CN2466152Y - Combined intermediate water recycle apparatus - Google Patents
Combined intermediate water recycle apparatus Download PDFInfo
- Publication number
- CN2466152Y CN2466152Y CN 01216525 CN01216525U CN2466152Y CN 2466152 Y CN2466152 Y CN 2466152Y CN 01216525 CN01216525 CN 01216525 CN 01216525 U CN01216525 U CN 01216525U CN 2466152 Y CN2466152 Y CN 2466152Y
- Authority
- CN
- China
- Prior art keywords
- strainer
- valve
- water
- reactor
- bio
- 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
Abstract
The utility model relates to a combined waste water recover device. An inlet of a multiple-way valve arranged on a bioreactor is communicated with a water inlet pump; the other four valve ports of the valve are respectively communicated with a drain cap in the bioreactor, an inlet of the bioreactor, an inlet of a multiple-way valve on a filter, and a valve port of a multiple-way valve on a drain pipe and the filter; the other three valve ports of the multiple-way valve on the filter are respectively communicated with an inlet of the filter, a drain cap in the filter, and a lower end port of a charcoal filter, and the charcoal filter is connected with a disinfecting device. The utility model has the advantages of small size, low cost, high automation, low operation cost, stable performance, and long service life.
Description
The utility model relates to a kind of sewage disposal device, water reuse apparatus in especially a kind of built-up type.
At present, the method that is used for the centering water treatment in the society can be divided into two classes substantially, and the one, biochemistry adds materilization freatment method; The 2nd, materialization ten activated carbon treatment methods.Equipment according to this two class methods manufacturing, though can realize the task of centering water treatment, but have following unsurmountable defective, the one, because the volume of equipment own is big, can only the split manufacturing, on-the-spot aggregate erection, make the installation cost height so have, floor space is big, and is unsuitable for the defective that manufacturer produces in batches; The 2nd, because this two classes treatment process technological principle is limit, its use cost is higher, and range of application is narrow, has limited and has applied; The 3rd, because automation degree of equipment is not high, the operating mass instability of its equipment is brought certain inconvenience to use, has also influenced and has applied.
Task of the present utility model is to provide that a kind of volume is little, low cost of manufacture, floor space are few, be convenient to manufacturer's batch process and installation, level of automation height, working cost is low, water reuse apparatus in the built-up type of the integrative-structure of stable performance, applied range, long service life.
Task of the present utility model is to adopt following technical scheme to realize.It comprises intake pump, the aeration turbulence pump, bio-reactor, strainer, the charcoal strainer, sterilization equipment, sterilization dispensing box and electrical control cubicles, it is characterized in that: the water outlet of intake pump is connected with the import of time controlled filter type multiway valve on being arranged on bio-reactor, other four valve ports on this a valve wherein valve port are connected with the drain cap that is arranged on the bio-reactor intracavity bottom, one valve port is connected with the import of bio-reactor, one valve port is connected and is connected with water shoot with a valve port of time controlled filter type multiway valve on being arranged on strainer, the import of the time controlled filter type multiway valve on one valve port and the strainer is connected and is connected with the water outlet of water pump, other three valve ports on the time controlled filter type multiway valve on the strainer each with the drain cap that is arranged on strainer inner chamber lower end, the import of strainer, the lower port of charcoal strainer is connected, the upper port of charcoal strainer is connected with the import of sterilization equipment, sterilization equipment is connected with thimerosal preparation case, the outlet of sterilization equipment is connected with water shoot, the water outlet of aeration turbulence pump is connected with the inner chamber lower end of bio-reactor and charcoal strainer respectively, its water-in and charcoal strainer upper end intracavity inter-connection.Intake pump described in the utility model, aeration turbulence pump, bio-reactor, strainer, charcoal strainer, sterilization equipment, sterilization dispensing box are fixed on the same base, also be provided with the electrical control cubicles that is used to control intake pump, aeration turbulence pump and time controlled filter type multiway valve on this base, adding in described bio-reactor has the charcoal granular filler.In described strainer, add quartz sand filter media is arranged.In described charcoal strainer, add carbon leaching material is arranged.Pending water enters bio-reactor after intake pump promotes, make COD, BCD, ammonia nitrogen, colourity and suspended matter in the water obtain removing, the required oxygen of microbial reaction is supplied with by the continuous oxygenation of aeration turbulence pump in the device, bio-reactor has time type and controls multiple valve one cover, this equipment is according to the time of setting, automatically just wash, when just washing, multiway valve is closed water outlet automatically, former water is directly entered in the bio-reactor by water inlet pipe and washes from top to bottom, and flush discharge is collected by drain cap and discharged automatically by water shoot.After the bio-reactor reaction, treat effluent is collected by drain cap and is entered the strainer filtration, suspended matter in the water is further removed, strainer has time type control multiway valve one cover, this equipment is according to the time of setting, automatically carry out back flushing, when the flushing of carrying out, multiway valve is closed water outlet automatically, former water is directly entered in the strainer by water inlet pipe and carries out back flushing by the drain cap water outlet, and the back flushing draining is discharged automatically by water shoot, and the water after filtering through filter is collected by drain cap and entered the charcoal strainer, further remove colourity and organic substance in the water, the charcoal strainer adopts the adverse current water intake mode, owing to adopt BAC process, can prolong the work-ing life of gac greatly, the saturated regeneration period of charcoal absorption prolongs, generally can use 3-4, water outlet enters sterilization equipment and carries out disinfection, and sterilization equipment use device pressure adds thimerosal to the treating water disinfection automatically through water sprayer, the processing qualified water enters in the tank and stores, and uses for the user.
Owing to adopted technique scheme, the utlity model has following evident characteristic: the one, because each part described in the utility model all is fixed on the same base, therefore form integrative-structure, so have compact construction, volume is little, floor space is few, be convenient to install the characteristics that are suitable for manufacturer to produce in batches; The 2nd, owing to adopt the technical scheme of electrical control cubicles control multiway valve, have the advantages that level of automation is high and be convenient to manage; The 3rd, bio-reactor has been adopted in biochemical treatment, this reactor also has the effect of sedimentation and filtration except carrying out biochemical reaction, and therefore having saved settling tank has simplified treatment scheme, so have manufacturing cost and the low characteristics of working cost; The 4th, owing to adopted the technical scheme of carrying out oxygenation with the aeration turbulence pump, so have the advantages that oxidation effect is good, oxygen transfer rate is high, power consumption is little, running cost is low; The 5th owing in bio-reactor, add the charcoal particulate vector is arranged, this carrier has the feature that microbial film easily adheres to and comes off, thus have be difficult for stopping up, treatment effect is good and the characteristics of life cycle length.
In sum, can effectively realize task of the present utility model.
Below will further describe as follows with reference to the accompanying drawings to the utility model.
Accompanying drawing has provided structural representation of the present utility model.
In the accompanying drawings, 1 be intake pump, 2 for the aeration turbulence pump, 3 for bio-reactor, 4 for strainer, 5 for biological carbon filter, 6 for sterilization equipment, 7 for thimerosal preparation case, 8 for electrical control cubicles, 9 for base, 10 and 11 for time controlled filter type multiway valve, 12 and 13 for drain cap, 14 for the charcoal granular filler, 15 for quartz sand filter media, 16 for carbon leaching material, 17 for water shoot, 18 for water inlet pipe, 19 be rising pipe.
With reference to the accompanying drawings, the water outlet of intake pump 1 is connected with the import of time controlled filter type multiway valve 10 on being arranged on bio-reactor 3, other four valve ports on this a valve wherein valve port are connected with the drain cap 13 that is arranged on bio-reactor 3 intracavity bottoms, one valve port is connected with the import of bio-reactor 3, one valve port is connected and is connected with water shoot 17 with a valve port of time controlled filter type multiway valve 11 on being arranged on strainer 4, import on the time controlled filter type multiway valve 11 on one valve port and the strainer 4, and be connected with the water outlet of water pump, three valve ports on the time controlled filter type multiway valve 11 on the strainer 4 each with the drain cap 12 that is arranged on strainer 4 inner chamber lower ends, the import of strainer 4, the lower port of charcoal strainer 5 is connected, the upper port of charcoal strainer 5 is connected with the import of sterilization equipment 6, sterilization equipment 6 is connected with thimerosal preparation case 7, the outlet of sterilization equipment 6 is connected with rising pipe 19, the water outlet of aeration turbulence pump 2 is connected with the inner chamber lower end of bio-reactor 3 and charcoal strainer 5 respectively, the upper end intracavity inter-connection of the water-in of aeration turbulence pump 2 and charcoal strainer 5.Intake pump 1, aeration turbulence pump 2, bio-reactor 3, strainer 4, charcoal strainer 5, sterilization equipment 6, sterilization dispensing box 7, electrical control cubicles 8 are fixed on the same base 9.
Claims (6)
1, water reuse apparatus in the built-up type, comprise intake pump, the aeration turbulence pump, bio-reactor, strainer, the charcoal strainer, sterilization equipment, sterilization dispensing box and electrical control cubicles, it is characterized in that: the water outlet of intake pump is connected with the import of time controlled filter type multiway valve on being arranged on bio-reactor, other four valve ports on this a valve wherein valve port are connected with the drain cap that is arranged on the bio-reactor intracavity bottom, one valve port is connected with the import of bio-reactor, one valve port is connected and is connected with water shoot with a valve port of time controlled filter type multiway valve on being arranged on strainer, the import of the time controlled filter type multiway valve on one valve port and the strainer is connected and is connected with the water outlet of water pump, other three valve ports on the time controlled filter type multiway valve on the strainer each with the drain cap that is arranged on strainer inner chamber lower end, the import of strainer, the lower port of charcoal strainer is connected, the upper port of charcoal strainer is connected with the import of sterilization equipment, sterilization equipment is connected with thimerosal preparation case, the outlet of sterilization equipment is connected with water shoot, the water outlet of aeration turbulence pump is connected with the inner chamber lower end of bio-reactor and charcoal strainer respectively, its water-in and charcoal strainer upper end intracavity inter-connection.
2, water reuse apparatus in the built-up type according to claim 1 is characterized in that: intake pump, aeration turbulence pump, bio-reactor, strainer, charcoal strainer, sterilization equipment, sterilization dispensing box are fixed on the same base.
3, water reuse apparatus in the built-up type according to claim 1 is characterized in that: also be provided with the electrical control cubicles that is used to control intake pump, aeration turbulence pump and time controlled filter type multiway valve on base.
4, water reuse apparatus in the built-up type according to claim 1 is characterized in that: adding in bio-reactor has the charcoal granular filler.
5, water reuse apparatus in the built-up type according to claim 1 is characterized in that: adding in strainer has quartz sand filter media.
6, water reuse apparatus in the built-up type according to claim 1 is characterized in that: adding in the charcoal strainer has carbon leaching material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01216525 CN2466152Y (en) | 2001-02-21 | 2001-02-21 | Combined intermediate water recycle apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01216525 CN2466152Y (en) | 2001-02-21 | 2001-02-21 | Combined intermediate water recycle apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2466152Y true CN2466152Y (en) | 2001-12-19 |
Family
ID=33634924
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01216525 Expired - Fee Related CN2466152Y (en) | 2001-02-21 | 2001-02-21 | Combined intermediate water recycle apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2466152Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1330593C (en) * | 2005-04-26 | 2007-08-08 | 迟景强 | Autocontrolling apparatus for reclaimed water treatment system |
| CN101870508B (en) * | 2009-02-06 | 2014-10-15 | 可虑康国际公司 | grey water treatment system |
-
2001
- 2001-02-21 CN CN 01216525 patent/CN2466152Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1330593C (en) * | 2005-04-26 | 2007-08-08 | 迟景强 | Autocontrolling apparatus for reclaimed water treatment system |
| CN101870508B (en) * | 2009-02-06 | 2014-10-15 | 可虑康国际公司 | grey water treatment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102139990A (en) | Ultrasonic combined waste water treatment process and system of refuse leachate | |
| CN102417235B (en) | Continuous gas stripping biological aerated filter sewage treatment device | |
| CN113582339A (en) | Energy-conserving MBR sewage treatment system | |
| CN2466152Y (en) | Combined intermediate water recycle apparatus | |
| CN210313931U (en) | Aerobic treatment device | |
| CN210764843U (en) | Rural sewage treatment plant | |
| CN203269735U (en) | Equipment for treating rubbish leachate by utilizing two-stage bioreactors | |
| CN212334941U (en) | Integrated high-efficiency biological sewage treatment device | |
| CN215480427U (en) | Domestic sewage integration treatment facility | |
| CN210163300U (en) | Skid-mounted sewage treatment equipment suitable for indirect thermal desorption of organic contaminated soil | |
| CN2341977Y (en) | Deep purifier for reuse of waste water | |
| CN205088072U (en) | Sewage treating and filtering device | |
| CN2507858Y (en) | Integral sewage treating device | |
| CN208933075U (en) | A kind of garbage leachate treatment device | |
| CN206219377U (en) | A kind of integrated sewage treating apparatus for not producing sludge | |
| CN2633872Y (en) | ICAST treatment self control and monitoring device for waste water reutilizing in small community | |
| CN215161711U (en) | Sewage treatment is with deposiing device | |
| CN109095726A (en) | A kind of leather waste water intermediate water reuse system | |
| CN220393476U (en) | Wastewater treatment device capable of realizing multi-layer separation | |
| CN216005352U (en) | Energy-conserving MBR sewage treatment system | |
| CN212854794U (en) | Multifunctional full-automatic filtering equipment | |
| CN220766733U (en) | Intelligent organic wastewater reclaimed water purifying tank | |
| KR100339017B1 (en) | Advanced Wate Water Treatment System of Package Type | |
| CN220283791U (en) | Combined aeration biological filter with denitrification and dephosphorization functions | |
| CN216687823U (en) | Isopropyl alcohol sewage treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |