CN204490585U - A kind of Microorganism incubation bed apparatus - Google Patents
A kind of Microorganism incubation bed apparatus Download PDFInfo
- Publication number
- CN204490585U CN204490585U CN201520125021.6U CN201520125021U CN204490585U CN 204490585 U CN204490585 U CN 204490585U CN 201520125021 U CN201520125021 U CN 201520125021U CN 204490585 U CN204490585 U CN 204490585U
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- China
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- tank body
- reacting tank
- bed apparatus
- circulating water
- microorganism incubation
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Abstract
The utility model relates to sewage treatment area, specifically a kind of Microorganism incubation bed apparatus, comprise reacting tank body, support and filling porous carrier therein, band microporosity separator and aeration ring are established in the bottom of described reacting tank body, and aeration ring connects ozonizer, receiver, sewage water inlet pipe and air intake duct; Reacting tank body inside is provided with the external circulating water inlet road of recirculated water spiral tube and circulating water outlet pipe road, and circulating water inlet road and circulating water outlet pipe road are outwards connected temperature controllable circulating water type well heater; The ultrasonic emitting end be connected with external ultrasound wave producer is provided with in the middle part of reacting tank body; The middle and upper part of reacting tank body is provided with COD on-Line Monitor Device, PH measuring apparatus and temperature measuring equipment; The top of described reacting tank body sets out waterpipe and gas exhaust duct.The utility model floor space is little, is convenient to maintenance, have processing efficiency high, stable, can the advantage such as purifying.
Description
Technical field
The utility model relates to a kind of sewage disposal device, specifically a kind of Microorganism incubation bed apparatus.
Background technology
Along with the development of industry, global most surface water and groundwater is all subject to pollution in various degree, and the healthy of people in serious threat.The whole world about has 1,000,000,000 tons of oil and byproduct thereof to enter by all means in underground water, surface water and soil every year according to estimates.Difficult degradation chemical substance (as benzene, toluene, phenols etc.) in oil can enter human body by food chain, can cause acute and chronic poisoning, even injured nerve system.Multiring aromatic hydrocarbon substance in oil can affect the normal function of the histoorgans such as skin, liver, kidney, even can cause skin carcinoma.
About the removal of water body PetroChina Company Limited. pollutent, what use was more at present is the method adopting artificial swamp polluted water body to be carried out to biopurification.Biological clarification utilizes microorganism in natural water and plant, artificial measures is adopted to create the environment of more favourable growth and breeding, thus can improve the organic degradation efficiency of polluted-water, the organic substance in waste water is converted into process that is more stable or mineral form material.Clean dirty ability is under field conditions (factors) very limited, especially for the degraded of specific pollutant, and raising biodegradability of must adopting an effective measure.
Summary of the invention
The purpose of this utility model is the problem that will solve for pointing out in background technology, proposes a kind of Microorganism incubation bed apparatus, and this equipment can process the petroleum pollution in water body effectively, and can improve biodegradability.
In order to solve the problems of the technologies described above, the technical scheme adopted is: a kind of Microorganism incubation bed apparatus, the porous carrier comprising reacting tank body and fill therein, this reacting tank body is supported by the support bottom it, the upper, middle and lower portion of reacting tank body side is respectively provided with thief hole, its front tank body is provided with viewing window, it is characterized in that: the bottom of described reacting tank body is provided with band microporosity separator, is provided with aeration ring between this band microporosity separator and reacting tank body lower rim; Described aeration ring connects the ozonizer and the receiver that are arranged on reacting tank body outside respectively by pipeline, this aeration ring is also respectively by the external sewage water inlet pipe of pump and air intake duct; The inside of described reacting tank body is provided with recirculated water spiral tube, the external circulating water inlet road, lower end of this recirculated water spiral tube, external circulating water outlet pipe road, its upper end; Described circulating water inlet road and circulating water outlet pipe road are outwards connected temperature controllable circulating water type well heater; The middle part of described reacting tank body is provided with the ultrasonic emitting end be connected with external ultrasound wave producer, and this ultrasonic emitting end stretches in recirculated water spiral tube; The middle and upper part of described reacting tank body is provided with COD on-Line Monitor Device, PH measuring apparatus and temperature measuring equipment; The top of described reacting tank body sets out waterpipe and gas exhaust duct, and gas exhaust duct is arranged higher than outlet conduit.
Preferred: described sewage water inlet pipe is connected in the pipeline that ozonizer is connected with aeration ring by three-way valve.
Preferred further: described three-way valve also connects a vacuum breaker.
Preferred: described COD on-Line Monitor Device is provided with COD on-line monitoring probe; Described PH measuring apparatus is provided with PH measuring sonde; Described temperature measuring equipment is provided with temperature measurement probe.
Preferred: in the pipeline that described receiver is connected with aeration ring, also to connect a storage liquid pump.
Preferred: the afterbody of described gas exhaust duct also connects a filtration unit.
Preferred: described porous carrier is polyvinyl alcohol foam filler.
Preferred: described viewing window, by 3, is separately positioned on the upper, middle and lower portion in reacting tank body front.
The beneficial effects of the utility model are: this equipment adopts Microorganism incubation technology to be fixed on by free microorganism in restriceted envelope reacting tank body, retains microorganism intrinsic activity, and can use by repetition with continuously.This equipment have processing efficiency high, stable, can the advantage such as purifying, this equipment is based on reacting tank body simultaneously, and its reaction biomass is large, good effect of separating solid from liquid, and operation cost is low, can keep efficient dominant bacteria, and can automatic monitoring system; In addition, this occupation area of equipment is little, is convenient to safeguard.
Accompanying drawing explanation
Fig. 1, structure iron of the present utility model.
Embodiment
Below in conjunction with accompanying drawing and preferred scheme, embodiment of the present utility model is described in further detail.
As shown in Figure 1, be the utility model structure iron, specifically a kind of Microorganism incubation bed apparatus, this equipment comprises an agent structure reacting tank body 1, and this reacting tank body 1 is supported by the support 2 bottom it.The upper, middle and lower portion of described reacting tank body 1 exterior lateral sides is respectively provided with a thief hole 3, and its front tank body is also provided with viewing window 4.The bottom of described reacting tank body 1 inside is provided with band microporosity separator 5, aeration ring 6 is provided with between this band microporosity separator 5 and reacting tank body 1 lower rim, described aeration ring 6 connects the ozonizer 7 and the receiver 8 that are arranged on reacting tank body 1 outside respectively by pipeline, this aeration ring 6 is also respectively by the external sewage water inlet pipe 9 of pump and air intake duct 10.In reacting tank body 1, be with the upper area of microporosity separator 5 to be filled with porous carrier 11, the recirculated water spiral tube 12 that the inside of described reacting tank body 1 is arranged stretches in described porous carrier 11, the external circulating water inlet road 13, lower end of this recirculated water spiral tube 12, external circulating water outlet pipe road 14, its upper end; Described circulating water inlet road 13 is outwards connected temperature controllable circulating water type well heater 15 with circulating water outlet pipe road 14.The middle part of described reacting tank body 1 is provided with the ultrasonic emitting end 17 be connected with external ultrasound wave producer 16, and this ultrasonic emitting end 17 stretches in recirculated water spiral tube 12.The middle and upper part of described reacting tank body 1 is provided with COD on-Line Monitor Device 18, PH measuring apparatus 19 and temperature measuring equipment 20.The top of described reacting tank body 1 sets out waterpipe 21 and gas exhaust duct 22, and gas exhaust duct 22 is arranged higher than outlet conduit 21.
Preferred scheme: the sewage water inlet pipe 9 described in the utility model can be connected in the pipeline that ozonizer 5 is connected with aeration ring 6 by three-way valve 23, a port of three-way valve 23 connects ozonizer 5 by pipeline, a port connects sewage water inlet pipe 9 by pump, connects aeration ring 6 after also having a port also can connect a vacuum breaker 24 by pipeline.
Preferred scheme is further: described COD on-Line Monitor Device 18 is provided with COD on-line monitoring probe 28; Described PH measuring apparatus 19 is provided with PH measuring sonde 29; Described temperature measuring equipment 20 is provided with temperature measurement probe 30.
Embodiment: the porous carrier 11 that this equipment is filled reacting tank body 1 inside in advance before operation carries out microbial inoculant to be fixed, and concrete steps are: first add nutrient broth liquid nutrient medium in receiver 8, and pump in reacting tank body 1; Then open ozonizer 7, by ozone, sterilising treatment is carried out to the liquid nutrient medium in reacting tank body 1; Opening temperature controllable circulating water type well heater 15 again, to control temperature in reacting tank body 1 be 25-37 DEG C; Open air intake duct 10 pairs of porous carriers 11 while receiver 8 pumps into reacting tank body 1 and inoculate being added by bacterium liquid, inoculation culture fixes complete closedown air intake duct 10; Substratum will be remained by reacting tank body 1 bottom thief hole 3 again and release reacting tank body 1; Open sewage water inlet pipe 9 again and air intake duct 10 starts to carry out sewage disposal.
Embodiment: the present embodiment is fixed in the reacting tank body 1 of filling a large amount of polyvinyl alcohol foam by oil degradation bacteria inoculation, and the afterbody of the gas exhaust duct 22 in the present embodiment is connected with filtration unit 31.
First by pump by the inorganic salt in receiver 8 and sewage suction reacting tank body 1, open air intake duct 10 makes it fully mix simultaneously, mixed contaminating fluid flows into from the bottom of reacting tank body 1, enter band microporosity separator 5 upper area, and by filler polyvinyl foam absorbing wherein; Then the microbial flora degraded inside weighting material is fixed on; After final reaction, liquid flows out from the top of reacting tank body 1.Whole sewage treatment process is by COD on-Line Monitor Device 18, pH measuring apparatus 19, temperature measuring equipment 20 is monitored in real time, and by adding the stable of inorganic salt solution or acid-alkali accommodation liquid keeping system running environment in receiver 8, after reacting tank body 1 runs certain hour, the contaminated thing of microorganism be fixed on porous carrier 11 covers and makes the decline of its degradation capability affect treatment effect, then need to use ultrasonic generator 16 pairs of reacting tank body 1 inside to clean, re-start porous carrier 11 to carry out microbial inoculant and fix, Microorganism incubation bed apparatus is made normally to keep running.Sewage is set as 0.5 hour between the stagnant stopping time in reacting tank body 1, controls temperature in this process at 25 DEG C, controls air vent amount that air intake duct 10 provided by pneumatic pump at 0.12VVM.
The present embodiment is to the petroleum hydrocarbon in water before and after treatment and BETX(benzene, toluene, ethylbenzene, dimethylbenzene) regularly (weekly twice) carry out analysiss discovery, removal rate of petroleum hydrocarbons reaches 92%, BETX clearance and reaches 96%.Test in 5 weeks is carried out, result quite stable in continuous system.
The utility model adopts Microorganism incubation technology to be fixed in restriceted envelope reacting tank body 1 by free microorganism, remains the intrinsic activity of microorganism, can use by repetition with continuously; Have processing efficiency high, stable, can the advantage such as purifying; This occupation area of equipment is little, is convenient to safeguard.
Claims (10)
1. a Microorganism incubation bed apparatus, the porous carrier (11) comprising reacting tank body (1) and fill therein, this reacting tank body is supported by the support (2) bottom it, the upper, middle and lower portion of reacting tank body side is respectively provided with thief hole (3), its front tank body is provided with viewing window (4), it is characterized in that: the bottom of described reacting tank body is provided with band microporosity separator (5), is provided with aeration ring (6) between this band microporosity separator and reacting tank body lower rim; Described aeration ring connects the ozonizer (7) and the receiver (8) that are arranged on reacting tank body outside respectively by pipeline, this aeration ring is also respectively by the external sewage water inlet pipe of pump (9) and air intake duct (10); The inside of described reacting tank body is provided with recirculated water spiral tube (12), the external circulating water inlet road (13) in lower end of this recirculated water spiral tube, the external circulating water outlet pipe road (14) in its upper end; Described circulating water inlet road and circulating water outlet pipe road are outwards connected temperature controllable circulating water type well heater (15); The middle part of described reacting tank body is provided with the ultrasonic emitting end (17) be connected with external ultrasound wave producer (16), and this ultrasonic emitting end stretches in recirculated water spiral tube; The middle and upper part of described reacting tank body is provided with COD on-Line Monitor Device (18), PH measuring apparatus (19) and temperature measuring equipment (20); The top of described reacting tank body sets out waterpipe (21) and gas exhaust duct (22), and gas exhaust duct is arranged higher than outlet conduit.
2. Microorganism incubation bed apparatus according to claim 1, is characterized in that: described sewage water inlet pipe (9) is connected in the pipeline that ozonizer (7) is connected with aeration ring (6) by three-way valve (23).
3. Microorganism incubation bed apparatus according to claim 2, is characterized in that: described three-way valve (23) also connects a vacuum breaker (24).
4. Microorganism incubation bed apparatus according to claim 1, is characterized in that: described COD on-Line Monitor Device (18) is provided with COD on-line monitoring probe (28).
5. Microorganism incubation bed apparatus according to claim 1, is characterized in that: described PH measuring apparatus (19) is provided with PH measuring sonde (29).
6. Microorganism incubation bed apparatus according to claim 1, is characterized in that: described temperature measuring equipment (20) is provided with temperature measurement probe (30).
7. Microorganism incubation bed apparatus according to claim 1, is characterized in that: also connect a storage liquid pump (32) in the pipeline that described receiver (8) is connected with aeration ring (6).
8. Microorganism incubation bed apparatus according to claim 1, is characterized in that: the afterbody of described gas exhaust duct (22) also connects a filtration unit (31).
9. Microorganism incubation bed apparatus according to claim 1, is characterized in that: described porous carrier (11) is polyvinyl alcohol foam filler.
10. Microorganism incubation bed apparatus according to claim 1, is characterized in that: described viewing window (4) is provided with three, is separately positioned in reacting tank body (1), upper and lower part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520125021.6U CN204490585U (en) | 2015-03-04 | 2015-03-04 | A kind of Microorganism incubation bed apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520125021.6U CN204490585U (en) | 2015-03-04 | 2015-03-04 | A kind of Microorganism incubation bed apparatus |
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| Publication Number | Publication Date |
|---|---|
| CN204490585U true CN204490585U (en) | 2015-07-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520125021.6U Expired - Fee Related CN204490585U (en) | 2015-03-04 | 2015-03-04 | A kind of Microorganism incubation bed apparatus |
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| Country | Link |
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| CN (1) | CN204490585U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106745974A (en) * | 2016-12-09 | 2017-05-31 | 南宁市黑晶信息技术有限公司 | A kind of chemical industry heavy metal devil liquor recovery processing equipment |
| CN107215946A (en) * | 2017-05-23 | 2017-09-29 | 江苏和顺环保有限公司 | Miniature water process ozone reaction unit |
-
2015
- 2015-03-04 CN CN201520125021.6U patent/CN204490585U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106745974A (en) * | 2016-12-09 | 2017-05-31 | 南宁市黑晶信息技术有限公司 | A kind of chemical industry heavy metal devil liquor recovery processing equipment |
| CN107215946A (en) * | 2017-05-23 | 2017-09-29 | 江苏和顺环保有限公司 | Miniature water process ozone reaction unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: CHENGDU EN-SHAIN TECHNOLOGY Inc. Assignor: JIANGSU MICROBE BIOLOGICAL ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY CO.,LTD. Contract record no.: 2016320000124 Denomination of utility model: Microbial fixed bed equipment Granted publication date: 20150722 License type: Exclusive License Record date: 20160330 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 214000 Jiangsu Province, Wuxi City Jinxi Road No. 99 Patentee after: Jiangsu Environmental Protection Technology Co.,Ltd. Maikebo Address before: 214000 Jiangsu Province, Wuxi City Jinxi Road No. 99 Patentee before: JIANGSU MICROBE BIOLOGICAL ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY CO.,LTD. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170728 Address after: 610000 Sichuan Province, Chengdu City, bay 66 Patentee after: CHENGDU EN-SHAIN TECHNOLOGY Inc. Address before: 214000 Jiangsu Province, Wuxi City Jinxi Road No. 99 Patentee before: Jiangsu Environmental Protection Technology Co.,Ltd. Maikebo |
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| 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: 20150722 |