CN206188486U - Waste mash processing system - Google Patents
Waste mash processing system Download PDFInfo
- Publication number
- CN206188486U CN206188486U CN201620957889.7U CN201620957889U CN206188486U CN 206188486 U CN206188486 U CN 206188486U CN 201620957889 U CN201620957889 U CN 201620957889U CN 206188486 U CN206188486 U CN 206188486U
- Authority
- CN
- China
- Prior art keywords
- aeration
- gas
- tank
- absorption tower
- processing system
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002699 waste material Substances 0.000 title abstract description 4
- 238000005273 aeration Methods 0.000 claims abstract description 31
- 238000000855 fermentation Methods 0.000 claims abstract description 24
- 230000004151 fermentation Effects 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 21
- 238000010521 absorption reaction Methods 0.000 claims abstract description 12
- 239000006228 supernatant Substances 0.000 claims abstract description 8
- 238000001514 detection method Methods 0.000 claims abstract description 5
- 239000002912 waste gas Substances 0.000 claims abstract description 4
- 125000003158 alcohol group Chemical group 0.000 claims description 14
- 239000010802 sludge Substances 0.000 claims description 14
- 241001148471 unidentified anaerobic bacterium Species 0.000 claims description 8
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000003337 fertilizer Substances 0.000 claims description 3
- 241000235342 Saccharomycetes Species 0.000 claims description 2
- 238000011081 inoculation Methods 0.000 claims description 2
- 235000014655 lactic acid Nutrition 0.000 claims description 2
- 239000004310 lactic acid Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 3
- 238000005457 optimization Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 230000000505 pernicious effect Effects 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 230000005059 dormancy Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a waste mash processing system, including useless wine with dregs fermentation cylinder, aeration tank, mud jar, gas collecting device, absorption tower, detection device etc, useless wine with dregs fermentation cylinder internally mounted has the aeration pipe, useless wine with dregs fermentation cylinder upper end is equipped with the supernatant overfall, and through the pipe connection aeration tank, the lower extreme is equipped with the mud mouth, with mud jar intercommunication, the aeration tank is a plurality of, through gas collector collects the aeration and produces waste gas, gas collector and absorption tower intercommunication, even there is the detector on the absorption tower. Compared with the prior art, this system innovation nature utilize the aeration pipe to fermentation intervention of anaerobe in the anaerobic fermentation pond, better realization solid -liquid separation, realize closedization to the aeration tank, guarantee that the aeration produces gas and does not leak, introduce the detector and detect the gas after handling, realize waste mash's innocent treatment.
Description
Technical field
The utility model is related to the processing method of factory's " three wastes ", is specifically exactly a kind of alcohol residue processing system.
Background technology
The pollution of alcohol industry is the most serious with the pollution of water, and the useless mash in production process is high concentration, high suspended matter
Organic wastewater, COD contents are high, it is impossible to directly discharge.Anaerobic Digestion alcohol residue is put into practice by 30 years of researches,
A kind of processing method of practicable efficient production capacity is proved, obtains generally recognizing and applying both at home and abroad.With recent people
To the pay attention to day by day of exhaust-gas treatment, treatment is carried out to the waste gas that alcohol residue sewage disposal is produced and has begun to implement.This practicality
The experience of alcohol residue processing system, is innovated on this basis before new summary, obtains a set of effective place
Reason system.
The content of the invention
The purpose of this utility model is to provide a kind of alcohol residue processing system, alcohol residue is obtained comprehensive place
Reason.
The technical scheme in the invention for solving the technical problem is：
A kind of alcohol residue processing system, including useless wine with dregs fermentation tank, aeration tank, sludge tank, gas collector, absorption
Tower, detection means etc., are provided with aeration tube inside the useless wine with dregs fermentation tank, the useless wine with dregs fermentation tank upper end is provided with supernatant spilling
Mouthful, aeration tank is connected by pipeline, lower end is provided with sludge mouthful, is connected with sludge tank, and the aeration tank is multiple, by the gas
Body collector collects aeration and produces waste gas, the gas collector to be connected with absorption tower, and the absorption tower is connected with detector.
Used as optimization, the anaerobic bacteria such as inoculation yeast bacterium, lactic acid bacteria is fermented in the useless wine with dregs fermentation tank.
Used as optimization, sludge can further manufacture fertilizer in described sludge tank.
Used as optimization, the aeration tank is located in confined space.
The beneficial effects of the utility model are：Compared with prior art, the utilization aeration tube of the system innovation is to anaerobism
The fermentation of anaerobic bacteria is intervened in fermentation vat, preferably realizes separation of solid and liquid；Closure is realized to aeration tank, it is ensured that aeration is produced
Angry body does not leak, and introduces detector and the gas after treatment is detected, realizes the harmless treatment of alcohol residue.
Brief description of the drawings
Fig. 1 is the utility model general structure schematic diagram；
Wherein, 1 useless wine with dregs fermentation tank, 2 sludge tanks, 3 aeration tanks, 4 gas collectors, 5 absorption towers, 6 detectors, 7 compressors.
Specific embodiment
In embodiment as shown in Figure 1, useless mash is added in useless wine with dregs fermentation tank 1, while adding the anaerobic bacteria bacterium such as saccharomycete
Kind, the strain is fermented in useless wine with dregs fermentation tank 1, by the fermentation of anaerobic bacteria so that the COD reductions in system, fermentation
After the completion of, due to the fermentation of anaerobic bacteria, mud granule is in suspended state, is unfavorable for the separation of solid and gas, now
It is aerated in system using aeration tube in useless wine with dregs fermentation tank 1, because dissolved oxygen increases in system, anaerobic bacteria is temporarily in stopping
Dormancy state, the supernatant in useless wine with dregs fermentation tank 1 can be easily separated with solid deposits.Supernatant enters pipe by supernatant overfall
Road, and then flow into aeration tank 3.Lower floor's sludge sediment is discharged into sludge tank 2 by the useless lower end sludge mouthful of wine with dregs fermentation tank 1, passes through
Further treatment is changed into fertilizer etc..Supernatant enters in aeration tank 3, is aerated, and using the effect of aerobic bacteria, will have in sewage
Evil material is further decomposed, and is decomposed the pernicious gases such as sulfur dioxide, hydrogen sulfide, the ammonia of generation and is present in aeration tank confined air
It is interior, absorption tower 5 is entered by gas collector 4, the treatment such as washed, absorbed to pernicious gas therein, treatment is completed
The gas to be discharged is detected in detector 6 afterwards, is discharged after detection is qualified, detect that underproof gas can lead to
Overcompression machine 7, becomes the compressed air of aeration, and aeration tank 3 is aerated, and adjusts the parameter on absorption tower 5, is washed again
Wash, absorb, until reaching emission request.
Operation principle：
A kind of alcohol residue processing system of the present utility model utilizes intervention of the aeration tube to anaerobic bacteria, in the useless mash of realization
Solid and liquid fast hierarchical, solid and liquid are divided and rule, detector is introduced in supernatant governance process, really
Discharge gas qualified discharge is protected, it is final to realize the innoxious of useless mash.
Above-mentioned specific embodiment is only specific case of the present utility model, and scope of patent protection of the present utility model includes
But it is not limited to the product form and style of above-mentioned specific embodiment, a kind of any wine for meeting the utility model claims
Appropriate change or modification that the useless wine with dregs processing system of essence and any person of an ordinary skill in the technical field are done to it, should all fall
Enter scope of patent protection of the present utility model.
Claims (4)
1. a kind of alcohol residue processing system, it is characterised in that：Including useless wine with dregs fermentation tank, aeration tank, sludge tank, gas collection dress
Put, absorption tower, detection means, aeration tube is installed inside the useless wine with dregs fermentation tank, the useless wine with dregs fermentation tank upper end is provided with supernatant
Hydrorrhea is exported, and aeration tank is connected by pipeline, and lower end is provided with sludge mouthful, is connected with sludge tank, and the aeration tank is multiple, is passed through
The gas collector collects aeration and produces waste gas, the gas collector to be connected with absorption tower, and the absorption tower is connected with detection
Device.
2. a kind of alcohol residue processing system according to claim 1, it is characterised in that：Inoculation in the useless wine with dregs fermentation tank
Saccharomycete, lactic acid bacteria anaerobic bacteria are fermented.
3. a kind of alcohol residue processing system according to claim 1, it is characterised in that：Sludge can be with the sludge tank
Further manufacture fertilizer.
4. a kind of alcohol residue processing system according to claim 1, it is characterised in that：The aeration tank is located at confined air
It is interior.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620957889.7U CN206188486U (en) | 2016-08-29 | 2016-08-29 | Waste mash processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620957889.7U CN206188486U (en) | 2016-08-29 | 2016-08-29 | Waste mash processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206188486U true CN206188486U (en) | 2017-05-24 |
Family
ID=58728835
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620957889.7U Expired - Fee Related CN206188486U (en) | 2016-08-29 | 2016-08-29 | Waste mash processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206188486U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108529746A (en) * | 2018-03-21 | 2018-09-14 | 碧沃丰工程有限公司 | A kind of method of ammonia nitrogen and total nitrogen in removal dyeing waste water |
-
2016
- 2016-08-29 CN CN201620957889.7U patent/CN206188486U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108529746A (en) * | 2018-03-21 | 2018-09-14 | 碧沃丰工程有限公司 | A kind of method of ammonia nitrogen and total nitrogen in removal dyeing waste water |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170524 |