CN2650856Y - Unitary gas purifying tower - Google Patents
Unitary gas purifying tower Download PDFInfo
- Publication number
- CN2650856Y CN2650856Y CN 200320117053 CN200320117053U CN2650856Y CN 2650856 Y CN2650856 Y CN 2650856Y CN 200320117053 CN200320117053 CN 200320117053 CN 200320117053 U CN200320117053 U CN 200320117053U CN 2650856 Y CN2650856 Y CN 2650856Y
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- Prior art keywords
- purifying column
- chamber
- moisture film
- gas
- whirlwind
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- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model discloses an integrated gas purification tower, which is characterized in: the rough purification part comprises a gas inlet pipe (1), a jet chamber (3), a water film chamber (39), and a separation chamber (16); the fine purification part comprises a cyclone purification tower (41) that stands above a horizontal part, a cyclone separator (35) and a cyclone rotor (34) are arrange in the cyclone purification tower (41), a centrifugal fan (37) and a water pump (38) are provided in the pneumatic part and the hydraulic part respectively; all parts of the equipment are connected into an integral assembly; the utility model overcomes the drawbacks of existing gas purification towers, including complex structure, large footprint, too many pipelines, and limited processing capacity; the utility model has advantages such as easy, safe, and reliable operation, small footprint, and less pipelines, and can achieve 98% or higher dust removing rate and 99% or higher desulphurization and organic exhaust gas removing efficiency, can be widely used for treatment of a variety of gas pollutants, and is especially suitable for flue gas dedusting and desulphurization for generator set, organic waste gas treatment, and treatment of gases containing heavy metal steams, etc.
Description
Technical field the utility model relates to a kind of integrated gas purifying column, more particularly, relates to the integrated gas purifying column of a kind of energy normal temperature and the various pernicious gases of high-temperature process.
Background technology in the prior art, existing all gases purifying column, but the following problem of ubiquity: the one, equipment disperses, and has complex structure, floor space is big, the pipeline configuration is many and shortcoming such as troublesome poeration; The 2nd, disposal ability is limited, generally is the special equipment at some pernicious gas, thereby needs to improve.
The summary of the invention the purpose of this utility model is to provide a kind of can handle normal temperature or high-temperature gas, can handle sulfur-bearing, dust-laden, contain organic solvent, contain the dusty gas of heavy metal steam, and can substitute or partly substitute the integrated gas purifying column of workshop ventilation.
In order to achieve the above object, the utility model provides following technical scheme: design a kind of integrated gas purifying column, by thick purification part, the smart part that purifies, aerodynamic force part and hydrodynamic partly constitute, its thick part that purifies is by gas inlet tube (1), spray chamber (3), moisture film chamber (39) and separation chamber (16) are formed, they communicate with each other and are linked to be the bottom that an integral body is lying in equipment integral body, the entrance point of spray chamber (3) is equipped with fog-spray nozzle (2), the smart part that purifies has an edge-on whirlwind purifying column (41) above horizontal part, has cyclone separator (35) in the whirlwind purifying column (41), the forward spin flow plate (30) of whirlwind (34) and cyclone separator (35), following eddy flow plate (33) is formed, have several moisture film pipes (4) in the moisture film chamber (39), separation chamber (16) is a hollow chamber, the centrifugal blower (37) of aerodynamic force part is respectively by blast pipe (15), discharge pipe (29) and separation chamber (16), cyclone separator (35) links to each other, the outlet (23) of the water pump (38) of hydrodynamic part divide two-way respectively with nozzle component (24), fog-spray nozzle (2) links to each other, the port of export of nozzle component (24) links to each other centrifugal blower (37) with whirlwind purifying column (41) top by the shower nozzle (26) of nozzle component (25) with purifying column (41) top, water pump (38) is positioned at the top of accumbency part.Waste gas enters spray chamber (3) flow velocity by gas inlet tube (1) and slows down, through fog-spray nozzle (2) spraying the temperature of waste gas, nuisance content are decreased, the air-flow of carrying atomized water secretly enters moisture film chamber (39), between several moisture film pipes (4), detour, make the solubility pollutant enter liquid phase, and further reduce temperature, gas in the separation chamber (16) owing to slow down and anxious turning round, get rid of the globule that major part is carried secretly, enter fan wind inleting tube (15).
The utility model technical scheme preferably is: several moisture film pipes (4) in moisture film chamber (39) are multilayer and tilt to be staggered, the upper end of moisture film pipe (4) is by location-plate (6) phase fastening position, insert in the locating shaft core pipe (5) lower end, in addition, below in overflow liquid reducing chamber (10), the top of each moisture film pipe (4) has liquid reducing hole (7).Because being multilayer, moisture film pipe (4) tilts to be staggered, with airflow direction angle is arranged, the upwards component of gas shock on tube wall is brought in constant renewal in moisture film, constantly absorb from grit in the waste gas and heat, can remove most of grit, being staggered detours air-flow complications between pipe, helps getting rid of grit by inertia and turbulent flow, make the solubility dusty gas enter liquid phase, and further reduce temperature.
The utility model technical scheme preferably can be: in discharge pipe (29) outlet shower nozzle (28) is housed, the emission direction of shower nozzle (28) is along airflow direction, in addition, purifying column (41) epimere has regenerated liquid return duct (31), and air-flow eddy flow and following time in cyclone separator sprays into the atomizing globule twice, once sprayed into by shower nozzle (28), another time is by regenerated liquid return duct (31), and spray head (32) sprays into, the atomized water that twice downstream direction sprays into, the dust better effects if in the adsorption gas flow.
The utility model technical scheme preferably can be again: the outlet (23) of water pump (38) has to the pipe tap of regenerated liquid storage tank, is convenient to feedwater.
The utility model technical scheme preferably can also be: whirlwind purifying column (41) bottom has desilting mouth (36), is convenient to clear up mud.
Compared with prior art, the utlity model has following tangible advantage: 1, of many uses: can be used for the processing of multiple dusty gas, comprise generating set flue-gas dust-removing and desulfurization, organic exhaust gas processing, contain the gas treatment of heavy metal steam etc.; 2, easy and simple to handle: can be unattended, and can become an automatic system operation with other equipment are chain; 3, efficient height: dust removal efficiency reaches more than 98%, because desulfurization and remove organic exhaust gas, when being equipped with suitable medicament, efficient can reach more than 99%; 4, operation is safe and reliable to operation, quick for installation; 5, floor space is little, and it is few to set up pipeline.
Be description of drawings of the present utility model below the description of drawings:
Fig. 1 is a frame structure schematic diagram of the present utility model;
Fig. 2 is an overall structure schematic diagram of the present utility model;
Fig. 3 is an overall structure vertical view of the present utility model;
Fig. 4 is a horizontal thick purification portion separation structure schematic diagram of the present utility model;
Fig. 5 is the vertical view of Fig. 4;
Fig. 6 is the A-A rotational structure schematic diagram of Fig. 4;
Fig. 7 is the II-II enlarged drawing of Fig. 4;
Fig. 8 is the I-I enlarged drawing of Fig. 4;
Fig. 9 is a smart purification portion separation structure schematic diagram of the present utility model;
Figure 10 is the smart side structure schematic diagram that purifies part of the present utility model.
Among Fig. 1～Figure 10, the 1st, gas inlet tube, the 2nd, fog-spray nozzle, the 3rd, spray chamber, the 4th, moisture film pipe, the 5th, locating shaft core pipe, the 6th, location-plate, the 7th, liquid reducing hole, the 8th, the water hole of both sides, the 9th, the chamber base plate that crouches, the 10th, overflow liquid reducing chamber, the 11st, liquid reducing chamber cover plate, the 12nd, side tank and liquid level control flume, the 13rd, water pump installing hole, the 14th, fan supporter, the 15th, blast pipe, the 16th, the separation chamber, the 17th, the chamber top board crouches, the 18th, soil cleaning port, the 19th, the chamber wallboard that crouches, the 20th, downflow weir, the 21st, overfall, the 22nd, the cyclone separator awl end, the 23rd, outlet, the 24th, nozzle component, the 25th, nozzle component, the 26th, shower nozzle, the 27th, cyclone separator top board, the 28th, shower nozzle, the 29th, discharge pipe, the 30th, the forward spin flow plate, the 31st, the regenerated liquid return duct, the 32nd, regenerated liquid is mended into spray head, the 33rd, following eddy flow plate, the 34th, whirlwind, the 35th, cyclone separator, the 36th, desilting mouth, the 37th, centrifugal blower, the 38th, water pump, the 39th, moisture film chamber, the 41st, whirlwind purifying column.
By specific embodiment the utility model is carried out more detailed description below the specific embodiment:
With reference to Fig. 1,2,3,9,10, the integrated gas purifying column is by thick purification part, the smart part that purifies, aerodynamic force part and hydrodynamic partly constitute, the top of gas purification tower has exhaust outlet, the thick part that purifies is by gas inlet tube (1), spray chamber (3), moisture film chamber (39) and separation chamber (16) are formed, they communicate with each other and are linked to be the bottom that an integral body is lying in equipment integral body, the entrance point of spray chamber (3) is equipped with fog-spray nozzle (2), the smart part that purifies has an edge-on whirlwind purifying column (41) above horizontal part, has cyclone separator (35) in the whirlwind purifying column (41), the forward spin flow plate (30) of whirlwind (34) and cyclone separator (35), following eddy flow plate (33) is formed, have several moisture film pipes (4) in the moisture film chamber (39), separation chamber (16) is a hollow chamber, the centrifugal blower (37) of aerodynamic force part is respectively by blast pipe (15), discharge pipe (29) and separation chamber (16), cyclone separator (35) links to each other, the outlet (23) of the water pump (38) of hydrodynamic part divide two-way respectively with nozzle component (24), fog-spray nozzle (2) links to each other, the port of export of nozzle component (24) links to each other centrifugal blower (37) with purifying column (41) top by the shower nozzle (26) of nozzle component (25) with whirlwind purifying column (41) top, water pump (38) is positioned at the top of accumbency part.
With reference to Fig. 4～8, moisture film pipe (4) in the moisture film chamber (39) is multilayer and tilts to be staggered, and the upper end of moisture film pipe (4) is by location-plate (6) phase fastening position, and insert in the locating shaft core pipe (5) lower end, below in overflow liquid reducing chamber (10), the top of each moisture film pipe (4) has liquid reducing hole (7).
With reference to Fig. 9,10, in discharge pipe (29) outlet shower nozzle (28) is housed, the emission direction of shower nozzle (28) is along airflow direction.
With reference to Fig. 1,2,6, whirlwind purifying column (41) epimere has regenerated liquid return duct (31).
With reference to Fig. 1, the outlet (23) of water pump (38) has to the pipe tap of regenerated liquid storage tank.
With reference to Fig. 9,10, whirlwind purifying column (41) bottom has desilting mouth (36).
Claims (7)
1, a kind of integrated gas purifying column, by thick purification part, the smart part that purifies, aerodynamic force part and hydrodynamic partly constitute, the top of gas purification tower has exhaust outlet, it is characterized in that: the thick part that purifies is by gas inlet tube (1), spray chamber (3), moisture film chamber (39) and separation chamber (16) are formed, they communicate with each other and are linked to be the bottom that an integral body is lying in equipment integral body, the entrance point of spray chamber (3) is equipped with fog-spray nozzle (2), the smart part that purifies has an edge-on whirlwind purifying column (41) above horizontal part, has cyclone separator (35) in the whirlwind purifying column (41), the forward spin flow plate (30) of whirlwind (34) and cyclone separator (35), following eddy flow plate (33) is formed, have several moisture film pipes (4) in the moisture film chamber (39), separation chamber (16) is a hollow chamber, the centrifugal blower (37) of aerodynamic force part is respectively by blast pipe (15), discharge pipe (29) and separation chamber (16), cyclone separator (35) links to each other, the outlet (23) of the water pump (38) of hydrodynamic part divide two-way respectively with nozzle component (24), fog-spray nozzle (2) links to each other, the port of export of nozzle component (24) links to each other centrifugal blower (37) with purifying column (41) top by the shower nozzle (26) of nozzle component (25) with whirlwind purifying column (41) top, water pump (38) is positioned at the top of accumbency part.
2, purifying column according to claim 1 is characterized in that: the moisture film pipe (4) in moisture film chamber (39) is multilayer and tilts to be staggered, and the upper end of moisture film pipe (4) is by location-plate (6) phase fastening position, and insert in the locating shaft core pipe (5) lower end.
3, purifying column according to claim 2 is characterized in that: the below in overflow liquid reducing chamber (10), the top of each moisture film pipe (4) has liquid reducing hole (7).
4, purifying column according to claim 1 is characterized in that: in discharge pipe (29) outlet shower nozzle (28) is housed, the emission direction of shower nozzle (28) is along airflow direction.
5, purifying column according to claim 1 is characterized in that: whirlwind purifying column (41) epimere has regenerated liquid return duct (31).
6, purifying column according to claim 1 is characterized in that: the outlet (23) of water pump (38) has to the pipe tap of regenerated liquid storage tank.
7, purifying column according to claim 1 is characterized in that: whirlwind purifying column (41) bottom has desilting mouth (36).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320117053 CN2650856Y (en) | 2003-10-13 | 2003-10-13 | Unitary gas purifying tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320117053 CN2650856Y (en) | 2003-10-13 | 2003-10-13 | Unitary gas purifying tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2650856Y true CN2650856Y (en) | 2004-10-27 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200320117053 Expired - Fee Related CN2650856Y (en) | 2003-10-13 | 2003-10-13 | Unitary gas purifying tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2650856Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102160953A (en) * | 2011-03-02 | 2011-08-24 | 深圳市华伦天成科技开发有限公司 | Cyclone flat bag dust collector |
| CN102614733A (en) * | 2012-04-09 | 2012-08-01 | 萧钠 | Air-supply desulfurization dust-control device of household cooking range |
| CN102657990A (en) * | 2012-05-07 | 2012-09-12 | 陕西紫兆环保产业开发有限责任公司 | Gas purification tower |
| CN105396401A (en) * | 2015-12-23 | 2016-03-16 | 天津赛智科技发展有限公司 | Aerodynamic atomizing, mixing and separating apparatus with gas-water separation wind channel |
| CN105413361A (en) * | 2015-12-23 | 2016-03-23 | 天津赛智科技发展有限公司 | Pneumatic atomization mixing and separating device |
-
2003
- 2003-10-13 CN CN 200320117053 patent/CN2650856Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102160953A (en) * | 2011-03-02 | 2011-08-24 | 深圳市华伦天成科技开发有限公司 | Cyclone flat bag dust collector |
| CN102160953B (en) * | 2011-03-02 | 2012-12-12 | 深圳市华伦天成科技开发有限公司 | Cyclone flat bag dust collector |
| CN102614733A (en) * | 2012-04-09 | 2012-08-01 | 萧钠 | Air-supply desulfurization dust-control device of household cooking range |
| CN102657990A (en) * | 2012-05-07 | 2012-09-12 | 陕西紫兆环保产业开发有限责任公司 | Gas purification tower |
| CN105396401A (en) * | 2015-12-23 | 2016-03-16 | 天津赛智科技发展有限公司 | Aerodynamic atomizing, mixing and separating apparatus with gas-water separation wind channel |
| CN105413361A (en) * | 2015-12-23 | 2016-03-23 | 天津赛智科技发展有限公司 | Pneumatic atomization mixing and separating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |