CN203692218U - Factory aquaculture device - Google Patents
Factory aquaculture device Download PDFInfo
- Publication number
- CN203692218U CN203692218U CN201420033391.2U CN201420033391U CN203692218U CN 203692218 U CN203692218 U CN 203692218U CN 201420033391 U CN201420033391 U CN 201420033391U CN 203692218 U CN203692218 U CN 203692218U
- Authority
- CN
- China
- Prior art keywords
- tank
- cultivation
- aeration
- milipore filter
- groove
- 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 - Lifetime
Links
- 238000009360 aquaculture Methods 0.000 title claims abstract description 47
- 244000144974 aquaculture Species 0.000 title claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000005273 aeration Methods 0.000 claims abstract description 44
- 238000003475 lamination Methods 0.000 claims abstract description 16
- 239000005416 organic matter Substances 0.000 claims abstract description 9
- 241000894006 Bacteria Species 0.000 claims abstract description 6
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 claims abstract description 5
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 238000004659 sterilization and disinfection Methods 0.000 claims description 19
- 238000009395 breeding Methods 0.000 claims description 13
- 230000001488 breeding effect Effects 0.000 claims description 13
- 238000010926 purge Methods 0.000 claims description 8
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 4
- 230000015556 catabolic process Effects 0.000 claims description 3
- 238000006731 degradation reaction Methods 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 2
- 238000000108 ultra-filtration Methods 0.000 abstract description 8
- 238000003911 water pollution Methods 0.000 abstract description 3
- 239000010865 sewage Substances 0.000 abstract description 2
- 239000012528 membrane Substances 0.000 abstract 6
- 238000011084 recovery Methods 0.000 abstract 3
- 238000011001 backwashing Methods 0.000 abstract 2
- 238000005406 washing Methods 0.000 abstract 2
- 230000001580 bacterial effect Effects 0.000 abstract 1
- 238000006065 biodegradation reaction Methods 0.000 abstract 1
- 230000000249 desinfective effect Effects 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 230000000737 periodic effect Effects 0.000 abstract 1
- 230000005484 gravity Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Landscapes
- Farming Of Fish And Shellfish (AREA)
Abstract
A factory aquaculture device comprises a cultivation aeration tank, a cultivation tank, a bio-aeration tank, an ultrafiltration membrane tank, an organic matter recovery tank, a cultivation water recovery disinfecting tank, a backwashing tank, an ultraviolet sterilizer, a lamination serial type ultrafiltration membrane, an air washing system, a backwashing lifting pump and a reusing lifting pump. Liquid in the cultivation aeration tank and liquid in the cultivation tank are smoothly communicated. Water in the cultivation tank overflows to the bio-aeration tank. Solid-state embedding bacteria are placed in the bio-aeration tank, and the content of ammonia nitrogen and nitrite in cultivation water is lowered through blast aeration. After cultivation water in the bio-aeration tank is subjected to biodegradation, the cultivation water overflows to the ultrafiltration membrane tank. The lamination serial type ultrafiltration membrane and the air washing system are arranged in the ultrafiltration membrane tank. The organic matter recovery tank is arranged below the ultrafiltration membrane tank. According to the technical scheme, factory cultivation can be achieved, risks such as typhoon, water pollution and bacterial pollution are lowered, cultivation water periodic replacement is of no need, sewage discharging is avoided, and economic benefit is improved.
Description
Technical field
The utility model relates to aquaculture field, relates in particular to a kind of industrialized aquiculture device.
Background technology
It is very large that seawater aquaculture is affected by typhoon, water pollution, nuclear pollution etc., has a big risk, and cultivation density is low, and the production cycle is long.
Summary of the invention
For the deficiencies in the prior art, the utility model provides a kind of industrialized aquiculture device.
The utility model is achieved through the following technical solutions:
Industrialized aquiculture device, comprises that cultivation aeration tank, breeding trough, bio-aeration groove, milipore filter groove, organic matter accumulator tank, aquaculture water reclaim disinfection trough, anti-wash tank, ultraviolet ray disinfector, lamination string data milipore filter, air purge system, backwash elevator pump and reuse elevator pump; Described cultivation aeration tank communicates with the liquid smoothness in breeding trough; Water in described breeding trough overflows to bio-aeration groove, is placed with solid-state embedding bacterium blast aeration and reduces the content of ammonia nitrogen and nitrite in aquaculture water in bio-aeration groove; Aquaculture water in described bio-aeration groove, after biological degradation, overflows to milipore filter groove; In described milipore filter groove, be provided with lamination string data milipore filter and air purge system, milipore filter groove is divided into organic matter accumulator tank; Lamination string data milipore filter in described milipore filter groove connects aquaculture water by pipeline and reclaims disinfection trough; Described backwash elevator pump reclaims in disinfection trough and extracts aquaculture water and be transported to anti-wash tank from aquaculture water, and anti-wash tank is communicated with lamination string data milipore filter by pipeline; The aquaculture water that described reuse elevator pump reclaims aquaculture water in disinfection trough by pipeline is transported to cultivation aeration tank; Described ultraviolet sterilizer is arranged on the pipeline between reuse elevator pump and cultivation aeration tank.
Further, in described milipore filter groove, be connected with ozone.
Further, described aquaculture water reclaims disinfection trough lower than milipore filter groove, and anti-wash tank is higher than milipore filter groove.
Adopt after technique scheme, the beneficial effects of the utility model are: 1, industrial aquaculture, reduces typhoon, water pollution and germ contamination equivalent risk; 2, do not need to regularly replace aquaculture water, without sewage discharge; 3, increase economic efficiency.
Brief description of the drawings
Fig. 1 is the utility model structural scheme of mechanism;
In figure: 1, aeration valve, 2, air purge valve, 3, ultraviolet sterilizer, 4, anti-wash tank, 5, backwash valve, 6, strainer valve, 7, lamination string data milipore filter, 8, air purge pipe, 9, milipore filter groove, 10, backwash elevator pump, 11, reuse elevator pump, 12, aquaculture water reclaims disinfection trough, 13, organic matter accumulator tank, 14, bio-aeration groove, 15, breeding trough, 16, cultivation aeration tank, 17, mud valve.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
embodiment: industrialized aquiculture device, as shown in the figure, comprise that cultivation aeration tank 16, breeding trough 15, bio-aeration groove 14, milipore filter groove 9, organic matter accumulator tank 13, aquaculture water reclaim disinfection trough 12, anti-wash tank 4, ultraviolet ray disinfector 3, lamination string data milipore filter 7, air purge system 2, backwash elevator pump 10 and reuse elevator pump 11; Described cultivation aeration tank 16 communicates with the liquid smoothness in breeding trough 15.Cultivation aeration tank 16 can be designed to same groove with breeding trough 15, middlely separates with net, and a side is used for aeration as cultivation aeration tank 16, and opposite side is used for cultivation, and relatively flowing of such two trough inner waters is freer, aeration better effects if.After water in described breeding trough 15 overflows to bio-aeration groove 14(cultivation a period of time, aquaculture water is no longer fresh, overflow to bio-aeration groove 14 by overflow mechanism), in bio-aeration groove 14, be placed with solid-state embedding bacterium blast aeration and reduce the content of ammonia nitrogen and nitrite in aquaculture water.Aquaculture water in described bio-aeration groove 14, after biological degradation, overflows to milipore filter groove 9 by overflow mechanism; In described milipore filter groove 9, be provided with lamination string data milipore filter 7(and in another patent, had detailed introduction) and air purge system, milipore filter groove 9 is divided into organic matter accumulator tank 13; Lamination string data milipore filter 7 in described milipore filter groove 9 connects aquaculture water by pipeline and reclaims disinfection trough 12, reclaims and sterilizes.Described backwash elevator pump 10 reclaims the interior extraction aquaculture water of disinfection trough 12 (only needing to extract a seldom part, enough backwashes) and is transported to anti-wash tank 4 from aquaculture water, and anti-wash tank 4 is communicated with lamination string data milipore filter 7 by pipeline.When the suspended particle on lamination string data milipore filter 7 is accumulated to certain time, close strainer valve 6, open backwash valve 5, purifying waste water in anti-wash tank 4 enters by backwash water pipe and is full of diaphragm under the effect of gravity, carries out backwash.The aquaculture water that described reuse elevator pump 11 reclaims aquaculture water in disinfection trough 12 by pipeline is transported to cultivation aeration tank 16, reuses.Described ultraviolet sterilizer 3 is arranged on the pipeline between reuse elevator pump 11 and cultivation aeration tank 16, carries out disinfection by ultraviolet light to being about to return the aquaculture water again utilizing.In described milipore filter groove 9, be connected with ozone, the aquaculture water in milipore filter groove 9 is carried out to ozonization.Described aquaculture water reclaims disinfection trough 12 lower than milipore filter groove 9, thereby can filter by the gravity of aquaculture water; Anti-wash tank 4, higher than milipore filter groove 9, carries out backwash by gravity.Gravity filtration, gravity backwash, saves the energy.
Whole process can be summarized as: adopt running water and sea salt after purifying to configure certain density seawater.Water in breeding trough 15 overflows to bio-tank (being bio-aeration groove 14), places solid-state embedding bacterium blast aeration and reduce ammonia nitrogen and nitrite in aquaculture water in groove.After biodegrading tank, overflow to automatic gravity and entirely filter ultra filtration filter (being milipore filter groove 9), after milipore filter groove 9 filtering microorganisms, bacterium and food-residue, fish excreta, pass through again ultra-filtration filters, ultraviolet disinfection, reenters breeding trough 15 after ozone (trace) sterilization and recycles.Above process, all can be controlled automatically and be completed by PLC.
The above is only preferred embodiments of the present utility model, and the equivalence of doing according to structure, feature and principle described in the utility model patent claim therefore all changes or modifies, and is included in the utility model patent claim.
Claims (3)
1. industrialized aquiculture device, is characterized in that: comprise that cultivation aeration tank, breeding trough, bio-aeration groove, milipore filter groove, organic matter accumulator tank, aquaculture water reclaim disinfection trough, anti-wash tank, ultraviolet ray disinfector, lamination string data milipore filter, air purge system, backwash elevator pump and reuse elevator pump; Described cultivation aeration tank communicates with the liquid smoothness in breeding trough; Water in described breeding trough overflows to bio-aeration groove, is placed with solid-state embedding bacterium blast aeration and reduces the content of ammonia nitrogen and nitrite in aquaculture water in bio-aeration groove; Aquaculture water in described bio-aeration groove, after biological degradation, overflows to milipore filter groove; In described milipore filter groove, be provided with lamination string data milipore filter and air purge system, milipore filter groove is divided into organic matter accumulator tank; Lamination string data milipore filter in described milipore filter groove connects aquaculture water by pipeline and reclaims disinfection trough; Described backwash elevator pump reclaims in disinfection trough and extracts aquaculture water and be transported to anti-wash tank from aquaculture water, and anti-wash tank is communicated with lamination string data milipore filter by pipeline; The aquaculture water that described reuse elevator pump reclaims aquaculture water in disinfection trough by pipeline is transported to cultivation aeration tank; Described ultraviolet sterilizer is arranged on the pipeline between reuse elevator pump and cultivation aeration tank.
2. industrialized aquiculture device according to claim 1, is characterized in that: in described milipore filter groove, be connected with ozone.
3. industrialized aquiculture device according to claim 1, is characterized in that: described aquaculture water reclaims disinfection trough lower than milipore filter groove, and anti-wash tank is higher than milipore filter groove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420033391.2U CN203692218U (en) | 2014-01-20 | 2014-01-20 | Factory aquaculture device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420033391.2U CN203692218U (en) | 2014-01-20 | 2014-01-20 | Factory aquaculture device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203692218U true CN203692218U (en) | 2014-07-09 |
Family
ID=51042748
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420033391.2U Expired - Lifetime CN203692218U (en) | 2014-01-20 | 2014-01-20 | Factory aquaculture device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203692218U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111153527A (en) * | 2020-01-20 | 2020-05-15 | 浙江乾仕智能科技有限公司 | Ozone water purifying device |
| CN113233604A (en) * | 2021-04-26 | 2021-08-10 | 重庆泓源渗滤取水科技有限公司 | Infiltration water intaking system |
-
2014
- 2014-01-20 CN CN201420033391.2U patent/CN203692218U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111153527A (en) * | 2020-01-20 | 2020-05-15 | 浙江乾仕智能科技有限公司 | Ozone water purifying device |
| CN113233604A (en) * | 2021-04-26 | 2021-08-10 | 重庆泓源渗滤取水科技有限公司 | Infiltration water intaking system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140709 |
|
| CX01 | Expiry of patent term |