CN201744264U - Large-energy precise flue gas treatment device - Google Patents
Large-energy precise flue gas treatment device Download PDFInfo
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- CN201744264U CN201744264U CN2010202435128U CN201020243512U CN201744264U CN 201744264 U CN201744264 U CN 201744264U CN 2010202435128 U CN2010202435128 U CN 2010202435128U CN 201020243512 U CN201020243512 U CN 201020243512U CN 201744264 U CN201744264 U CN 201744264U
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- tank body
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- steam treatment
- main tank
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Abstract
The utility model discloses a large-energy precise flue gas treatment device which comprises a main tank body (1), a flue gas inlet (3) is arranged at the lower part of the side wall of the main tank body (1), the main tank body (1) is partly filled with water (4), a water collector (5) is arranged in water (4), the bottom of the water collector (5) is positioned below the level of water (4) and connected with the side wall of the main tank body (1), a floater/steam treatment device (6) is arranged above the water collector (5), a tar/steam treatment device (7) is arranged above the floater/steam treatment device (6), the top part of the main tank body (1) is connected with a flue gas inlet (3) on an auxiliary tank body (2) through a connecting pipe (8), a floater/steam treatment device (6) and a tar/steam treatment device (7) are arranged in the auxiliary tank body (2) from bottom to top, and the top of the auxiliary tank body (2) is connected with an outlet pipe (9). The large-energy precise flue gas treatment device is used conveniently, has novel structure, and can enable the flue gas after treatment to meet the technical requirement of a generator on gas.
Description
Technical field
The utility model relates to the biomass energy apparatus field, especially prepares the equipment that purifies flue gas in the process in living beings, the accurate flue-gas treater of a kind of specifically macro-energy.
Background technology
The development of society has driven the demand of the energy, and the pressure of primary energy (coal, oil etc.) supply and the enhancing of human environmental consciousness make regenerative resource be subjected to domestic and international scientist's extensive concern.Living beings have wide, the sustainable supply of distribution, transform characteristics such as convenient, and very suitable China's national situation has application promise in clinical practice.But prior biological matter preparation flow, majority be directly the fume emission that produces in the system carbon process in atmosphere, both polluted environment, wasted the energy again.Living beings are when high temperature cabonization, its thermal decomposition product is very complicated mist, wherein comprises hundreds of hydrocarbons at least, and some condensation at normal temperatures forms tar, some incondensable gas can directly use as gaseous fuel, is pretty good middle calorific value destructive distillation gas.Therefore, prepare in the process in living beings, how integrated treatment living beings prepare the material that produces in the process, just become the problem that needs solution of biting.
The utility model content
The purpose of this utility model is the defective at prior art, and a kind of easy to use, the accurate flue-gas treater of macro-energy that can do fine processing to the water vapour, tar and the floating thing that contain in the flue gas is provided.
The purpose of this utility model solves by the following technical programs:
The accurate flue-gas treater of a kind of macro-energy, comprise main tank body, the lower sidewall of described main tank body is provided with gas approach, be filled with part water in the main tank body, water collector is set in the water, the bottom of water collector links to each other under the horizontal plane of water and with the sidewall of main tank body, the top of water collector is provided with floating thing steam treatment device, the top of floating thing steam treatment device is provided with tar and steam treatment device, the top of main tank body links to each other with gas approach on the auxiliary tank body by tube connector, set gradually floating thing steam treatment device and tar and steam treatment device from down to up in auxiliary tank body, the top of auxiliary tank body links to each other with outlet.
Described floating thing steam treatment device is connected with the madial wall contact of main tank body and auxiliary tank body with tar and steam treatment device.
The center line of the gas approach on the described main tank wall is positioned at the middle part of main tank body water.
The top of described gas approach sets gradually sewage draining exit, water supplement port and gas bypass import on the same sidewall of main tank body.
Described sewage draining exit be positioned at gas approach directly over, the bottom of sewage draining exit is concordant with the horizontal plane of water.
Described water supplement port is directly over the sewage draining exit and between water collector and floating thing steam treatment device.
Described gas bypass import is positioned at the upside of tar and steam treatment device, and the pipeline place that links to each other with the gas bypass import is provided with valve.
On the sidewall of described main tank body visor is set, visor and sewage draining exit are symmetricly set on the both sides of main tank body, and visor is identical with the center line of sewage draining exit.
The bottom of described auxiliary tank body is provided with sewage draining exit, and sewage draining exit is positioned at a side bottom opposite with gas approach on the auxiliary tank body.
The utility model has following advantage compared to existing technology:
1, the utility model has been owing to adopted two tank bodies and a plurality of floating thing steam treatment device and tar and steam treatment device, thus the utility model to remove the ability of tar, water vapour and floating thing in use strong;
2, the utility model is owing at first adopt water as cleaning of substances, so the tar that contains in the flue gas and floating thing can be handled fully, and simultaneous temperature is further reduced;
3, not moisture in the auxiliary tank body of the utility model owing to employing, so water vapour can obtain fine processing by multilayer floating thing steam treatment device, tar and steam treatment device the time;
4, the utility model is provided with valve owing to adopting in gas bypass import department, the feasible mode that can select flue gas is carried out fine processing according to actual needs;
5, the utility model novel structure, long service life suit to promote the use of in living beings preparation and research field.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model.
Wherein: 1-master's tank body; 2-assists tank body; The 3-gas approach; 4-water; The 5-water collector; 6-floating thing floating thing steam treatment device; 7-tar and floating thing steam treatment device; The 8-tube connector; The 9-outlet; The 10-sewage draining exit; The 11-water supplement port; The import of 12-gas bypass; The 13-valve; The 14-visor.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is further described.
As shown in the figure: the accurate flue-gas treater of a kind of macro-energy, comprise main tank body 1, on the same sidewall of main tank body 1, set gradually gas approach 3, sewage draining exit 10, water supplement port 11 and gas bypass import 12 from down to up.Be filled with part water 4 in the main tank body 1, water collector 5 is set in the water 4, the bottom of water collector 5 links to each other under the horizontal plane of water 4 and with the sidewall of main tank body 1, the top of water collector 5 is provided with floating thing steam treatment device 6, the top of floating thing steam treatment device 6 is provided with tar and steam treatment device 7, the top of main tank body 1 links to each other with gas approach 3 on the auxiliary tank body 2 by tube connector 7, set gradually floating thing steam treatment device 6 and tar and steam treatment device 7 from down to up in auxiliary tank body 2 inside, the top of auxiliary tank body 2 links to each other with outlet 9.Wherein, the center line of the gas approach 3 on main tank body 1 sidewall residing position on main tank body 1 sidewall is positioned at the middle part of water 4; Sewage draining exit 10 be positioned at gas approach 3 directly over, the bottom of sewage draining exit 10 is concordant with the horizontal plane of water 4; Water supplement port 11 is directly over the sewage draining exit 10 and between water collector 5 and floating thing steam treatment device 6; Gas bypass import 12 is positioned at the upside of tar and steam treatment device 6, and the pipeline place that links to each other with gas bypass import 12 is provided with valve 13.Simultaneously, visor 14 is set also on the sidewall of main tank body 1, visor 14 and sewage draining exit 10 are symmetricly set on the both sides of main tank body 1, and visor 14 is identical with the center line of sewage draining exit 10.On the outer wall of auxiliary tank body 2, the gas approach 3 on sidewall and the outlet 9 at top, also be provided with sewage draining exit 10 in the bottom of auxiliary tank body 2, sewage draining exit 10 is positioned on the auxiliary tank body 2 side bottom opposite with gas approach 3.
As shown in Figure 1, the utility model is when implementing, flue gas overcomes laggard the becoming owner of in the tank body 1 of resistance of hydraulic head from gas approach 3, flue gas in entering water 4 after, the part tar and the floating thing that contain in the flue gas will be trapped within the water, and float on the water surface from sewage draining exit 10 and discharge, water collector 5 is used to remove smoke and impacts the water wave that water 4 is produced simultaneously; Flue gas from water 4 through after, contact with multilayer floating thing steam treatment device 6, tar and the steam treatment device 7 of main tank interior respectively, multilayer floating thing steam treatment device 6, tar and steam treatment device 7 are adsorbed on the most of water vapor that contains in the flue gas, tar and floating thing on its device, and are pooled under the effect of gravity in the water 4 through sewage draining exit 10 discharges.Then the flue gas of handling in main tank body 1 enters auxiliary tank body 2 by tube connector 8 from the gas approach 3 of assisting tank body 2, in auxiliary tank body 2, contact with multilayer floating thing steam treatment device 6, tar and steam treatment device 7 once more, multilayer floating thing steam treatment device 6, tar and 7 pairs of flue gases of steam treatment device in the auxiliary tank body 2 carry out fine processing, can separate 98% water vapour, tar and floating thing in the flue gas, reach the specification requirement of igniting even generator gas.
The utility model also can directly enter auxiliary tank body 2 from gas bypass import 12 by tube connector 8 with flue gas and carry out fine processing when implementing.Concrete enforcement can be selected according to actual conditions.
Claims (9)
1. the accurate flue-gas treater of a macro-energy, comprise main tank body (1), the lower sidewall that it is characterized in that described main tank body (1) is provided with gas approach (3), be filled with part water (4) in the main tank body (1), water collector (5) is set in the water (4), the bottom of water collector (5) links to each other under the horizontal plane of water (4) and with the sidewall of main tank body (1), the top of water collector (5) is provided with floating thing steam treatment device (6), the top of floating thing steam treatment device (6) is provided with tar and steam treatment device (7), the top of main tank body (1) links to each other with gas approach (3) on the auxiliary tank body (2) by tube connector (8), set gradually floating thing steam treatment device (6) and tar and steam treatment device (7) in auxiliary tank body (2) from down to up, the top of auxiliary tank body (2) links to each other with outlet (9).
2. the accurate flue-gas treater of macro-energy according to claim 1 is characterized in that described floating thing steam treatment device (6) is connected with the madial wall contact of main tank body (1) and auxiliary tank body (2) with tar and steam treatment device (7).
3. the accurate flue-gas treater of macro-energy according to claim 1 is characterized in that the center line of the gas approach (3) on described main tank body (1) sidewall is positioned at the middle part of main tank body (1) water (4).
4. the accurate flue-gas treater of macro-energy according to claim 1 is characterized in that the top of described gas approach (3) sets gradually sewage draining exit (10), water supplement port (11) and gas bypass import (12) on the same sidewall of main tank body (1).
5. according to claim 1 or the accurate flue-gas treaters of 4 described macro-energy, it is characterized in that described sewage draining exit (10) be positioned at gas approach (3) directly over, the bottom of sewage draining exit (10) is concordant with the horizontal plane of water (4).
6. according to claim 1 or the accurate flue-gas treaters of 4 described macro-energy, it is characterized in that described water supplement port (11) is directly over the sewage draining exit (10) and be positioned between water collector (5) and the floating thing steam treatment device (6).
7. according to claim 1 or the accurate flue-gas treater of 4 described macro-energy, it is characterized in that described gas bypass import (12) is positioned at the upside of tar and steam treatment device (7), the pipeline place that links to each other with gas bypass import (12) is provided with valve (13).
8. according to claim 1 or the accurate flue-gas treater of 4 described macro-energy, it is characterized in that on the sidewall of described main tank body (1) visor (14) being set, visor (14) and sewage draining exit (10) are symmetricly set on the both sides of main tank body (1), and visor (14) is identical with the center line of sewage draining exit (10).
9. the accurate flue-gas treater of macro-energy according to claim 1 is characterized in that the bottom of described auxiliary tank body (2) is provided with sewage draining exit (10), and sewage draining exit (10) is positioned at auxiliary tank body (2) and goes up a side bottom opposite with gas approach (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202435128U CN201744264U (en) | 2010-06-30 | 2010-06-30 | Large-energy precise flue gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202435128U CN201744264U (en) | 2010-06-30 | 2010-06-30 | Large-energy precise flue gas treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201744264U true CN201744264U (en) | 2011-02-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202435128U Expired - Fee Related CN201744264U (en) | 2010-06-30 | 2010-06-30 | Large-energy precise flue gas treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201744264U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102746904A (en) * | 2012-07-04 | 2012-10-24 | 卓寿镛 | Treating device and treating process for waste gas produced in pyrolysis of waste rubber and plastics |
-
2010
- 2010-06-30 CN CN2010202435128U patent/CN201744264U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102746904A (en) * | 2012-07-04 | 2012-10-24 | 卓寿镛 | Treating device and treating process for waste gas produced in pyrolysis of waste rubber and plastics |
| CN102746904B (en) * | 2012-07-04 | 2014-02-12 | 陈湘君 | Treating device and treating process for waste gas produced in pyrolysis of waste rubber and plastics |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110216 Termination date: 20140630 |
|
| EXPY | Termination of patent right or utility model |