CN215693130U - Odor collecting system - Google Patents
Odor collecting system Download PDFInfo
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- CN215693130U CN215693130U CN202122249783.5U CN202122249783U CN215693130U CN 215693130 U CN215693130 U CN 215693130U CN 202122249783 U CN202122249783 U CN 202122249783U CN 215693130 U CN215693130 U CN 215693130U
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- tank
- reaction tank
- odor
- sludge
- pump
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- 238000006243 chemical reaction Methods 0.000 claims abstract description 38
- 239000010802 sludge Substances 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000006228 supernatant Substances 0.000 claims abstract description 4
- 238000011282 treatment Methods 0.000 claims description 30
- 239000010865 sewage Substances 0.000 claims description 26
- 239000007789 gas Substances 0.000 claims description 16
- 238000004062 sedimentation Methods 0.000 claims description 16
- 239000002912 waste gas Substances 0.000 claims description 11
- 238000009826 distribution Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 3
- 239000002245 particle Substances 0.000 abstract description 4
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- 238000010168 coupling process Methods 0.000 abstract 3
- 238000005859 coupling reaction Methods 0.000 abstract 3
- 238000010981 drying operation Methods 0.000 abstract 1
- 238000004332 deodorization Methods 0.000 description 8
- 230000032258 transport Effects 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 6
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 239000003337 fertilizer Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000010815 organic waste Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
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- 238000011221 initial treatment Methods 0.000 description 2
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- 208000024891 symptom Diseases 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 206010010071 Coma Diseases 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 206010028813 Nausea Diseases 0.000 description 1
- 208000005374 Poisoning Diseases 0.000 description 1
- 208000013738 Sleep Initiation and Maintenance disease Diseases 0.000 description 1
- 206010047700 Vomiting Diseases 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
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- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
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- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
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- Treatment Of Sludge (AREA)
- Treating Waste Gases (AREA)
Abstract
The application provides an odor collecting system, including two sets of odor discharge systems, two sets of discharge systems are provided with the machine pump, the machine pump has the flow divider through the tube coupling, the flow divider is connected with light pollution module and heavy pollution module, light pollution module has just heavy pond through the tube coupling, just sink the supernatant of pond rear end and derive to synthesize the equalizing basin through the water pump in, heavy pollution module has the effluent water sump through the tube coupling, gas is leading-in to the reaction tank in by the air pump, the reaction tank is including first reaction tank, second reaction tank and third reaction tank. According to the utility model, a plurality of groups of sludge with different particle sizes are transported through the screw conveyor, and the sludge is solarized through the sludge bucket, so that the subsequent drying operation is facilitated.
Description
Technical Field
The utility model relates to the field of waste gas treatment equipment, in particular to an odor collecting system.
Background
The offensive odor is mainly caused by putrefaction of various organic substances, mold odor of organisms, odor of pesticides and chemicals, odor of raw materials or intermediate products and paints in the production process, and putrefaction odor of various domestic wastes, etc.
The evaluation of the malodors is highly subjective, and different people feel different malodors with different intensities. Malodors are typically produced by ammonia, methyl mercaptan, hydrogen sulfide, methyl sulfide, dimethyl sulfide, trimethylamine, acetaldehyde, styrene, and the like. The malodor can cause discomfort to people, influence the metabolism of people through the nervous system, and cause dizziness, nausea, vomiting, insomnia and other symptoms, and in severe cases, the malodor can also cause poisoning symptoms such as coma and the like. So that the odor needs to be collected and treated before being discharged.
However, the existing deodorization device only treats the odor simply, and the deodorization is not thorough, so that the odor can be continuously generated.
SUMMERY OF THE UTILITY MODEL
The utility model mainly aims to provide an odor collecting system which can effectively solve the problems in the background technology.
In order to achieve the purpose, the utility model adopts the technical scheme that:
a malodor collection system comprising: two sets of odor emission systems are provided with mechanical pumps which are connected with a flow divider through pipelines, the flow divider is connected with two sets of branch pipes and respectively connected with a light pollution module and a heavy pollution module, the communication between the light pollution module and the heavy pollution module is controlled through the flow divider, a corresponding deodorization module is selected according to the pollution index,
the light pollution module is connected with a primary sedimentation tank through a pipeline, the primary sedimentation tank carries out primary treatment on the imported sewage and waste gas, the settled impurities are periodically salvaged and treated, the supernatant at the rear end of the primary sedimentation tank is led out to a comprehensive regulation tank through a water pump, the inside of the comprehensive regulation tank regulates the water tank through chemical agents, the comprehensive regulation tank further purifies the sewage,
the heavy pollution module has the effluent water sump through the pipe connection, the effluent water sump carries out sedimentation treatment with the sewage and the waste gas of deriving, separates after sedimentation treatment of effluent water sump, and gas is leading-in to the reaction tank in by the air pump, the reaction tank is including first reaction tank, second reaction tank and third reaction tank, first reaction tank, second reaction tank and third reaction tank are inside all to be provided with the treatment fluid, and leading-in first reaction tank, second reaction tank and the third reaction tank of stink carry out the deodorization operation, carry out parallelly connected processing after shunting gas simultaneously through three group's structures, promote purification efficiency.
Preferably, the effluent water sump is with liquid and the mud of bottom by the leading-in sludge impoundment, separate processing, promote treatment effeciency, sludge impoundment rear end is provided with screw conveyer, screw conveyer is provided with first screw conveyer, second screw conveyer, third screw conveyer and fourth screw conveyer, screw conveyer can level, slope or vertical transport, have simple structure, the cross-sectional area is little, advantages such as leakproofness is good, realize transporting sludge to the sludge bucket through first screw conveyer, second screw conveyer, third screw conveyer and fourth screw conveyer, transport the mud of multiunit different particle sizes through first screw conveyer, second screw conveyer, third screw conveyer and fourth screw conveyer.
Preferably, the screw conveyer rear end is provided with the sludge bucket, exposes to the sun mud through the sludge bucket, subsequent stoving operation of being convenient for, the sludge bucket will expose to the sun the mud of storage and transport first hydroextractor and second hydroextractor in, carry out wind-force and electric heat through first hydroextractor and second hydroextractor and dry, through the preliminary treatment of sludge bucket, reduce the consumption of follow-up dewatering equipment energy, carry the sludge bucket with the mud of bottom through screw conveyer and dry after filtering, be rich in a large amount of organic matters in the mud, can be used as fertilizer after the follow-up processing, promote the environment-friendly.
Preferably, the integrated regulation tank is connected with an accident tank through a pipeline, the accident tank is one of the structures required in the sewage treatment process, the reason is that after production accidents of the factories, organic waste water with high concentration and large pH value fluctuation is discharged in a short time, if the waste water directly enters the sewage treatment system, the waste water can bring high impact load to the running biological treatment system, the influence can be recovered for a long time, and sometimes fatal damage can be caused.
Preferably, the accident pond collects and guides out untreated wastewater, gas on the upper layer of the accident pond is pumped into the water distribution well through the gas pump, and the water distribution well can filter and adsorb upper layer waste gas to improve the treatment efficiency of odor.
Preferably, the machine pump comprises a first machine pump and a second machine pump, and the sewage is communicated with the odor and is pumped out together through the two sets of machine pumps, so that the deodorization efficiency is improved.
Compared with the prior art, the utility model has the following beneficial effects:
1. the light pollution module has the primary sedimentation tank through the pipe connection, the accident pond is the required structure of sewage treatment in-process, the reason lies in after the production accident appears in these mills, can discharge the high concentration of amplification and the big organic waste water of pH value fluctuation in the short time, these waste water if direct entering sewage treatment system, can bring very high impact load for the biological treatment system in service, the influence that causes needs to recover for a long time, can cause fatal destruction sometimes, the distribution well can filter upper waste gas and adsorb the processing, promote the treatment effeciency to the foul smell.
2. The heavy pollution module has the effluent water sump through the pipe connection, through first screw conveyer, second screw conveyer, third screw conveyer and fourth screw conveyer come to transport the mud of the different particle diameters of multiunit, come to insolate mud through the sludge bucket, be convenient for subsequent stoving operation, carry out wind-force and electric heat through first hydroextractor and second hydroextractor and dry, preliminary treatment through the sludge bucket, reduce the consumption of follow-up dewatering equipment energy, carry the mud of bottom to dry after filtering in the sludge bucket through screw conveyer, be rich in a large amount of organic matters in the mud, can be as fertilizer after the follow-up treatment, promote the environment-friendly.
Drawings
Fig. 1 is an overall configuration diagram of an odor collection system according to the present invention.
In the figure: 1-1, a first pump; 1-2, a second pump; 2. a comprehensive adjusting tank; 3. an accident pool; 4. a primary sedimentation tank; 5. distributing a water well; 6. a sewage tank; 7. a sludge tank; 8-1, a first screw conveyor; 8-2, a second screw conveyor; 8-3, a third screw conveyor; 8-4, a fourth screw conveyor; 9-1, a first reaction tank; 9-2, a second reaction tank; 9-3, a third reaction tank; 10. a sludge hopper; 11-1, a first dehydrator; 11-2, a second dehydrator; 12. a flow divider valve.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
In which like parts are designated by like reference numerals. 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 "bottom" and "top," "inner" and "outer" refer to directions toward and away from, respectively, the geometric center of a particular component.
Referring to fig. 1, a malodor collection system includes: the two sets of odor emission systems are provided with mechanical pumps, the mechanical pumps comprise a first mechanical pump 1-1 and a second mechanical pump 1-2, sewage is communicated with odor through the two sets of mechanical pumps and is pumped out together, the deodorization efficiency is improved, the mechanical pumps are connected with a flow dividing valve 12 through a pipeline, the flow dividing valve 12 is connected with two sets of branch pipes and is respectively connected with a light pollution module and a heavy pollution module, the communication of the light pollution module and the heavy pollution module is controlled through the flow dividing valve 12, the corresponding deodorization module is selected according to the pollution index,
the light pollution module is connected with a primary sedimentation tank 4 through a pipeline, the primary sedimentation tank 4 carries out primary treatment on the imported sewage and waste gas, the settled impurities are periodically salvaged and treated, the supernatant at the rear end of the primary sedimentation tank 4 is led out into a comprehensive adjusting tank 2 through a water pump, the interior of the comprehensive adjusting tank 2 is adjusted in a water tank through chemical agents, the sewage is further purified through the comprehensive adjusting tank 2, the comprehensive adjusting tank 2 is connected with an accident tank 3 through a pipeline, the accident tank 3 is one of the required structures in the sewage treatment process, the reason is that after production accidents occur in factories, organic waste water with high concentration and large pH value fluctuation can be discharged in a short time, if the waste water directly enters a sewage treatment system, high impact load can be brought to the running biological treatment system, and the caused influence needs to be recovered for a long time, sometimes causing fatal damage, untreated wastewater is collected and led out through the accident pool 3, gas on the upper layer of the accident pool 3 is pumped into the water distribution well 5 through the air pump, the water distribution well 5 can filter and adsorb upper layer waste gas to improve the treatment efficiency of odor,
the heavy pollution module is connected with a sewage tank 6 through a pipeline, the sewage tank 6 carries out sedimentation treatment on the derived sewage and waste gas, the sewage and the waste gas are separated after the sedimentation treatment of the sewage tank 6, the gas is led into a reaction tank by an air pump, the reaction tank comprises a first reaction tank 9-1, a second reaction tank 9-2 and a third reaction tank 9-3, treatment liquid is respectively arranged in the first reaction tank 9-1, the second reaction tank 9-2 and the third reaction tank 9-3, odor is led into the first reaction tank 9-1, the second reaction tank 9-2 and the third reaction tank 9-3 for deodorization operation, the gas is shunted and then is treated in parallel through three groups of structures, and the purification efficiency is improved,
liquid and sludge at the bottom are led into a sludge tank 7 through a sewage tank 6 for separation treatment, the treatment efficiency is improved, a spiral conveyor is arranged at the rear end of the sludge tank 7 and is provided with a first spiral conveyor 8-1, a second spiral conveyor 8-2, a third spiral conveyor 8-3 and a fourth spiral conveyor 8-4, the spiral conveyor can horizontally, obliquely or vertically convey and has the advantages of simple structure, small cross section area, good sealing performance and the like, the sludge is conveyed into a sludge hopper 10 through the first spiral conveyor 8-1, the second spiral conveyor 8-2, the third spiral conveyor 8-3 and the fourth spiral conveyor 8-4, and a plurality of groups of sludge with different particle sizes are conveyed into the sludge hopper 10 through the first spiral conveyor 8-1, the second spiral conveyor 8-2, the third spiral conveyor 8-3 and the fourth spiral conveyor 8-4 Mud transports, the screw conveyer rear end is provided with sludge bucket 10, comes to insolate mud through sludge bucket 10, the subsequent stoving operation of being convenient for, sludge bucket 10 will insolate the mud of storage and transport first hydroextractor 11-1 and second hydroextractor 11-2 in, carry out wind-force and electric heat through first hydroextractor 11-1 and second hydroextractor 11-2 and dry, through sludge bucket 10's preliminary treatment, reduce the consumption of follow-up dewatering equipment energy, carry the mud of bottom to dry after filtering in sludge bucket 10 through screw conveyer, be rich in a large amount of organic matters in the mud, can be used as fertilizer after the follow-up treatment, promote the environment-friendly.
The foregoing shows and describes the general principles and broad features of the present invention and advantages thereof. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the utility model as claimed. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (6)
1. An odor collection system, characterized by: comprises two sets of odor discharge systems, the two sets of odor discharge systems are provided with mechanical pumps, the mechanical pumps are connected with a flow divider (12) through pipelines, the flow divider (12) is connected with two sets of branch pipes which are respectively connected with a light pollution module and a heavy pollution module,
the light pollution module is connected with a primary sedimentation tank (4) through a pipeline, supernatant liquor at the rear end of the primary sedimentation tank (4) is led out to the comprehensive adjusting tank (2) through a water pump,
the heavy pollution module is connected with a sewage tank (6) through a pipeline, the sewage tank (6) carries out sedimentation treatment on the derived sewage and waste gas, the sewage and the waste gas are separated after the sedimentation treatment of the sewage tank (6), the gas is led into a reaction tank by a gas pump, the reaction tank comprises a first reaction tank (9-1), a second reaction tank (9-2) and a third reaction tank (9-3), and treatment liquid is arranged inside the first reaction tank (9-1), the second reaction tank (9-2) and the third reaction tank (9-3).
2. The odor gas collection system according to claim 1, wherein: the sewage pool (6) guides liquid and sludge at the bottom into the sludge pool (7), the rear end of the sludge pool (7) is provided with a spiral conveyor, and the spiral conveyor is provided with a first spiral conveyor (8-1), a second spiral conveyor (8-2), a third spiral conveyor (8-3) and a fourth spiral conveyor (8-4).
3. The odor gas collection system according to claim 2, wherein: the rear end of the spiral conveyor is provided with a sludge bucket (10), and the sludge bucket (10) conveys the sludge subjected to solarization storage to the first dewatering machine (11-1) and the second dewatering machine (11-2).
4. The odor gas collection system according to claim 1, wherein: the comprehensive adjusting tank (2) is connected with an accident tank (3) through a pipeline.
5. The odor gas collection system according to claim 4, wherein: and the gas on the upper layer of the accident pool (3) is pumped out to the water distribution well (5) through the gas pump.
6. The odor gas collection system according to claim 1, wherein: the pump comprises a first pump (1-1) and a second pump (1-2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122249783.5U CN215693130U (en) | 2021-09-16 | 2021-09-16 | Odor collecting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122249783.5U CN215693130U (en) | 2021-09-16 | 2021-09-16 | Odor collecting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215693130U true CN215693130U (en) | 2022-02-01 |
Family
ID=80021308
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122249783.5U Expired - Fee Related CN215693130U (en) | 2021-09-16 | 2021-09-16 | Odor collecting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215693130U (en) |
-
2021
- 2021-09-16 CN CN202122249783.5U patent/CN215693130U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220201 |