CN201031167Y - Microorganism reactor - Google Patents
Microorganism reactor Download PDFInfo
- Publication number
- CN201031167Y CN201031167Y CNU2006201490992U CN200620149099U CN201031167Y CN 201031167 Y CN201031167 Y CN 201031167Y CN U2006201490992 U CNU2006201490992 U CN U2006201490992U CN 200620149099 U CN200620149099 U CN 200620149099U CN 201031167 Y CN201031167 Y CN 201031167Y
- Authority
- CN
- China
- Prior art keywords
- retort
- pipe
- microorganisms
- microorganism
- utility
- 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
- 244000005700 microbiome Species 0.000 title claims abstract description 37
- 238000010438 heat treatment Methods 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 8
- 239000000126 substance Substances 0.000 claims description 8
- 238000012258 culturing Methods 0.000 abstract description 10
- 230000000813 microbial effect Effects 0.000 abstract description 6
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000009395 breeding Methods 0.000 abstract description 4
- 230000001488 breeding effect Effects 0.000 abstract description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 2
- 235000015097 nutrients Nutrition 0.000 abstract description 2
- 239000001301 oxygen Substances 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 abstract description 2
- 230000004913 activation Effects 0.000 abstract 1
- 230000001737 promoting effect Effects 0.000 abstract 1
- 239000010865 sewage Substances 0.000 description 17
- 230000000694 effects Effects 0.000 description 7
- 230000015556 catabolic process Effects 0.000 description 5
- 238000006731 degradation reaction Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 239000002361 compost Substances 0.000 description 3
- 231100001261 hazardous Toxicity 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 2
- 244000005706 microflora Species 0.000 description 2
- 230000001473 noxious effect Effects 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001850 reproductive effect Effects 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
Images
Classifications
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- 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
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- 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
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model relates to a microbial reactor, and comprises a retort, an inlet pipe, and a heater box and the like. The heater box is communicated with the retort. A mixer, a level-meter, and a circulating pump are all arranged in the retort, and a circulating pipe is communicated with the inlet pipe. An emptying pipe and a discharge pipe are arranged on the lower portion of the retort, and a measuring pump is arranged on the discharge pipe. The upper portion of the retort is provided with a dosage can which is connected with the retort through a dosing pipe and a flow-meter, the above components are assembled in a tank body, and a control panel is arranged on the tank body. The utility model has the advantages that according to the characteristics of microbial breeding and growth, the microorganisms are intensively cultured and domesticated for promoting the microorganisms to quickly breed and grow through controlling the conditions of breeding and growth, and the conditions are needed by microorganisms, such as nutrient, temperature, oxygen, and PH, the activation and the quantity of microorganisms are enhanced, preferential flora is cultured, and the time of culturing and domestication is shortened. The utility model also has the advantages of saving dosage of microorganisms, reducing cost, simple utilization, and convenient operation.
Description
Technical field
The utility model relates to the equipment of environmental pollution biological treating, the microorganism reactor that the useless admittedly processing of sewage disposal specifically, water body purification and rubbish, ight soil processing and biological compost, waste gas and stink are administered.
Technical background
The biological treatment of sewage is the metabolism that utilizes microorganism, and the decomposition and inversion pollutants in sewage reaches the purpose that purifies water.Biological treatment is one of effective, the most most economical method of present sewage disposal.
The core of biological sewage treatment is to cultivate to tame out the superior microorganism flora that is fit to waste water characteristic, and maintenance and contaminated wastewater the substrate concentration microbial biomass and the activity that adapt, the superior microorganism flora is handled in best degrading activity, give full play to its degradation function, improve the biological treatment ability and the processing efficiency of system to greatest extent.
Biological sewage treatment generally adopts nature culturing sludge acclimated microorganism at present, though it is with low cost, but there is the shortcoming that is difficult to overcome, be mainly reflected in: bad adaptability, hazardous and noxious substances can suppress microbial growth even cause microorganism deactivatedly in the sewage, and most of industrial sewages especially high concentration organic sewage and high-ammonia-nitrogen sewage are difficult to handle; Culture cycle is long, especially at Sewage Plant easy inactivation of microorganism between turn(a)round, occurs sludge bulking easily, must cultivate again when sewage work moves once more; Biomass is few, and degradation capability is poor, and processing efficiency is low, and macromole, difficult degradation, poisonous and hazardous pollution substance and nitrogen, phosphorus etc. are difficult to effectively, thoroughly degrade, and goes out water unstable; To the poor processing effect of ammonia nitrogen, and when ammonia nitrogen concentration is high, can inhibition be arranged, thereby reduce processing efficiency microbic activity; Shock resistance is poor, and temperature, PH etc. are required height, operational administrative complexity; Fluctuation of service be difficult to guarantee that sewage work is normal, steady running and qualified discharge.So utilize natural activity culturing sludge acclimated microorganism that certain limitation is arranged, do not reach the optimum handling effect.
Though the method that also has some sewage works' employings to add high-effective microorganism is at present cultivated the microorganism in the domestication treatment system, adopt the direct method of spilling of throwing mostly, the microorganism consumption is big, the cost height, general enterprise is difficult to bear.
The utility model is according to the characteristics of microbial reproduction, growth, by breeding growth conditionss such as the required nutrient of controlling microbial, temperature, oxygen, PH, microorganism is carried out the hot housing domestication, promote that microorganism breeds growth fast, improve microorganism active and quantity, cultivate dominant microflora, shorten and cultivate the domestication time, save microorganism consumption and use cost, use simple, easy to operate.
The utility model both had been applicable to the domestication of sewage disposal microorganism culturing, also was applicable to the useless admittedly processing of water body purification, rubbish, ight soil processing and microorganism culturing domestications such as biological compost, waste gas and stink improvement.
Summary of the invention
The purpose of this utility model is to overcome the weak point of above-mentioned existing biological sewage treatment microorganism culturing domestication, and provides a kind of microorganism culturing efficient, quick, superior performance to tame reactor.
The purpose of this utility model can reach by following measure:
The utility model is made up of retort, water inlet pipe, heating container, heating tube, thermometer, liquid discharge pipe, volume pump, liquidometer, mixing tank, recycle pump, circulation tube, evacuated tube, dispensing canister, chemical feed pipe, under meter, control panel, casing.
The utility model heating container is communicated with retort, retort inside is provided with mixing tank, liquidometer, recycle pump, circulation tube is communicated with water inlet pipe, evacuated tube, liquid discharge pipe are established in the retort bottom, design flow pump on the liquid discharge pipe, retort top dispensing canister, dispensing canister is connected with retort by chemical feed pipe, under meter, above-mentioned parts are assembled in the casing, establish control panel on the casing.
The utility model heating container divides three grades, establishes heating tube for every grade, and the third stage is established thermometer, the water inlet down of each level, third stage upper water-out, overflow step by step.
The utility model is made up of battery main switch, timer, time display instrument, PH display instrument, temperature display meter, height displaying instrument table in control panel.
The utility model is compared with the sewage disposal microorganism culturing acclimation method of domestic present application has following advantage:
(1) the microorganism reproductive speed is fast, cultivates domestication time weak point, can go out a large amount of dominant microfloras by fast breeding;
(2) cultured microorganism adaptability is strong, and difficult degradation, macromole, hazardous and noxious substances and ammonia nitrogen are had good adaptability and degradation effect;
(3) strong shock resistance when system is impacted or restart, can start fast with recovery system and move;
(4) consumption of saving microorganism improves the microorganism utilising efficiency;
(5) can reduce input cost, have remarkable economic efficiency and social benefit;
(6) use is simple, easy to operate.
Description of drawings
Concrete structure of the present utility model is provided by the following drawings:
Fig. 1 is a structural representation of the present utility model:
(1) is retort among the figure, and (2) are water inlet pipe, and (3) are heating container, (4) be heating tube, (5) are thermometer, and (6) are liquid discharge pipe, (7) be volume pump, (8) are liquidometer, and (9) are mixing tank, (10) be recycle pump, (11) are circulation tube, and (12) are evacuated tube, (13) be dispensing canister, (14) are chemical feed pipe, and (15) are under meter, (16) be control panel, (17) are casing.
Fig. 2 is the utility model heating container structural representation figure:
(4) are heating tube among the figure, and (5) are thermometer.
Fig. 3 is the utility model control panel structural representation figure:
(18) are battery main switch among the figure, and (19) are timer, and (20) are the time display instrument, and (21) are the PH display instrument, and (22) are temperature display meter, and (23) are the height displaying instrument table.
Embodiment
Enumerate 1 embodiment below, in conjunction with the accompanying drawings, the utility model is further specified, but the utility model is not only limited to this embodiment.
The reactor of a kind of microorganism comprises the steps:
The first step: the volume, diameter and the height that calculate (1) of retort according to the microorganism culturing amount.
Second step: determine the volume and the length of heating container (3) according to the volume of retort (1), liquid is 30-60 minute in the residence time of heating container (3), and temperature is 40-50 ℃, determines the power of heating tube (4), the flow of recycle pump (10) in view of the above.
The 3rd step: determine the power of mixing tank (9) according to the volume of retort (1), the flow of volume pump (7), volume pump (7) drain time is 30-60 minute.
The 4th step: determine the volume of dispensing canister (13) according to the volume of retort (1), the volume of dispensing canister (13) is retort (a 1) volumetrical 1%; Determine the specification of under meter (15) according to the volume of dispensing canister (13).
The 5th step: according to the specification of selected device parts, the display instrument of configuration control panel (16).
The 6th step: determined parts are assembled by Fig. 1, Fig. 2, Fig. 3.
The utility model can be used for the reactor of the microorganism culturing domestication in the useless admittedly processing of sewage disposal, water body purification and rubbish, ight soil processing and biological compost, waste gas and the stink governance process.
Claims (3)
1. microorganism reactor is characterized in that it is made up of retort (1), water inlet pipe (2), heating container (3), heating tube (4), thermometer (5), liquid discharge pipe (6), volume pump (7), liquidometer (8), mixing tank (9), recycle pump (10), circulation tube (11), evacuated tube (12), dispensing canister (13), chemical feed pipe (14), under meter (15), control panel (16), casing (17); Heating container (3) is communicated with retort (1), retort (1) inside is provided with mixing tank (9), liquidometer (8), recycle pump (10), circulation tube (11) is communicated with water inlet pipe (2), evacuated tube (12), liquid discharge pipe (6) are established in the retort bottom, design flow pump (7) on the liquid discharge pipe, retort top dispensing canister (13), dispensing canister is connected with retort (1) by chemical feed pipe (14), under meter (15), above-mentioned parts are assembled in the casing (17), establish control panel (16) on the casing (17).
2. a kind of microorganism reactor according to claim 1 is characterized in that heating container (3) divides three grades, establishes heating tube (4) for every grade, and the third stage is established thermometer (5), the water inlet down of each level, third stage upper water-out, overflow step by step.
3. a kind of microorganism reactor according to claim 1 and 2 is characterized in that control panel (16) is made up of battery main switch (18), timer (19), time display instrument (20), PH display instrument (21), temperature display meter (22), height displaying instrument table (23).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201490992U CN201031167Y (en) | 2006-10-25 | 2006-10-25 | Microorganism reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201490992U CN201031167Y (en) | 2006-10-25 | 2006-10-25 | Microorganism reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201031167Y true CN201031167Y (en) | 2008-03-05 |
Family
ID=39163061
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2006201490992U Expired - Fee Related CN201031167Y (en) | 2006-10-25 | 2006-10-25 | Microorganism reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201031167Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102432109A (en) * | 2011-10-27 | 2012-05-02 | 宝钢工程技术集团有限公司 | Wastewater treatment method for microbial proliferation device |
| CN103771590A (en) * | 2014-02-24 | 2014-05-07 | 陈贤芳 | Method and device for processing sewage by virtue of multistage alternative microbial generator |
| CN110776102A (en) * | 2019-12-07 | 2020-02-11 | 生态环境部南京环境科学研究所 | Microbial community water purification system device based on Internet of things |
-
2006
- 2006-10-25 CN CNU2006201490992U patent/CN201031167Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102432109A (en) * | 2011-10-27 | 2012-05-02 | 宝钢工程技术集团有限公司 | Wastewater treatment method for microbial proliferation device |
| CN103771590A (en) * | 2014-02-24 | 2014-05-07 | 陈贤芳 | Method and device for processing sewage by virtue of multistage alternative microbial generator |
| CN110776102A (en) * | 2019-12-07 | 2020-02-11 | 生态环境部南京环境科学研究所 | Microbial community water purification system device based on Internet of things |
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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: 20080305 Termination date: 20151025 |
|
| EXPY | Termination of patent right or utility model |