CN212293063U - Apramycin waste water concentration system - Google Patents
Apramycin waste water concentration system Download PDFInfo
- Publication number
- CN212293063U CN212293063U CN202020849252.2U CN202020849252U CN212293063U CN 212293063 U CN212293063 U CN 212293063U CN 202020849252 U CN202020849252 U CN 202020849252U CN 212293063 U CN212293063 U CN 212293063U
- Authority
- CN
- China
- Prior art keywords
- water
- water inlet
- stage nanofiltration
- tubular
- water tank
- 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
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides an apramycin waste water concentration system, contain a small amount of calcium carbonate in the waste water, and the protein class organic matter of higher concentration, the organic matter mainly utilizes glucose for the microbial thallus, maize meal, soybean cake powder, produced metabolite such as peptone, can deposit calcium carbonate in the liquid and detach other impurity particles through tubular ceramic microfiltration device, tubular ultrafiltration device can effectively hold back protein class macromolecule organic matter in the liquid and a small amount of in the concentrated process are appeared, feed liquid after tubular ceramic microfiltration device and tubular ultrafiltration device handle is concentrated through the two-stage nanofiltration device, realize the minimizing of the concentrated water yield of receiving and receiving the dischargeable of water of receiving and receiving.
Description
Technical Field
The utility model belongs to the technical field of special material is concentrated and water treatment, especially, relate to an apramycin waste water concentration system.
Background
At present, most of conventional wastewater can be properly treated by a water treatment technology, along with the rapid development of the water treatment technology, the application range is gradually expanded, and aiming at the wastewater which is generated in the pharmaceutical and chemical industry and contains a plurality of organic and inorganic substances and is difficult to treat, the treatment of the wastewater which cannot be solved or cannot be efficiently solved by the traditional equipment through a simple treatment system is the core for evaluating whether the wastewater has market prospect. If the wastewater is continuously precipitated or crystallized in the treatment process, the treatment difficulty is inevitably increased, the efficiency and the stability of treatment equipment are influenced, the water quality is gradually improved through mutual connection and cooperation of different equipment, the treatment obstacle is solved, and the design of a low-cost and high-efficiency treatment system superior to the traditional equipment is an urgent need in the present stage. The apramycin waste water contains higher salt and COD, and has more macromolecular protein in the waste water simultaneously, separates the concentrated processing with evaporation equipment and not only consumes time and consumes energy, and equipment area is great moreover, and inconvenient transport, needs a processing system easy and simple to handle and high-efficient urgently.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an apramycin waste water concentration system to the not enough of existence among the prior art, can realize the high-efficient concentration to waste water with few equipment combination.
To this end, the above object of the present invention is achieved by the following technical solutions:
a concentration system for apramycin production wastewater is characterized by comprising a raw water tank, a tubular ceramic microfiltration device, a concentration water tank, a tubular ultrafiltration device, a two-stage nanofiltration concentration device and a water production tank, wherein the raw water tank comprises a water inlet and a water outlet, the concentration water tank comprises a first water inlet, a second water inlet and a water outlet, the tubular ceramic microfiltration device, the tubular ultrafiltration device and the two-stage nanofiltration device respectively comprise a water inlet, a concentrated water port and a water production port, the water outlet of the raw water tank is communicated with the water inlet of the tubular ceramic microfiltration device by a pump, the concentrated water port of the tubular ceramic microfiltration device is communicated with the water inlet of the raw water tank, the water production port of the tubular ceramic microfiltration device is communicated with the first water inlet of the concentration water tank, the water outlet of the concentration water tank is communicated with the water inlet of the tubular ultrafiltration device, and the concentrated water port of the tubular, the water producing port of the tubular ultrafiltration device is communicated with the water inlet of the two-stage nanofiltration device by a pump, the concentrated water port of the two-stage nanofiltration device is communicated with the second water inlet of the concentrated water tank, and the water producing port of the two-stage nanofiltration device is communicated with the water inlet of the water producing tank.
When adopting above-mentioned technical scheme, the utility model discloses can also adopt or make up and adopt following further technical scheme:
preferably, the top of the raw water tank is provided with an opening and a top cover, and a water inlet and a water outlet of the raw water tank are both arranged on the side wall of the bottom of the water tank; the top of the concentrated water tank is provided with an opening and a top cover, the first water inlet and the water outlet are arranged on the side wall of the bottom of the water tank, and the second water inlet is arranged on the top cover.
Preferably, the tubular ceramic microfiltration device consists of a ceramic membrane element and a membrane shell, the raw water tank is communicated with the tubular ceramic microfiltration device through a pump, the pump is one of centrifugal pumps, and the aperture of the ceramic microfiltration membrane element is 30-60 nm.
Preferably, the tubular ultrafiltration device consists of a tubular ultrafiltration membrane element and a membrane shell, and the molecular weight cut-off of the membrane element is 1000-5000 Da.
Preferably, the two-stage nanofiltration device comprises a booster pump, two rolled nanofiltration membrane components and a central control system, the rolled nanofiltration membrane components comprise rolled nanofiltration membrane component and membrane shell, the front end of the booster pump is arranged behind the water inlet of the two-stage nanofiltration device, the rear end of the booster pump is communicated with the water inlet end of the first-stage nanofiltration membrane component, the water outlet end of the first-stage nanofiltration membrane component is communicated with the water inlet end of the second-stage nanofiltration membrane component, the water outlet end of the second-stage nanofiltration membrane component is the water outlet of the two-stage nanofiltration device, and the concentrated water ends of the first-stage nanofiltration membrane component and the second-stage nanofiltration membrane component.
Preferably, the concentrated water ends of the first-stage nanofiltration membrane component and the second-stage nanofiltration membrane component are connected with concentrated water ports of the two-stage nanofiltration device through tee joints.
Preferably, the concentrated water ports of the tubular ceramic microfiltration device, the tubular ultrafiltration device and the two-stage nanofiltration device are communicated with the water inlet at the bottom of the raw water tank through a tee joint.
Preferably, the devices are connected with each other and the inside of the devices by using UPVC or stainless steel pipelines, and all the joints are sealed by adopting threads.
The utility model provides an apramycin waste water concentration system, contain a small amount of calcium carbonate in the waste water, and the protein class organic matter of higher concentration, the organic matter mainly utilizes glucose for the microbial thallus, maize meal, soybean cake powder, produced metabolite such as peptone, can deposit calcium carbonate in the liquid and detach other impurity particles through tubular ceramic microfiltration device, tubular ultrafiltration device can effectively hold back protein class macromolecule organic matter in the liquid and a small amount of in the concentrated process are appeared, feed liquid after tubular ceramic microfiltration device and tubular ultrafiltration device handle is concentrated through the two-stage nanofiltration device, realize the minimizing of the concentrated water yield of receiving and receiving the dischargeable of water of receiving and receiving.
Drawings
FIG. 1 is a connection relationship and a construction diagram of an apramycin production wastewater concentration system provided by the present invention;
Detailed Description
The invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
The apramycin production wastewater concentration system comprises a raw water tank 1, a tubular ceramic microfiltration device 2, a concentration water tank 3, a tubular ultrafiltration device 4, a two-stage nanofiltration concentration device 5 and a production water tank 6, wherein a buckle-press type top cover 11 is arranged at the top of the raw water tank 1, so that feed liquid can be conveniently and rapidly added, pollutants can be prevented from entering the raw water tank in the operation process, and a water outlet 12 at the bottom of the raw water tank is connected with a water inlet 21 of the tubular ceramic microfiltration device through an UPVC pipe and a self-priming centrifugal pump 7; a concentrated water port 22 of the tubular ceramic microfiltration device 2 is connected with a water inlet 13 at the bottom of the raw water tank by an UPVC pipe, a produced water port 23 is connected with a first water inlet 32 of the concentrated water tank 3 by an UPVC pipe, a top cover 31 is arranged at the top of the concentrated water tank 3, feed liquid enters the tubular ceramic microfiltration device 2, after impurity filtration, concentrated water flows back to the raw water tank 1 for circulation, and produced water enters the concentrated water tank 3; the water outlet 33 of the concentrated water tank 3 is connected with the water inlet 41 of the tubular ultrafiltration device 4 through an UPVC pipe, the concentrated water outlet 42 of the tubular ultrafiltration device 4 is connected with the water inlet 13 of the raw water tank through an UPVC pipe and a three-way joint, the water production port 43 of the tubular ultrafiltration device 4 is connected with the water inlet 51 of the two-stage nanofiltration device 5 through an UPVC pipe, a booster pump 8 is arranged between the water inlet of the two-stage nanofiltration device and the water inlet 52 of the first-stage nanofiltration membrane component, the booster pump pumps the wastewater into the first-stage nanofiltration membrane component, the produced water after the wastewater is treated by the first-stage nanofiltration membrane component enters the second-stage nanofiltration membrane component, the booster pump 8 is connected with the water inlet 52 of the first-stage nanofiltration membrane component through a stainless steel pipe, the internal components of the two-stage nanofiltration device 5 are connected through stainless steel pipes, the concentrated water end 53 of, the water production end 55 of the second-stage nanofiltration membrane component is connected with the water production port 56 of the two-stage nanofiltration membrane device 5 through a UPVC pipe, the concentrated water port 54 of the two-stage nanofiltration membrane device is connected with the second water inlet 34 of the concentrated water tank 3 through the UPVC pipe, the concentrated water after nanofiltration of the wastewater flows back to the concentrated water tank 3 for circulation, the water production port 56 of the two-stage nanofiltration membrane device 5 is connected with the water inlet 61 of the water production tank 6 through the UPVC pipe, and the produced water enters the water production tank and is uniformly discharged.
The above detailed description is provided for explaining the present invention, and is only a preferred embodiment of the present invention, but not for limiting the present invention, and any modifications, equivalent replacements, improvements, etc. made by the present invention are within the scope of the present invention.
Claims (8)
1. A concentration system for apramycin production wastewater is characterized by comprising a raw water tank, a tubular ceramic microfiltration device, a concentration water tank, a tubular ultrafiltration device, a two-stage nanofiltration concentration device and a water production tank, wherein the raw water tank comprises a water inlet and a water outlet, the concentration water tank comprises a first water inlet, a second water inlet and a water outlet, the tubular ceramic microfiltration device, the tubular ultrafiltration device and the two-stage nanofiltration device respectively comprise a water inlet, a concentrated water port and a water production port, the water outlet of the raw water tank is communicated with the water inlet of the tubular ceramic microfiltration device by a pump, the concentrated water port of the tubular ceramic microfiltration device is communicated with the water inlet of the raw water tank, the water production port of the tubular ceramic microfiltration device is communicated with the first water inlet of the concentration water tank, the water outlet of the concentration water tank is communicated with the water inlet of the tubular ultrafiltration device, and the concentrated water port of the tubular, the water producing port of the tubular ultrafiltration device is communicated with the water inlet of the two-stage nanofiltration device by a pump, the concentrated water port of the two-stage nanofiltration device is communicated with the second water inlet of the concentrated water tank, and the water producing port of the two-stage nanofiltration device is communicated with the water inlet of the water producing tank.
2. The apramycin production wastewater concentration system of claim 1, wherein the raw water tank is provided with an opening at the top and a top cover, and the water inlet and the water outlet of the raw water tank are both arranged on the side wall of the bottom of the water tank; the top of the concentrated water tank is provided with an opening and a top cover, the first water inlet and the water outlet are arranged on the side wall of the bottom of the water tank, and the second water inlet is arranged on the top cover.
3. The apramycin production wastewater concentration system of claim 1, wherein the tubular ceramic microfiltration device is composed of a ceramic membrane element and a membrane shell, the raw water tank is communicated with the tubular ceramic microfiltration device through a pump, the pump is one of centrifugal pumps, and the aperture of the ceramic microfiltration membrane element is 30-60 nm.
4. The apramycin production wastewater concentration system of claim 1, wherein the tubular ultrafiltration device is composed of a tubular ultrafiltration membrane element and a membrane shell, and the molecular weight cut-off of the membrane element is 1000-5000 Da.
5. The apramycin production wastewater concentration system of claim 1, wherein the two-stage nanofiltration device comprises a booster pump, two rolled nanofiltration membrane modules and a central control system, the rolled nanofiltration membrane modules comprise rolled nanofiltration membrane elements and membrane shells, the front end of the booster pump is arranged behind the water inlet of the two-stage nanofiltration device, the rear end of the booster pump is communicated with the water inlet end of the first-stage nanofiltration membrane module, the water outlet end of the first-stage nanofiltration membrane module is communicated with the water inlet end of the second-stage nanofiltration device, the water outlet end of the second-stage nanofiltration membrane module is the water outlet of the two-stage nanofiltration device, and the water concentrate ends of the first-stage nanofiltration membrane module and the second-stage nanofiltration membrane module are both communicated with the.
6. The apramycin production wastewater concentration system of claim 5, wherein the concentrate ends of the first and second nanofiltration membrane modules are connected to the concentrate ends of the two-stage nanofiltration device by a tee joint.
7. The apramycin production wastewater concentration system of claim 1, wherein the concentrate ports of the tubular ceramic microfiltration device, the tubular ultrafiltration device and the two-stage nanofiltration device are communicated with the bottom water inlet of the raw water tank through a tee joint.
8. The apramycin process wastewater concentration system of claim 1, wherein the devices are connected with each other and the interior of the devices by UPVC or stainless steel pipelines, and all connections are threaded sealing joints.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020849252.2U CN212293063U (en) | 2020-05-21 | 2020-05-21 | Apramycin waste water concentration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020849252.2U CN212293063U (en) | 2020-05-21 | 2020-05-21 | Apramycin waste water concentration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212293063U true CN212293063U (en) | 2021-01-05 |
Family
ID=73968931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020849252.2U Active CN212293063U (en) | 2020-05-21 | 2020-05-21 | Apramycin waste water concentration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212293063U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113443966A (en) * | 2021-06-24 | 2021-09-28 | 德兰梅勒（北京）分离技术股份有限公司 | Extraction device and extraction method of resveratrol |
-
2020
- 2020-05-21 CN CN202020849252.2U patent/CN212293063U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113443966A (en) * | 2021-06-24 | 2021-09-28 | 德兰梅勒（北京）分离技术股份有限公司 | Extraction device and extraction method of resveratrol |
| CN113443966B (en) * | 2021-06-24 | 2022-10-04 | 德兰梅勒（北京）分离技术股份有限公司 | Extraction device and extraction method of resveratrol |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN212293063U (en) | Apramycin waste water concentration system | |
| US20090120862A1 (en) | Method of ecological restoration of water bodies containing excess nutrient | |
| CN109092065A (en) | A kind of device and method of systemic circulation reverse osmosis process abjection low molecular weight alcohols | |
| KR101453497B1 (en) | Rotary Type Energy Recovery Device | |
| CN117016475A (en) | Multistage circulating water culture system | |
| CN217264876U (en) | Enrichment system of lithium in salt lake brine | |
| CN202465408U (en) | System for concentrating and recycling residual polyethyleneglycol in condensation waste water | |
| CN103382074B (en) | Treatment system and process for removing wastewater COD of multistage domesticated yeast | |
| CN207102346U (en) | A kind of reverse osmosis type sewage-treatment plant | |
| CN115159739A (en) | Reverse osmosis seawater desalination system | |
| CN105776673B (en) | A kind of micro-polluted water treatment equipment and the method using its processing water | |
| CN214457022U (en) | Internal pressure type ultrafiltration membrane distribution backwashing device | |
| CN201678490U (en) | Condensation and recycling device for copolymerization resin waste water | |
| CN214973085U (en) | Membrane concentration polyol system | |
| CN210560185U (en) | Device for purifying and recovering protein peptide by membrane method | |
| CN209010331U (en) | A kind of sludge drying Wastewater zero-discharge treatment system | |
| CN204017671U (en) | The high power enrichment facility of high efficiency low energy consumption | |
| CN206692381U (en) | Water treatment system and cooling water recirculation system | |
| CN206418058U (en) | A kind of system that valine is extracted from zymotic fluid | |
| CN106044950B (en) | A kind of positive osmosis treatment system and its processing method of saline-alkali water | |
| CN106286903B (en) | Integral type multi-pass ball valve | |
| CN111018272A (en) | Integrated treatment system and treatment process for erythromycin thiocyanate production wastewater | |
| CN104096480B (en) | The high power enrichment facility of high efficiency low energy consumption and the method for feed liquid process thereof | |
| CN205635230U (en) | Energy -efficient salt effluent disposal system that contains | |
| CN220502859U (en) | Concentrated solution full-quantity treatment device for landfill leachate treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Room 249, 2nd floor, building 2, Huaye hi tech Industrial Park, 1180 Bin'an Road, Binjiang District, Hangzhou City, Zhejiang Province, 310052 Patentee after: Zhejiang Dixiao Technology Co.,Ltd. Address before: Room 249, 2nd floor, building 2, Huaye hi tech Industrial Park, 1180 Bin'an Road, Binjiang District, Hangzhou City, Zhejiang Province, 310052 Patentee before: ZHEJIANG DIXIAO ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |