CN104014218B - A kind of clean cigarette taste removal dust removal environment-protecting machine - Google Patents
A kind of clean cigarette taste removal dust removal environment-protecting machine Download PDFInfo
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- CN104014218B CN104014218B CN201410278817.5A CN201410278817A CN104014218B CN 104014218 B CN104014218 B CN 104014218B CN 201410278817 A CN201410278817 A CN 201410278817A CN 104014218 B CN104014218 B CN 104014218B
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Abstract
The present invention relates to a kind of clean cigarette taste removal dust removal environment-protecting machine, comprise: primary separation purification devices, the second-order separation purification devices, coil condenser, terminal process equipment, described primary separation purification devices, be made up of water ring vacuum pump, separation water tank, water ring vacuum pump, mixing comb, separator tube, separation water tank and water inlet pipe form the passage of a circulation; Described the second-order separation purification devices, is made up of filter, water ring compressor, separation and purification tank, lime set plate, tank body heat radiation air duct and purifying tank extraction fan; Described coil condenser, is made up of fan housing in thick coil pipe, thin coil pipe, coil pipe external air hood, coil pipe; Described terminal process equipment, be fluid purification tank, gas furnace, gas collector one wherein, wherein gas furnace is made up of large gas furnace and little gas furnace.The invention provides a kind of clean cigarette taste removal dust removal environment-protecting machine, this equipment volume is little, and cost is low, is convenient to install, and equipment is durable, and maintenance cost is low, and result of use is good.
Description
Technical field
The present invention relates to a kind of environmental protecting device, particularly relate to a kind of clean cigarette taste removal dust removal environment-protecting machine.
Background technology
Environment is the basic premise of human survival and development.Environment is that our survival and development provide required resource and condition.Along with socioeconomic development, environmental problem has put on the agenda of national governments as a unavoidable major issue.Protection of the environment, alleviates environmental pollution, and containment ecological degeneration trend, becomes the vital task of government's social management.National for us, protection of the environment is a fundamental state policy of China, solves the environmental problem that the whole nation is outstanding, and promoting economy, society and harmonious development and the Implement of sustainable development strategy, is the important of government faces and difficult task.Current environmental protection equipment kind is a lot, but is mostly that equipment is huge, cost is high, and maintenance cost is high, and these seriously constrain carrying out of efforts at environmental protection and process.
Summary of the invention
Object of the present invention is just to provide a kind of clean cigarette taste removal dust removal environment-protecting machine, and equipment volume is little, and cost is low, is convenient to install, and maintenance expense is low, and result of use is good.
For achieving the above object, the present invention adopts following technical scheme:
A kind of clean cigarette taste removal dust removal environment-protecting machine, comprising:
Primary separation purification devices, be made up of water ring vacuum pump, separation water tank, several pieces of vertical baffle plates are provided with in described separation water tank, water tank is divided into several casing by baffle plate, passage is left in the below of each baffle plate, separation water tank is wherein while be provided with vertical separator tube, and under the lower end insertion separation water tank liquid level of separator tube, the upper end of separator tube is provided with unilateral gate; Its import of described water ring vacuum pump is communicated with exhanst gas outlet by flue, Water-ring vacuum pump discharge is communicated with separator tube by gas-vapor mix comb, the pipeline of Water-ring vacuum pump inlet is provided with water inlet, water inlet is communicated with separation water tank by water inlet pipe, and water ring vacuum pump, mixing comb, separator tube, separation water tank and water inlet pipe form the passage of a circulation;
The second-order separation purification devices, be made up of filter, water ring compressor, separation and purification tank, lime set plate, tank body heat radiation air duct and purifying tank extraction fan, described separation and purification tank is the vertical sealed shell of tank arranged, the bottom of tank body is by two pipeline communication water level tanks, switch is provided with in water level tank, water level tank is by water level pipeline communication separation water tank, and water level pipeline is provided with magnetic valve; Described water ring compressor import is by pipeline communication filter, the front end of filter is communicated with the top of separator tube, water ring compressor outlet is by the air inlet pipe of pipeline communication separation and purification tank, and the air inlet pipe of separation and purification tank is connected to the position above the water level of separation and purification tank; Described lime set plate at least arranges one piece, and be spaced a distance and be arranged above and below, every clotting liquid plate is provided with inclination angle, the liquid of lime set plate collection also can be caught in the upper end of the lower end aligned adapter of lime set plate, under the liquid level of separation and purification tank bottom is stretched in the lower end of adapter, separation and purification tank top is provided with purifying tank escape pipe; Described radiation air jacket casing is connected on the outside of separation and purification tank, and leaves tank body and have certain spacing to form heat dissipation wind channel, and extraction fan is located at the upper end of heat radiation air duct;
Coil condenser, be made up of fan housing in thick coil pipe, thin coil pipe, coil pipe external air hood, coil pipe, described thick coil pipe is that column spirals more than 16 meters from top to bottom, and its upper end is by pipeline communication purifying tank escape pipe, and its lower end is communicated with blast pipe one; Described thin coil pipe is that column spirals more than 5 meters from top to bottom, its upper end is communicated with the lower end of thick coil pipe, the lower end of thin coil pipe is communicated with blast pipe two, thin coil pipe is located at the below of thick coil pipe, the inner side of thick coil pipe and thin coil pipe is provided with fan housing in coil pipe, the outside of thick coil pipe and thin coil pipe is provided with coil pipe external air hood, and form coil pipe heat dissipation wind channel between fan housing in coil pipe external air hood and coil pipe, the top of coil pipe heat dissipation wind channel is provided with coil pipe extraction fan;
Terminal process equipment, be fluid purification tank, gas furnace, gas collector one wherein, wherein gas furnace is made up of large gas furnace and little gas furnace.
The pressure of described separation and purification tank inside is between 0.5 kg/cm to 2 kg/cm.
The power of described water ring compressor is greater than the power of water ring vacuum pump.
The periphery in the outside of described separation and purification tank is evenly equipped with fin.
The thick coil pipe of described coil condenser and thin coil pipe are evenly equipped with fin.
Be provided with water purification in described fluid purification tank, blast pipe one and blast pipe two insert the bottom of water purification.
Cleanser is provided with in water purification in described fluid purification tank.
Described water level pipeline is provided with water pump, and the magnetic valve of water level pipeline and water pump are synchronously opened.
Described water level pipeline is connected to separation and purification tank water surface bottom.
Described gas furnace is made up of body of heater, burner, burner is made up of top board, burner lower platen, waffle slab, the bottom of described body of heater is provided with closed furnace bottom, the middle part of body of heater is provided with burner, described burner which is provided with circular burner top board, its underpart is provided with circular burner lower platen, is provided with multilayer laminated waffle slab between top board and lower platen, is provided with body of heater air inlet pipe between burner and furnace bottom.
The course of work of the present invention: first carry out primary separation purifying, pending flue gas is communicated with the exhaust gases passes pipe of primary separation purification devices, under the effect of water ring vacuum pump, the water that flue gas and water inlet constantly spray into constantly carries out high-speed stirred by the impeller of water ring vacuum pump and mixes, produce air-water mixture, mixture enters separator tube by mixing comb, the mixing water be only absorbed by the water under gravity enters separation water tank downwards along separator tube, and unmixing gas upwards enters the second-order separation purification devices along separator tube.The mixing water flow velocity entering separation water tank slows down suddenly, in mixture, the mixture of different specific weight starts to be separated, heavy water is in bottom, other material has slowly floated on the water surface, floating superincumbent material is many to be collected by the valve opened in separation water tank with regard to needing to a certain extent, the water of bottom has blocked the floating thing of top through several baffle plate, the just basic no suspended substance of water tank below, extracted out the mixing continuing to participate in flue gas by water inlet pipe by water ring vacuum pump or the pump separately established, water like this constantly mixes with flue gas, the temperature of flue gas is considerably reduced in mixing, most of flue dust and peculiar smell and water have carried out mixed product to be existed in separation water tank.
Unmixing gas enters in the second-order separation purification devices, preposition filter first through water ring compressor filters large particle, separation and purification tank is entered again through water ring compressor, the gas entering separation and purification tank moves up, a small amount of water is also had to be pooled at the bottom of tank downwards, the gas moved up is condensed into drop and constantly enters adapter along the lime set plate current tilted when passing the aperture of multilayer lime set plate, imported in the water of tank bottom by adapter, because under the effect of water ring compressor, there is pressure separation and purification tank inside, add separation and purification tank constantly to dispel the heat to purifying tank under the effect of air exhauster, accelerate the separation of aqueous vapor, when the water of separation and purification tank bottom reaches certain water level, switch in water level tank starts magnetic valve and opens water to be extracted in separation water tank the water level of separation and purification tank is maintained in certain scope.Cigarette and the peculiar smell basic handling of passing through this process flue gas are clean, now gas carries out forced condensation from purifying tank escape pipe inflow coil condenser, condenser of the present invention is the coil pipe having certain length, gas accelerates condensation through coil pipe under the thermolysis of coil pipe extraction fan, make gas purity higher, the condensation of coil condenser is purified as terminal process equipment does last process preparation, if the gas of process is fuel gas, now the gas of process can be connected gas furnace by blast pipe one or blast pipe two to carry out burning and exhausting or other gas collection equipment and collect fuel gas and utilize, if gas is just discharged in fluid purification tank by non-combustible gas, process, after above-mentioned process, finally discharged gas has reached the requirement of country's discharge.
Contribution of the present invention there are provided a kind of clean cigarette taste removal dust removal environment-protecting machine, and this equipment volume is little, and cost is low, is convenient to install, and equipment is durable, and maintenance cost is low, and result of use is good; Owing to adopting the second-order separation purification devices, operating pressure is low, remove flue gas peculiar smell efficiency high, because of in gas in processes containing water, so not easily burning, non-explosive and easily control in the course of work.
Accompanying drawing explanation
Fig. 1 is the schematic perspective view of one of them embodiment of the present invention.
Fig. 2 is the schematic perspective view that Fig. 1 removes the second-order separation purification devices bracing frame.
Fig. 3 is the schematic perspective view at visual angle, Fig. 2 back side.
Fig. 4 is separation water tank internal structure schematic diagram.
Fig. 5 is the internal structure external structure schematic diagram of the second-order separation purification devices and coil condenser.
Fig. 6 is the heat dissipation channel schematic diagram of the second-order separation purification devices.
Fig. 7 is the heat dissipation channel schematic diagram of coil condenser.
Fig. 8 is the schematic perspective view of coil condenser.
Fig. 9 is the schematic perspective view at another visual angle of coil condenser.
Figure 10 is the schematic perspective view of the outer radiation fin of the second-order separation purification devices and coil condenser.
Figure 11 is the schematic perspective view that the body of heater of gas furnace vertically cuts a part open.
Figure 12 is the schematic perspective view looking up visual angle of Figure 11.
Detailed description of the invention
Embodiment 1:
Be the overall structure schematic diagram of one of them embodiment of the present invention as shown in Figures 1 to 4, the present invention includes: primary separation purification devices 1, the second-order separation purification devices 2, coil condenser 3 and terminal process equipment 4, described primary separation purification devices 1 is made up of water ring vacuum pump 13, separation water tank 17, water ring vacuum pump not only makes flue gas be drawn out of under suction function, also play the effect mixed of stirring and accelerating flue gas and water, the large-scale sprinkling equipment of the many employings of this procedure of traditional equipment mixes and cooled flue gas simultaneously.The vertical baffle plate of polylith 171 is provided with in described separation water tank 17, water tank is divided into several casing by dividing plate, and passage is left in the below of each baffle plate, and separation water tank is wherein provided with vertical separator tube 18, separation water tank liquid level is inserted in the lower end of separator tube, and the upper end of separator tube is provided with unilateral gate 181, described Water-ring vacuum pump inlet 131 is communicated with exhanst gas outlet by flue 11, the pipeline of the front end of water ring vacuum pump is provided with front end filter 12, slightly large particle can be filtered, Water-ring vacuum pump discharge 132 is communicated with separator tube by gas-vapor mix comb 16, the pipeline of Water-ring vacuum pump inlet is provided with water inlet 15, water inlet is communicated with separation water tank 17 by water inlet pipe 151, another water pipe 14 connecting separation water tank connects water ring vacuum pump, it is made normally to work to water ring vacuum pump supply water, water ring vacuum pump 13, mixing comb 16, separator tube 18, separation water tank 17 and water inlet pipe 151 form the passage of a circulation.The present invention adopt water ring vacuum pump not only equipment volume significantly reduce, also play the effect of Forced Mixing, the efficiency that flue gas is mixed in water is higher.
As shown in Fig. 5 to Figure 10, described the second-order separation purification devices 2, by filter 27, water ring compressor 26, separation and purification tank 22, lime set plate 24, tank body heat radiation air duct 21 and purifying tank extraction fan 28 form, described separation and purification tank is the vertical sealed shell of tank arranged, the bottom of tank body is communicated with water level tank 25 by two pipelines 251, switch is provided with in water level tank, described water ring compressor import 262 is by pipeline communication filter 27, the front end of filter is communicated with the top of separator tube 18, water ring compressor outlet 261 is by the air inlet pipe 221 of pipeline communication separation and purification tank, the air inlet pipe of separation and purification tank is connected to the position above the water level of separation and purification tank, described lime set plate 24 at least arranges one piece and is spaced a distance and is arranged above and below, every clotting liquid plate is provided with inclination angle, the liquid of lime set plate collection also can be caught in the upper end of the lower end aligned adapter 23 of lime set plate, under the liquid level of separation and purification tank bottom is stretched in the lower end of adapter, separation and purification tank top is provided with purifying tank escape pipe 222, described heat radiation air duct 21 is socketed in the outside of separation and purification tank, and leaving tank body has certain spacing to form heat dissipation wind channel, extraction fan 28 is located at the upper end of heat radiation air duct, because under the effect of water ring compressor, there is pressure separation and purification tank inside, add separation and purification tank constantly to dispel the heat under the effect of air exhauster, accelerate the separation of aqueous vapor, make the efficiency of the gas separaion that can not incorporate in water higher.
Described coil condenser 3, be made up of fan housing 34 in thick coil pipe 31, thin coil pipe 32, coil pipe external air hood 33, coil pipe, described thick coil pipe is that column spirals more than 16 meters from top to bottom, and its upper end is by pipeline communication purifying tank escape pipe, and its lower end is communicated with blast pipe 1; Described thin coil pipe is that column spirals more than 5 meters from top to bottom, wherein one end is communicated with the lower end of thick coil pipe, the other end of thin coil pipe is communicated with blast pipe 2 312, thin coil pipe is located at the below of thick coil pipe, the inner side of thick coil pipe and thin coil pipe is provided with fan housing in coil pipe, the outside of thick coil pipe and thin coil pipe is provided with coil pipe external air hood, and form coil pipe heat dissipation wind channel between fan housing in coil pipe external air hood and coil pipe, the top of coil pipe heat dissipation wind channel is provided with coil pipe extraction fan 35;
Described terminal process equipment 4, be fluid purification tank 41, gas furnace 42, gas collector one wherein, wherein gas furnace 42 is made up of large gas furnace and little gas furnace.
The pressure of described separation and purification tank 22 inside is between 0.5 kg/cm to 2 kg/cm.The power of described water ring compressor 26 is greater than the power of water ring vacuum pump 13.The periphery in the outside of described separation and purification tank 22 is evenly equipped with fin 223, arranges fin radiating effect better.The thick coil pipe of described coil condenser and thin coil pipe are evenly equipped with fin 313.Be provided with water purification in described fluid purification tank 41, blast pipe one and blast pipe two insert the bottom of water purification.Cleanser is provided with in water purification in described fluid purification tank 41.Burn different its cleansers of material different, select according to different flue gases in work, cleanser as, fume-clarifying agent for reducing smoke and dust and desulfurizing, limewash, garbage-incineration smoke purifying agent etc.
As shown in Figure 11,12, described gas furnace is made up of body of heater 421, burner, burner 422 top board 4221, burner lower platen 4222, waffle slab 4223, the bottom of described body of heater is provided with closed furnace bottom 424, the middle part of body of heater is provided with burner 422, described burner which is provided with circular burner top board 4221, its underpart is provided with circular burner lower platen 4222, multilayer laminated waffle slab 4223 is provided with between top board and lower platen, general waffle slab 1-6 layer, is provided with body of heater air inlet pipe 423 between burner and furnace bottom.Burner bottom is the cavity of sealing, only have the stacked waffle slab at circular middle part out combustion gas mix with air and burn, therefore the cavity of burner bottom does not have air at work, burning can not be produced, more there will not be the potential safety hazards such as blast, so this gas furnace work is safety and stability.If this gas furnace top arranges chimney class heat dissipation channel, the sidewall of the body of heater on burner top arranges several air intake, so that the Thorough combustion of combustion gas.
The present invention by need transform cigarette, taste gas (comprising dirt) whatsoever kind as easily burn, explosive, poisonous, corrosive, all it is changed in the process of compression moisture, through water dilution, cooling, degraded, and water in water pipe, water tank, moisture trap to be separated water outlet gentle.In the process of cooling by particulate deposits in the harmful useless gas cigarette that need remove that is mixed in flue gas in water.
The present inventor obtains good result through repetition test, in production for the treatment of waste plastic regeneration, filter screen in producing in plastics-production uses the regular hour will be cleared up by burning, burning will produce a large amount of harmful high-temperature flue gas, this flue gas environmental pollution is very large, this equipment is adopted to make the flue-gas temperature entering primary separation purification devices 1 drop to five or six ten degrees Celsius from 600-700 DEG C, and smoke which, pungent taste amount and harmful amount thing significantly reduce, the mixing water flow velocity entering separation water tank slows down suddenly, in mixture, the mixture of different specific weight starts to be separated, heavy water is in bottom, other material has slowly floated on the water surface, floating superincumbent material many just needs is to a certain extent collected by the valve 172 opened in separation water tank, heavy oil 178 can be appeared in one's mind above the flue gas water tank of process waste or used plastics, the water 5 of bottom has blocked the floating thing of top through several baffle plate, the just basic no suspended substance of water tank below, extracted out the mixing continuing to participate in flue gas by water inlet pipe by water ring vacuum pump or the pump separately established, water like this constantly mixes with flue gas, the temperature of flue gas is considerably reduced in mixing, most of flue dust and peculiar smell and water have carried out mixed product to be existed in separation water tank.
Obviously improved by the flue gas after the process of primary separation purification devices, this creates good condition for secondary transforms.The gas content now exported is about 97%, and water is about 3%.Transform through the second-order separation purification devices, this conversion is carried out pressure separation to the gas entering the second-order separation purification devices and is carried out purifying again.Because containing a large amount of moisture and particle inside the gas of primary transformants, so first will through a good particulate filter, enter liquid piston compressor again, through separation and purification tank 22 gas-water separation, while moisture trap, separation and purification tank cools, such ability is better separated water outlet, and the purity of gas is improved.Now more than 90% cigarette and taste, dirt transform all under pressure and be separated into smokeless state, again after special coil condenser strengthening condensation, moisture in gas is reduced further, remaining gas is sent in boiler and is carried out burning utilization, its discharge smoke-free and tasteless reaches the discharge standard of country, not only not to environment, also use waste gas and carry out useful utilization.
Different its equipment of flue gas of process of the present invention will adopt different materials, as process has corrosive flue gas, use corrosion-resistant material making apparatus, as stainless steel etc.
The present invention is not limited to described implementation method, and under the invention not exceeding claim is thought, for the personnel of ABC with field belonging to the present invention, can implement a lot of distortion, these modification also belong to scope of the present invention.
Claims (10)
1. a clean cigarette taste removal dust removal environment-protecting machine, is characterized in that comprising:
Primary separation purification devices (1), be made up of water ring vacuum pump (13), separation water tank (17), several pieces of vertical baffle plates (171) are provided with in described separation water tank (17), water tank is divided into several casing by baffle plate, passage is left in the below of each baffle plate, separation water tank is wherein while be provided with vertical separator tube (18), and under the lower end insertion separation water tank liquid level of separator tube, the upper end of separator tube is provided with unilateral gate (181); Its import of described water ring vacuum pump (131) is communicated with exhanst gas outlet by flue (11), Water-ring vacuum pump discharge (132) is communicated with separator tube by gas-vapor mix comb (16), the pipeline of Water-ring vacuum pump inlet is provided with water inlet (15), water inlet is communicated with separation water tank (17) by water inlet pipe (151), water ring vacuum pump (13), mixing comb (16), separator tube (18), separation water tank and water inlet pipe (151) composition passage circulated;
The second-order separation purification devices (2), be made up of filter (27), water ring compressor (26), separation and purification tank (22), lime set plate (24), tank body heat radiation air duct (21) and purifying tank extraction fan (28), described separation and purification tank is the vertical sealed shell of tank arranged, the bottom of tank body is communicated with water level tank (25) by two pipelines (251), switch is provided with in water level tank, water level tank is by water level pipeline communication separation water tank (17), and water level pipeline is provided with magnetic valve; Described water ring compressor import (262) is by pipeline communication filter (27), the front end of filter is communicated with the top of separator tube (18), water ring compressor outlet (261) is by air inlet pipe (221) of pipeline communication separation and purification tank, and the air inlet pipe of separation and purification tank is connected to the position above the water level of separation and purification tank; Described lime set plate (24) at least arranges one piece, and be spaced a distance and be arranged above and below, every clotting liquid plate is provided with inclination angle, the liquid of lime set plate collection also can be caught in the upper end of the lower end aligned adapter (23) of lime set plate, under the liquid level of separation and purification tank bottom is stretched in the lower end of adapter, separation and purification tank top is provided with purifying tank escape pipe (222); Described heat radiation air duct (21) is socketed in the outside of separation and purification tank, and leaves tank body and have certain spacing to form heat dissipation wind channel, and extraction fan (28) is located at the upper end of heat radiation air duct;
Coil condenser (3), be made up of fan housing (34) in thick coil pipe (31), thin coil pipe (32), coil pipe external air hood (33), coil pipe, described thick coil pipe is that column spirals more than 16 meters from top to bottom, its upper end is by pipeline communication purifying tank escape pipe (222), and its lower end is communicated with blast pipe one (311); Described thin coil pipe is that column spirals more than 5 meters from top to bottom, its upper end is communicated with the lower end of thick coil pipe, the lower end of thin coil pipe is communicated with blast pipe two (312), thin coil pipe is located at the below of thick coil pipe, the inner side of thick coil pipe and thin coil pipe is provided with fan housing in coil pipe, the outside of thick coil pipe and thin coil pipe is provided with coil pipe external air hood, and form coil pipe heat dissipation wind channel between fan housing in coil pipe external air hood and coil pipe, the top of coil pipe heat dissipation wind channel is provided with coil pipe extraction fan (35);
Terminal process equipment (4), be fluid purification tank (41), gas furnace (42), gas collector one wherein, wherein gas furnace (42) is made up of large gas furnace and little gas furnace.
2. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: the pressure of described separation and purification tank (22) inside is between 0.5 kg/cm to 2 kg/cm.
3. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: the power of described water ring compressor (26) is greater than the power of water ring vacuum pump (13).
4. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: the periphery in the outside of described separation and purification tank (22) is evenly equipped with fin (223).
5. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: the thick coil pipe of described coil condenser and thin coil pipe are evenly equipped with fin (313).
6. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: be provided with water purification in described fluid purification tank (41), blast pipe one and blast pipe two insert the bottom of water purification.
7. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: be provided with cleanser in the water purification in described fluid purification tank (41).
8. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: described water level pipeline is provided with water pump, and the magnetic valve of water level pipeline and water pump are synchronously opened.
9. one according to claim 8 clean cigarette taste removal dust removal environment-protecting machine, is characterized in that: described water level pipeline is connected to separation and purification tank water surface bottom.
10. one according to claim 1 clean cigarette taste removal dust removal environment-protecting machine, it is characterized in that: described gas furnace is by body of heater (421), burner forms, burner (422) is by top board (4221), burner lower platen (4222), waffle slab (4223) forms, the bottom of described body of heater is provided with closed furnace bottom (424), the middle part of body of heater is provided with burner (422), described burner which is provided with circular burner top board (4221), its underpart is provided with circular burner lower platen (4222), multilayer laminated waffle slab (4223) is provided with between top board and lower platen, body of heater air inlet pipe (423) is provided with between burner and furnace bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410278817.5A CN104014218B (en) | 2014-06-21 | 2014-06-21 | A kind of clean cigarette taste removal dust removal environment-protecting machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410278817.5A CN104014218B (en) | 2014-06-21 | 2014-06-21 | A kind of clean cigarette taste removal dust removal environment-protecting machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104014218A CN104014218A (en) | 2014-09-03 |
| CN104014218B true CN104014218B (en) | 2015-12-16 |
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| CN201410278817.5A Expired - Fee Related CN104014218B (en) | 2014-06-21 | 2014-06-21 | A kind of clean cigarette taste removal dust removal environment-protecting machine |
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Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107008135A (en) * | 2017-04-24 | 2017-08-04 | 克拉玛依市杰德科技有限责任公司 | One kind removes deimpurity knot screen from atm number gas stream |
| CN109331598A (en) * | 2018-12-11 | 2019-02-15 | 邹远华 | A kind of soot blower |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5445673A (en) * | 1977-09-19 | 1979-04-11 | Kobe Steel Ltd | Waste gas treatment method |
| JPH11128644A (en) * | 1997-10-29 | 1999-05-18 | Toshio Awaji | Dust removing device and dust removal |
| CN2454648Y (en) * | 2000-12-05 | 2001-10-17 | 李莹 | Sedimentation room made of toughened glass for smoke purifying device |
| CN203862082U (en) * | 2014-06-21 | 2014-10-08 | 武柔权 | Smoke cleaning smell removing dusting environmental friendly machine |
-
2014
- 2014-06-21 CN CN201410278817.5A patent/CN104014218B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5445673A (en) * | 1977-09-19 | 1979-04-11 | Kobe Steel Ltd | Waste gas treatment method |
| JPH11128644A (en) * | 1997-10-29 | 1999-05-18 | Toshio Awaji | Dust removing device and dust removal |
| CN2454648Y (en) * | 2000-12-05 | 2001-10-17 | 李莹 | Sedimentation room made of toughened glass for smoke purifying device |
| CN203862082U (en) * | 2014-06-21 | 2014-10-08 | 武柔权 | Smoke cleaning smell removing dusting environmental friendly machine |
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| CN104014218A (en) | 2014-09-03 |
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