CN204779602U - Directional domestication constant temperature cultivation system of biochemical pond of sewage microorganism - Google Patents
Directional domestication constant temperature cultivation system of biochemical pond of sewage microorganism Download PDFInfo
- Publication number
- CN204779602U CN204779602U CN201520476779.4U CN201520476779U CN204779602U CN 204779602 U CN204779602 U CN 204779602U CN 201520476779 U CN201520476779 U CN 201520476779U CN 204779602 U CN204779602 U CN 204779602U
- Authority
- CN
- China
- Prior art keywords
- constant temperature
- tank
- ferment
- nutrition
- heating
- 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.)
- Active
Links
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a directional domestication constant temperature cultivation system of biochemical pond of sewage microorganism, it is including the heating jar, the constant temperature fermentation jar body and at least one nutrition are thrown and are added the jar, the heating jar is through hot water circulating pump and heat -exchange cycle coil pipe and constant temperature fermentation jar bodily form one -tenth constant temperature unit, nutrition is thrown and is thrown the cultivation unit with pump and the directional domestication microorganism of constant temperature fermentation jar bodily form one -tenth with the jar through nutrition, the constant temperature fermentation jar body is through pipeline and raw water intake pump intercommunication, the constant temperature fermentation jar body communicates with biochemical pond after straining the fungus pump, the speed reduction mixer is installed to the upper end of the constant temperature fermentation jar body, the constant temperature fermentation jar body parts with the heating jar, carry out heat exchange through the heat -exchange cycle coil pipe, the temperature of accurate control constant temperature fermentation jar more, the constant temperature fermentation jar body is thrown with nutrition and is added the jar separately, can supply corresponding nutrients according to different fermentation stage of microorganism or different bacterials, and the manual operation degree of difficulty is also reduced to the while.
Description
Technical field
The utility model relates to a kind of culture device, particularly relates to a kind of wastewater biochemical pool microorganism orientation domestication constant temperature culture system.
Background technology
Along with the development of modern compound probability, a large amount of xenobiotic (Xenobiotics) enters in various trade effluent and urban comprehensive wastewater, owing to itself having structural complexity and the strange property of biology, be therefore difficult to be oxidized by the microbial decomposition in conventional biological treatment system at short notice.Biological reinforcing technology refers to and reach by adding microorganism, the nutrition with specific function every day batch a kind of processing method improving water treatment effect and make system stability in biological treatment engineering system.Can be applicable to various common sewage (comprising urban comprehensive wastewater and various industrial parks composite wastewater) Biochemical Treatment, engineering system can be made to shorten start time, improve the thermal adaptation scope of system, improve stability and the shock-resistance of system.Strengthen sludge settling again simultaneously, effectively can eliminate sludge bulking, reduce sludge quantity, improve effluent quality, improve draining water quality standard.Can be applicable to various industrial sewage Biochemical Treatment, engineering system can be made to improve specific conductivity subject range and heavy metal subject range simultaneously, significantly improve system resistant to ammonia and (comprise aniline, N-methyl-p-nitroaniline etc.), resistance to agricultural chemicals, antibiotics resistant, resistance to prussiate, the ability of the toxicants such as resistance to formaldehyde, acetone and solvent based material, significantly improve the degradation capability of system to obstinate type tensio-active agent and obstinate type dye radical and obstinate type complexing agent, thus improve stability and the shock-resistance of system.Raising COD, BOD5, TOC, ammonia nitrogen, total phosphorus that can be larger, colourity, the clearance of turbidity and some specific hard-degraded substance, water outlet be as clear as crystal.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of wastewater biochemical pool microorganism orientation domestication constant temperature culture system.
The utility model solves the technical scheme that its technical problem adopts: wastewater biochemical pool microorganism orientation domestication constant temperature culture system, it comprises heating tank, ferment at constant temperature tank body and at least one nutrition add tank, described heating tank is by hot water circulating pump and be positioned at the heat exchange circulation coil pipe of ferment at constant temperature tank body and ferment at constant temperature tank body forms constant temperature unit, described nutrition adds tank and adds by nutrition the cultivation unit that pump and ferment at constant temperature tank body form directed acclimated microorganism, described ferment at constant temperature tank body is communicated with former water intake pump by pipeline, ferment at constant temperature tank body is communicated with biochemistry pool after straining bacterium pump, the upper end of ferment at constant temperature tank body is provided with deceleration stirrer, the stirring section of described deceleration stirrer stretches into the inside of ferment at constant temperature tank body, the lower disposed of ferment at constant temperature tank interior has multiple titanium aeration head, described titanium aeration head is communicated with air compressor machine by pipeline, pipeline between titanium aeration head and air compressor machine is provided with air inlet electromagnetic valve.
Be further used as the improvement of technical solutions of the utility model, high level switch, low liquid level switch and ferment at constant temperature tank temperature sensor are installed in described ferment at constant temperature tank body.
Be further used as the improvement of technical solutions of the utility model, the working order of described former water intake pump is controlled by high level switch and low liquid level switch, and the startup of described hot water circulating pump is controlled by ferment at constant temperature tank sensor with closedown working order.
Be further used as the improvement of technical solutions of the utility model, be provided with heating rod and heating tank temperature sensor in described heating tank, heating tank is also provided with heating tank filling pipe and heating tank evacuated tube.
Be further used as the improvement of technical solutions of the utility model, the working order of described heating rod is controlled by heating tank temperature sensor.
Be further used as the improvement of technical solutions of the utility model, described nutrition adds tank upper surface and is provided with nutrition and adds tank stirrer, the stirring section that described nutrition adds tank stirrer stretches into nutrition and adds tank inside, and the upper end that described nutrition adds tank is provided with tap water and supplements pipeline.
Be further used as the improvement of technical solutions of the utility model, the outside surface of described ferment at constant temperature tank body is enclosed with ferment at constant temperature tank thermal insulation layer, and the outside surface of described heating tank is enclosed with heating tank thermal insulation layer.
Be further used as the improvement of technical solutions of the utility model, described ferment at constant temperature tank thermal insulation layer and heating tank thermal insulation layer are polyurethane insulation coating.
The beneficial effects of the utility model: the ferment at constant temperature tank body in the utility model separates with heating tank, thermal exchange is carried out by heat exchange circulation coil pipe, more precisely can control the temperature of ferment at constant temperature tank and can effectively avoid the heating rod direct heating fermented liq in heating tank to make the microorganism of local dead by high temperature, also increasing the work-ing life of heating rod simultaneously; Ferment at constant temperature tank body and nutrition add tank and separate, and can supplement corresponding nutritive substance according to microorganism different fermentations stage or different bacterial classifications, also reduce manual operation difficulty simultaneously.Active sludge in the bacterial classification that need tame or biochemical wastewater treatment engineering, in ferment at constant temperature tank body, other nutritive substance synergy under, long-term constantly with target degradation material for primary carbon source and the energy, through the strengthening biological process such as domestication, mutagenesis, Natural Selection, the biochemistry pool after cultivating breeding batch or continuously in input biochemical wastewater treatment system.The utility model is applicable in the domestication of biochemical wastewater treatment system microorganism orientation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
As shown in Figure 1, wastewater biochemical pool microorganism orientation domestication constant temperature culture system, it comprises heating tank 7, ferment at constant temperature tank body 2 and at least one nutrition add tank 13, described heating tank 7 forms constant temperature unit by hot water circulating pump 11 and the heat exchange circulation coil pipe 21 that is positioned at ferment at constant temperature tank body 2 with ferment at constant temperature tank body 2, described nutrition adds tank 13 and adds by nutrition the cultivation unit that pump 15 and ferment at constant temperature tank body 2 form directed acclimated microorganism, need the bacterial classification of domestication, the adding of nutritive substance can only add tank 13 by nutrition and add and enter in ferment at constant temperature tank body 2, described ferment at constant temperature tank body 2 is communicated with former water intake pump 1 by pipeline, ferment at constant temperature tank body 2 is communicated with biochemistry pool after straining bacterium pump 12, the upper end of ferment at constant temperature tank body 2 is provided with deceleration stirrer 5, the stirring section of described deceleration stirrer 5 stretches into the inside of ferment at constant temperature tank body 2, the lower disposed of ferment at constant temperature tank body 2 inside has multiple titanium aeration head 16, described titanium aeration head 16 is communicated with air compressor machine 6 by pipeline, pipeline between titanium aeration head 16 and air compressor machine 6 is provided with air inlet electromagnetic valve 20.The time adjustable (adjustable according to the time of aerobic cultivation and Anaerobic culturel) that air compressor machine 6, deceleration stirrer 5 run, aerobic bacteria can be cultivated and also can train anerobe, also can cultivate amphimicrobe simultaneously.The wide accommodation of equipment, operability is high.Former water intake pump 1, strain bacterium pump 12, hot water circulating pump 11 and nutrition and add that pump 15 is other is all provided with manually operated control valve.Ferment at constant temperature tank body 2 lower end is provided with ferment at constant temperature tank evacuated tube, is emptied completely by the liquid in ferment at constant temperature tank body 2 by ferment at constant temperature tank evacuated tube.
Ferment at constant temperature tank body 2 separates with heating tank 7, thermal exchange is carried out by heat exchange circulation coil pipe 21, more precisely can control the temperature of ferment at constant temperature tank and can effectively avoid the heating rod 8 direct heating fermented liq in heating tank 7 to make the microorganism of local dead by high temperature, also increasing the work-ing life of heating rod 8 simultaneously; Ferment at constant temperature tank body 2 and nutrition add tank 13 and separate, and can supplement corresponding nutritive substance according to microorganism different fermentations stage or different bacterial classifications, also reduce manual operation difficulty simultaneously.Active sludge in the bacterial classification that need tame or biochemical wastewater treatment engineering, in ferment at constant temperature tank body 2, other nutritive substance synergy under, long-term constantly with target degradation material for primary carbon source and the energy, through the strengthening biological process such as domestication, mutagenesis, Natural Selection, the biochemistry pool after cultivating breeding batch or continuously in input biochemical wastewater treatment system.Compare with conventional biochemical system, just the utility model is set up to raw waste water Biochemical Treatment, its the long-term precipitation active sludge of former biochemical treatment system is constantly eliminated, inoculation, optimize domestication, constantly fresh flora kind is turned back to former biochemical system, thus stability plays to original system escort effect.
As the utility model preferred embodiment, high level switch 3, low liquid level switch 4 and ferment at constant temperature tank temperature sensor 18 are installed in described ferment at constant temperature tank body 2.
As the utility model preferred embodiment, the working order of described former water intake pump 1 is controlled by high level switch 3 and low liquid level switch 4, and the startup of described hot water circulating pump 11 is controlled by ferment at constant temperature tank temperature sensor 18 with closedown working order.When the temperature that ferment at constant temperature tank temperature sensor 18 detects is lower than set(ting)value, start hot water circulating pump 11 to heat up to the liquid in ferment at constant temperature tank body 2, when the temperature that ferment at constant temperature tank temperature sensor 18 detects is higher than set(ting)value, close hot water circulating pump 11, control the liquid fermenting temperature in ferment at constant temperature tank body 2, the full-automatic unmanned of whole process, safe and reliable.
As the utility model preferred embodiment, heating rod 8 and heating tank temperature sensor 19 are installed in described heating tank 7, heating tank 7 is also provided with heating tank filling pipe 9 and heating tank evacuated tube 10, by heating tank filling pipe 9 toward moisturizing in heating tank 7, by heating tank evacuated tube 10 by emptying for the water in heating tank 7.
As the utility model preferred embodiment, the working order of described heating rod 8 is controlled by heating tank temperature sensor 19.When the temperature that heating tank temperature sensor 19 detects is lower than set(ting)value, start heating rod 8 to the liquid warming in heating tank 7, when the temperature that heating tank temperature sensor 19 detects is higher than set(ting)value, close heating rod 8 to control the temperature of liquid in heating tank 7, the full-automatic unmanned of whole process, safe and reliable.
As the utility model preferred embodiment, described nutrition adds tank 13 upper surface and is provided with nutrition and adds tank stirrer 14, the stirring section that described nutrition adds tank stirrer 14 stretches into nutrition, and to add tank 13 inner, and the upper end that described nutrition adds tank 13 is provided with tap water and supplements pipeline 23.
As the utility model preferred embodiment, the outside surface of described ferment at constant temperature tank body 2 is enclosed with ferment at constant temperature tank thermal insulation layer 17, and the outside surface of described heating tank 7 is enclosed with heating tank thermal insulation layer 22.
As the utility model preferred embodiment, described ferment at constant temperature tank thermal insulation layer 17 and heating tank thermal insulation layer 22 are polyurethane insulation coating, adopt polyurethane insulation coating, can effectively prevent heat loss from reducing energy consumption simultaneously.
Below the process that the utility model runs:
A. deliver in ferment at constant temperature tank body 2 by sewage by former water intake pump 1, when liquid level rises to high level switch 3, former water intake pump 1 stops upper water automatically.
B. by the nutritive substance prepared and need the bacterial classification of domestication manually to increase to enter nutrition and add in tank 13, open nutrition and add tank stirrer 14, open nutrition after stirring and add pump 15 and deliver in ferment at constant temperature tank body 2.
C. air compressor machine 6 and air inlet electromagnetic valve 20 are opened, aeration 8 hours (time is adjustable) closes air compressor machine 6 and air inlet electromagnetic valve 20 afterwards, then deceleration stirrer 5 is opened, stir 8 hours (time is adjustable) and close deceleration stirrer 5 afterwards, leave standstill after 1 hour, open and strain bacterium pump 12 directed bacterial classification pump of having tamed to biochemistry pool, when liquid level is down to low liquid level switch 4 in ferment at constant temperature tank body 2, bacterium pump 12 is strained in automatic closedown, completes the cultivation of one-period bacterial classification with this.
D. after completing steps A, the constant temperature system in ferment at constant temperature tank body 2 is adjusted automatically, when the temperature that ferment at constant temperature tank temperature sensor 18 detects is lower than 30 degree (temperature is adjustable), start hot water circulating pump 11 the liquid of the hot water in heating tank 7 in heat exchange circulation coil pipe 21 post-heating ferment at constant temperature tank body 2; When the temperature that ferment at constant temperature tank temperature sensor 18 detects is higher than 40 degree (temperature is adjustable), close hot water circulating pump 11.
E. after completing steps A, the constant temperature system in heating tank 7 is adjusted automatically, when the temperature that heating tank temperature sensor 19 detects is lower than 50 degree (temperature is adjustable), start heating rod 8, when the temperature that heating tank temperature sensor 19 detects is higher than 65 degree (temperature is adjustable), close heating rod 8.
Certainly, the utility model is created and is not limited to above-mentioned embodiment, those of ordinary skill in the art also can make equivalent variations or replacement under the prerequisite without prejudice to the utility model spirit, and these equivalent modification or replacement are all included in the application's claim limited range.
Claims (8)
1. wastewater biochemical pool microorganism orientation domestication constant temperature culture system, it is characterized in that: it comprises heating tank, ferment at constant temperature tank body and at least one nutrition add tank, described heating tank is by hot water circulating pump and be positioned at the heat exchange circulation coil pipe of ferment at constant temperature tank body and ferment at constant temperature tank body forms constant temperature unit, described nutrition adds tank and adds by nutrition the cultivation unit that pump and ferment at constant temperature tank body form directed acclimated microorganism, described ferment at constant temperature tank body is communicated with former water intake pump by pipeline, ferment at constant temperature tank body is communicated with biochemistry pool after straining bacterium pump, the upper end of ferment at constant temperature tank body is provided with deceleration stirrer, the stirring section of described deceleration stirrer stretches into the inside of ferment at constant temperature tank body, the lower disposed of ferment at constant temperature tank interior has multiple titanium aeration head, described titanium aeration head is communicated with air compressor machine by pipeline, pipeline between titanium aeration head and air compressor machine is provided with air inlet electromagnetic valve.
2. wastewater biochemical pool microorganism orientation domestication constant temperature culture system according to claim 1, is characterized in that: be provided with high level switch, low liquid level switch and ferment at constant temperature tank temperature sensor in described ferment at constant temperature tank body.
3. wastewater biochemical pool microorganism orientation domestication constant temperature culture system according to claim 2, it is characterized in that: the working order of described former water intake pump is controlled by high level switch and low liquid level switch, the startup of described hot water circulating pump is controlled by ferment at constant temperature tank sensor with closedown working order.
4. wastewater biochemical pool microorganism orientation domestication constant temperature culture system according to claim 1, it is characterized in that: be provided with heating rod and heating tank temperature sensor in described heating tank, heating tank is also provided with heating tank filling pipe and heating tank evacuated tube.
5. wastewater biochemical pool microorganism orientation domestication constant temperature culture system according to claim 4, is characterized in that: the working order of described heating rod is controlled by heating tank temperature sensor.
6. wastewater biochemical pool microorganism orientation domestication constant temperature culture system according to claim 1, it is characterized in that: described nutrition adds tank upper surface and is provided with nutrition and adds tank stirrer, the stirring section that described nutrition adds tank stirrer stretches into nutrition and adds tank inside, and the upper end that described nutrition adds tank is provided with tap water and supplements pipeline.
7. wastewater biochemical pool microorganism orientation domestication constant temperature culture system according to claim 1, is characterized in that: the outside surface of described ferment at constant temperature tank body is enclosed with ferment at constant temperature tank thermal insulation layer, and the outside surface of described heating tank is enclosed with heating tank thermal insulation layer.
8. wastewater biochemical pool microorganism orientation domestication constant temperature culture system according to claim 1, is characterized in that: described ferment at constant temperature tank thermal insulation layer and heating tank thermal insulation layer are polyurethane insulation coating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520476779.4U CN204779602U (en) | 2015-06-30 | 2015-06-30 | Directional domestication constant temperature cultivation system of biochemical pond of sewage microorganism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520476779.4U CN204779602U (en) | 2015-06-30 | 2015-06-30 | Directional domestication constant temperature cultivation system of biochemical pond of sewage microorganism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204779602U true CN204779602U (en) | 2015-11-18 |
Family
ID=54519692
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520476779.4U Active CN204779602U (en) | 2015-06-30 | 2015-06-30 | Directional domestication constant temperature cultivation system of biochemical pond of sewage microorganism |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204779602U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107574117A (en) * | 2017-07-04 | 2018-01-12 | 河北地质大学 | A kind of preparation facilities and its method of penicillin resistant class amonifying bacteria microbial inoculum |
| CN108102907A (en) * | 2018-01-15 | 2018-06-01 | 淮阴师范学院 | A kind of fermentation jar temperature measure and control device |
| CN108441419A (en) * | 2018-02-11 | 2018-08-24 | 中国电建集团华东勘测设计研究院有限公司 | Small-sized targeting strain intelligence culture apparatus and method |
-
2015
- 2015-06-30 CN CN201520476779.4U patent/CN204779602U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107574117A (en) * | 2017-07-04 | 2018-01-12 | 河北地质大学 | A kind of preparation facilities and its method of penicillin resistant class amonifying bacteria microbial inoculum |
| CN108102907A (en) * | 2018-01-15 | 2018-06-01 | 淮阴师范学院 | A kind of fermentation jar temperature measure and control device |
| CN108441419A (en) * | 2018-02-11 | 2018-08-24 | 中国电建集团华东勘测设计研究院有限公司 | Small-sized targeting strain intelligence culture apparatus and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108249574A (en) | It is a kind of to handle pig farm breeding wastewater using microalgae and produce the device and its technique of algae powder | |
| CN204779602U (en) | Directional domestication constant temperature cultivation system of biochemical pond of sewage microorganism | |
| CN112520945B (en) | Coal gasification wastewater biological strengthening treatment method and device | |
| CN106365300A (en) | Self-self-purification type breeding device and self-purification method thereof | |
| CN109055285A (en) | A kind of enrichment method of Autotrophic nitrification bacterial consortium | |
| CN102079568B (en) | Online automatic microorganism dosing system | |
| CN108358323A (en) | A kind of purifying water micrcxDrganism automatic vaccination corollary apparatus and its method | |
| CN103420545A (en) | Sludge digestion method based on microorganism compound enzyme | |
| CN105948243B (en) | A kind of fast culture is suitable for the method for the anaerobic grain sludge of pharmacy wastewater treatment | |
| CN100395326C (en) | Microbial culture system and microbial culture method using same | |
| CN109022271A (en) | A kind of nitrifier of multistage amplification automatically spreads cultivation device and propagation method online | |
| CN212504905U (en) | Full-automatic low-temperature and high-altitude microorganism culture and domestication equipment | |
| CN107653197A (en) | A kind of preparation method of microorganism formulation and its application in leather waste water processing | |
| JP2000084587A (en) | Automatic culturing type sewage cleaning device | |
| CN204454730U (en) | A kind of biologically-intensifying device | |
| CN203807476U (en) | Fermentation tank | |
| CN103755013B (en) | Cultivate the novel method of acclimated activated sludge a kind of winter | |
| CN107720957A (en) | Constant-temperatureanaerobic anaerobic processing high concentrated organic wastewater and the reaction unit and processing method of solid waste in batch-type | |
| CN209367935U (en) | Adaptive intelligent ACMBR reactor | |
| CN208361995U (en) | A kind of purifying water micrcxDrganism automatic vaccination corollary apparatus | |
| CN205011480U (en) | Active fungus crowd's of sewage treatment equipment is trained and saved | |
| CN201793431U (en) | Biological on-line automatic feeding system | |
| CN105753247B (en) | A kind of penicillin composite waste low-temperature treatment plant and its method | |
| CN207891336U (en) | The integrated processing system of high concentrated organic wastewater and solid waste | |
| CN201793424U (en) | Printing and dyeing wastewater anaerobic treatment bacterium cultivation and inoculation device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |