14 for carbide slag dust, the overflow water tank 8 is communicated with an water inlet of the high-efficiency dust remover 14 for carbide slag dust through a dust remover water supply pipeline 12, a water outlet of the high-efficiency dust remover 14 for carbide slag dust is communicated with the overflow water tank 8 through a dust remover water discharge pipeline 11, an overflow water pipeline 13 is arranged at the overflow port of the high-efficiency dust remover 14 for carbide slag dust, the other end of the overflow water pipeline 13 is communicated with the dust remover water discharge pipeline 11, an overflow water pump 9 is arranged on the dust remover water supply pipeline 12, for example, a water pump with model number IRG50-125 is selected, and the dust remover water discharge, The overflow pipe 13 is made of stainless steel.
The efficient carbide slag dust collector 14 comprises a barrel 3 and an upper cap 7, the upper end face of the barrel 3 is in flange connection with the lower end face of the upper cap 7, the bottom side of the barrel 3 is fixedly provided with a gas distributor 1 and a water receiving tank 6 respectively, an exhaust port of the gas distributor 1 penetrates through the water receiving tank 6, the side face of the barrel 3 is fixedly provided with a liquid distributor 2, the liquid distributor 2 is positioned on the upper side of the gas distributor 1, a water outlet of the efficient carbide slag dust collector 14 and an overflow port of the efficient carbide slag dust collector 14 are fixedly arranged on the side face of the water receiving tank 6 respectively, the overflow port of the efficient carbide slag dust collector 14 is positioned on the upper portion of the water outlet of the efficient carbide slag dust collector 14, an air inlet of the gas distributor 1 is in flange connection with the exhaust port of a carbide slag buffer bin 10, the liquid distributor 2 is communicated with an overflow water tank 8 through a dust collector water feeding pipeline 12.
The liquid distributor 2 comprises a spraying component 4 and a spraying support plate 5, the spraying support plate 5 is fixedly installed on the inner side of the cylinder 3, the spraying component 4 is fixedly installed on the spraying support plate 5, the water inlet end of the spraying component 4 is communicated with the overflow water tank 8 through a dust remover water supply pipeline 12, and an overflow water pump 9 is installed on the dust remover water supply pipeline 12.
The spray assembly comprises a spray pipe and a coil pipe, the coil pipe is arranged on the spray supporting plate 5, one side of the coil pipe is connected with a dust remover water supply pipeline 12 through a flange, the spray pipe is welded on the lower side of the coil pipe, and the coil pipe is communicated with the interior of the spray pipe.
The upper cap 7 is trapezoidal in shape.
The bottom side of the cylinder 3 is obliquely arranged.
The inclination angle between the side surface of the cylinder 3 provided with the water outlet of the high-efficiency carbide slag dust collector 14 and the bottom side of the cylinder 3 is 75 degrees.
The working principle is as follows: the efficient carbide slag dust removal device comprises a carbide slag buffer bin 10, a high-efficient carbide slag dust remover 14 and an overflow water tank 8, wherein the overflow water tank 8 is communicated with external fresh water, an exhaust port of the carbide slag buffer bin 10 is in flange connection with an air inlet of the high-efficient carbide slag dust remover 14, in operation, the high-efficient carbide slag dust remover 14 comprises a liquid distributor 2, a gas distributor 1 and a water receiving tank 6, gas containing carbide slag and water vapor and discharged from the exhaust port of the carbide slag buffer bin 10, gas containing water vapor and carbide slag dust in a high-temperature state is uniformly dispersed by the gas distributor 1 and discharged from the periphery of the exhaust port of the carbide slag buffer bin 10 to enter the high-efficient carbide slag dust remover 14 and flows reversely with high-speed droplets atomized by the liquid distributor 2, and the carbide slag dust and the high-speed droplets are contacted and collided with each other by means of hydrophilicity of the carbide slag dust, and carbide slag particles in airflow, the liquid drops after dust collection fall into the water receiving tank 6 under the action of gravity, so as to achieve the aim of dust removal, the barrel body 3 of the carbide slag high-efficiency dust remover is provided with an overflow port 14 of the carbide slag dust high-efficiency dust remover, when the water outlet of the carbide slag dust high-efficiency dust remover 14 at the bottom of the carbide slag high-efficiency dust remover barrel 3 is scaled and blocked, the spray water can be discharged from the overflow port of the carbide slag dust high-efficiency dust remover 14, thereby preventing the spray water from entering the carbide slag buffer bin 10 after passing through the exhaust port of the carbide slag buffer bin 10, ensuring the safe operation of the high-efficiency carbide slag dust remover 14, because the dynamic pressure of the exhaust holes of the carbide slag buffer bin 10 is less than or equal to 15Pa, in order to avoid the atomized liquid from sealing the exhaust holes, the liquid distributor 2 adopts double-layer arrangement to form a dust removal and layered dust removal mode, the dust removal efficiency is improved, the exhaust hole is prevented from being sealed by liquid, a smooth air passage is formed, and potential safety hazards caused by acetylene gas gathering due to the fact that the discharged gas flows smoothly are avoided.
The high-efficiency carbide slag dust remover 14 is characterized in that spray water is from an overflow water tank of an original system, is conveyed to the high-efficiency carbide slag dust remover 14 through an overflow water pump 9, is mixed with water vapor and carbide slag dust discharged by a carbide slag buffer bin 10 and then falls into a water receiving tank 6, and returns to an overflow water tank 8 through a dust remover water drainage pipeline 11, and the overflow water tank 8 serving as a production water tank can continuously supplement fresh water, so that the low solid content of the overflow water tank is ensured.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
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, and it is intended that the described embodiments of the invention be construed as merely a subset of the embodiments of the invention and not as a whole. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Claims (7)
1. Carbide slag dust high efficiency dust collector, its characterized in that: the calcium carbide slag dust collection device comprises a calcium carbide slag buffer bin (10), a calcium carbide slag dust high-efficiency dust collector (14) and an overflow water tank (8), wherein the overflow water tank (8) is communicated with external fresh water, an exhaust port of the calcium carbide slag buffer bin (10) is in flange connection with an air inlet of the calcium carbide slag dust high-efficiency dust collector (14), the overflow water tank (8) is communicated with a water inlet of the calcium carbide slag dust high-efficiency dust collector (14) through a dust collector water supply pipeline (12), a water outlet of the calcium carbide slag dust high-efficiency dust collector (14) is communicated with the overflow water tank (8) through a dust collector water discharge pipeline (11), an overflow water pipeline (13) is installed at an overflow port of the calcium carbide slag dust high-efficiency dust collector (14), the other end of the overflow water pipeline (13) is communicated with the dust collector water discharge pipeline (11), and an overflow water pump (9) is installed on the dust.
2. The efficient carbide slag dust removal device as claimed in claim 1, wherein: the carbide slag dust high-efficiency dust remover (14) comprises a cylinder body (3) and an upper cap cover (7), the upper end face of the cylinder body (3) is in flange connection with the lower end face of the upper cap cover (7), a gas distributor (1) and a water receiving tank (6) are fixedly mounted on the bottom side of the cylinder body (3) respectively, an exhaust port of the gas distributor (1) penetrates through the water receiving tank (6), a liquid distributor (2) is fixedly mounted on the side face of the cylinder body (3), the liquid distributor (2) is located on the upper side of the gas distributor (1), a water outlet of the carbide slag dust high-efficiency dust remover (14) and an overflow port of the carbide slag dust high-efficiency dust remover (14) are fixedly mounted on the side face of the water receiving tank (6) respectively, an overflow port of the carbide slag dust high-efficiency dust remover (14) is located on the upper portion of the water outlet of the carbide slag dust high-efficiency dust remover (14), an air inlet of the gas distributor, the liquid distributor (2) is communicated with the overflow water tank (8) through a dust remover water supply pipeline (12).
3. The efficient carbide slag dust removal device as claimed in claim 2, wherein: the liquid distributor (2) comprises a spraying assembly (4) and a spraying support plate (5), the spraying support plate (5) is fixedly installed on the inner side of the barrel (3), the spraying assembly (4) is fixedly installed on the spraying support plate (5), and the water inlet end of the spraying assembly (4) is communicated with the overflow water tank (8) through a dust remover water supply pipeline (12).
4. The efficient carbide slag dust removal device as claimed in claim 3, wherein: the spray assembly comprises a spray pipe and a coil pipe, the coil pipe is installed on the spray supporting plate (5), one side of the coil pipe is connected with a dust remover water supply pipeline (12) through a flange, the spray pipe is welded on the lower side of the coil pipe, and the coil pipe is communicated with the interior of the spray pipe.
5. The efficient carbide slag dust removal device as claimed in claim 4, wherein: the upper cap (7) is trapezoidal in shape.
6. The efficient carbide slag dust removal device as claimed in claim 5, wherein: the bottom side of the cylinder (3) is obliquely arranged.
7. The efficient carbide slag dust removal device as claimed in claim 6, wherein: the inclination angle between the side surface of the cylinder (3) provided with the water outlet of the carbide slag dust high-efficiency dust remover (14) and the bottom side of the cylinder (3) is 75 degrees.
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CN202011597888.3A CN112915683A (en) | 2020-12-30 | 2020-12-30 | Efficient carbide slag dust removing device |
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CN202011597888.3A CN112915683A (en) | 2020-12-30 | 2020-12-30 | Efficient carbide slag dust removing device |
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090113881A1 (en) * | 2005-03-29 | 2009-05-07 | Dai Sung Engineering Environment Co., Ltd. | Wet type scrubber for exhaust gas and method of operation |
CN202860338U (en) * | 2012-10-31 | 2013-04-10 | 重庆鹏越科技发展有限公司 | Washing device for acetylene gas |
CN203990223U (en) * | 2014-08-18 | 2014-12-10 | 湖南省湘维有限公司 | A kind of dry carbide slag storehouse |
CN206082004U (en) * | 2016-10-17 | 2017-04-12 | 北京瑞思达化工设备有限公司 | Carbide slag storehouse top dust remover |
CN209333949U (en) * | 2018-09-18 | 2019-09-03 | 内蒙古鄂尔多斯电力冶金集团股份有限公司 | Dry acetylene sludge dust pelletizing system |
CN209828585U (en) * | 2018-12-05 | 2019-12-24 | 安徽华塑股份有限公司 | Calcium carbide furnace gas purifying and dust removing device |
CN211753495U (en) * | 2020-03-13 | 2020-10-27 | 南京林业大学 | Dust-containing waste gas adsorption and separation device |
CN215539405U (en) * | 2020-12-30 | 2022-01-18 | 安徽华塑股份有限公司 | Efficient carbide slag dust removing device |
-
2020
- 2020-12-30 CN CN202011597888.3A patent/CN112915683A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090113881A1 (en) * | 2005-03-29 | 2009-05-07 | Dai Sung Engineering Environment Co., Ltd. | Wet type scrubber for exhaust gas and method of operation |
CN202860338U (en) * | 2012-10-31 | 2013-04-10 | 重庆鹏越科技发展有限公司 | Washing device for acetylene gas |
CN203990223U (en) * | 2014-08-18 | 2014-12-10 | 湖南省湘维有限公司 | A kind of dry carbide slag storehouse |
CN206082004U (en) * | 2016-10-17 | 2017-04-12 | 北京瑞思达化工设备有限公司 | Carbide slag storehouse top dust remover |
CN209333949U (en) * | 2018-09-18 | 2019-09-03 | 内蒙古鄂尔多斯电力冶金集团股份有限公司 | Dry acetylene sludge dust pelletizing system |
CN209828585U (en) * | 2018-12-05 | 2019-12-24 | 安徽华塑股份有限公司 | Calcium carbide furnace gas purifying and dust removing device |
CN211753495U (en) * | 2020-03-13 | 2020-10-27 | 南京林业大学 | Dust-containing waste gas adsorption and separation device |
CN215539405U (en) * | 2020-12-30 | 2022-01-18 | 安徽华塑股份有限公司 | Efficient carbide slag dust removing device |
Non-Patent Citations (2)
Title |
---|
ZHAO, QIUYUE等: "Sources of volatile organic compounds and policy implications for regional ozone pollution control in an urban location of Nanjing, East China", 《ATMOSPHERIC CHEMISTRY AND PHYSICS》, vol. 20, no. 6, 14 April 2020 (2020-04-14), pages 3905 - 3919 * |
丛龙成: "窑尾废气管道增湿喷雾系统的改造", 《水泥》, no. 1, 10 January 2013 (2013-01-10), pages 44 * |
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