CN208038269U - A kind of Two-way Cycle multistage anaerobic reaction unit - Google Patents
A kind of Two-way Cycle multistage anaerobic reaction unit Download PDFInfo
- Publication number
- CN208038269U CN208038269U CN201820340717.4U CN201820340717U CN208038269U CN 208038269 U CN208038269 U CN 208038269U CN 201820340717 U CN201820340717 U CN 201820340717U CN 208038269 U CN208038269 U CN 208038269U
- Authority
- CN
- China
- Prior art keywords
- liquid separator
- anaerobic reaction
- cyclone gas
- gas
- condenser
- 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
- Cyclones (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a kind of Two-way Cycle multistage anaerobic reaction units, belong to wastewater recovery processing equipment field, including water inlet pipe and cyclone gas-liquid separator, the water inlet pipe is connected with the retort, the water inlet pipe is connected by return duct with reflux force (forcing) pump, the reflux force (forcing) pump is connected with condenser, the condenser between the cyclone gas-liquid separator by being provided with recovery tube, the condenser side is provided with threeway coupling bar, the cyclone gas-liquid separator is arranged at the top of the retort, the cyclone gas-liquid separator is connected by gas collecting tube with the retort, it is provided with firedamp drainage pipe at the top of the cyclone gas-liquid separator.The utility model can carry out Two-way Cycle to the water in wastewater treatment process, improve water use efficiency, and waste water treatment efficiency is improved by the water of recycling, while the utility model can also carry out multistage according to actual demand and wear even use, to improve water treatment effect.
Description
Technical field
The utility model belongs to wastewater recovery processing equipment field, and in particular to a kind of Two-way Cycle multistage anaerobic reaction dress
It sets.
Background technology
High concentrated organic wastewater is common a kind of sewage in factory, enterprise's life and production process, and feature is exactly COD
Concentration is high, therefore intractability is higher, and conventional high-concentration organic wastewater treatment device includes UASB anaerobic reactors, anaerobism
, there is the problems such as investment is big, and operating cost is high, poor processing effect in biofilter etc., the presence of these problems causes highly concentrated
Spend with high costs, the disadvantage of promoted extension difficulty for the treatment of of Organic Wastewater.
And, the aggravation of environmental pollution and increasingly the carrying of people environmental consciousness increasing with the output of organic wastewater
Height needs to make improvement to organic wastewater anaerobic reaction.
Utility model content
The purpose of this utility model is that solve the above-mentioned problems and provides a kind of Two-way Cycle multistage anaerobic reaction dress
It sets.
The utility model is achieved through the following technical solutions above-mentioned purpose：
A kind of Two-way Cycle multistage anaerobic reaction unit, including water inlet pipe and cyclone gas-liquid separator, the water inlet pipe and institute
It states retort to be connected, the water inlet pipe is connected by return duct with reflux force (forcing) pump, the reflux force (forcing) pump and condenser
It is connected, the condenser is provided with by being provided with recovery tube, the condenser side between the cyclone gas-liquid separator
Threeway coupling bar, the cyclone gas-liquid separator are arranged at the top of the retort, and the cyclone gas-liquid separator passes through collection
Tracheae is connected with the retort, and firedamp drainage pipe, the cyclone gas-liquid point are provided at the top of the cyclone gas-liquid separator
Device bottom is provided with hollow flow-guiding vertical beam frame, the hollow flow-guiding vertical beam frame bottom is provided with dispenser, the retort
Both sides are provided with fixed frame, and level-one three phase separator and two level three are disposed with from top to bottom on the hollow flow-guiding vertical beam frame
Phase separator, threeway coupling bar bottom are provided with anaerobic reaction agent.
In above structure, pending high concentrated organic wastewater is injected by the water inlet pipe in the retort, with
The anaerobic reaction agent of the reaction pot bottom is reacted, and the biogas generated after reaction passes through described in gas collecting tube injection
Cyclone gas-liquid separator, and emitted by the firedamp drainage pipe after being detached with vapor, the vapor in anaerobic reaction
Enter in the cyclone gas-liquid separator after the separation of the level-one three phase separator and the two level three phase separator, and
It rear vapor is isolated by the cyclone gas-liquid separator is imported in the condenser by the recovery tube and condensed, it is cold
Water after solidifying is imported by the return duct in the water inlet pipe after being pressurizeed by the reflux force (forcing) pump, is carried out circular response, is carried
The diffusion area of high sewage, to improve its reaction speed.
In order to further increase the performance of the utility model, the water inlet pipe is sealed with the return duct by pipe collar
Twist-on, the return duct seal twist-on with the reflux force (forcing) pump by pipe collar, and the reflux force (forcing) pump is logical with the condenser
Piping is connected to.
In order to further increase the performance of the utility model, the condenser passes through pipe collar with the threeway coupling bar
Twist-on is sealed, the condenser is connect with the recovery tube by gasket, the recovery tube and the cyclone gas-liquid separator
Twist-on is sealed by pipe collar.
In order to further increase the performance of the utility model, the retort is welded to connect with the fixed frame, institute
The interval stated between level-one three phase separator and the two level three phase separator is not less than 50 centimetres.
In order to further increase the performance of the utility model, the gas collecting tube is sealed with the cyclone gas-liquid separator
Connection, the cyclone gas-liquid separator are connect with the firedamp drainage seal of tube.
In order to further increase the performance of the utility model, the hollow flow-guiding vertical beam frame and the cyclone gas-liquid point
It seals and is connected to from device, the hollow flow-guiding vertical beam frame is connected to dispenser sealing, and the dispenser bottom is provided with through-hole.
In order to further increase the performance of the utility model, the dispenser is directly embedded in the anaerobic reaction agent
Portion.
Advantageous effect is：The utility model can carry out Two-way Cycle to the water in wastewater treatment process, improve water
Utilization rate, and waste water treatment efficiency is improved by the water of recycling, while the utility model can also be carried out according to actual demand
Multistage, which is worn, even to be used, to improve water treatment effect.
Description of the drawings
Fig. 1 is a kind of front view of Two-way Cycle multistage anaerobic reaction unit described in the utility model；
Fig. 2 is that a kind of two-stage of Two-way Cycle multistage anaerobic reaction unit described in the utility model wears even schematic diagram；
Fig. 3 is that a kind of three-level of Two-way Cycle multistage anaerobic reaction unit described in the utility model wears even schematic diagram.
The reference numerals are as follows：
1, water inlet pipe；2, return duct；3, flow back force (forcing) pump；4, condenser；5, retort；6, fixed frame；7, dispenser；
8, level-one three phase separator；9, hollow flow-guiding vertical beam frame；10, two level three phase separator；11, gas collecting tube：12, cyclone gas-liquid detaches
Device；13, firedamp drainage pipe；14, recovery tube；15, threeway coupling bar；16, anaerobic reaction agent.
Specific implementation mode
The utility model is described in further detail below in conjunction with the accompanying drawings：
As shown in Figs. 1-3, a kind of Two-way Cycle multistage anaerobic reaction unit, including water inlet pipe 1 and cyclone gas-liquid separator 12,
Water inlet pipe 1 is connected with retort 5, water inlet pipe 1 by return duct 2 with reflux force (forcing) pump 3 be connected, reflux force (forcing) pump 3 with it is cold
Condenser 4 is connected, and condenser 4 is provided with three by being provided with recovery tube 14,4 side of condenser between cyclone gas-liquid separator 12
Logical coupling bar 15, cyclone gas-liquid separator 12 are arranged at the top of retort 5, cyclone gas-liquid separator 12 by gas collecting tube 11 with
Retort 5 is connected, and 12 top of cyclone gas-liquid separator is provided with firedamp drainage pipe 13, the setting of 12 bottom of cyclone gas-liquid separator
There are hollow flow-guiding vertical beam frame 9,9 bottom of hollow flow-guiding vertical beam frame to be provided with dispenser 7, the both sides of retort 5 are provided with fixed frame
6, it is disposed with level-one three phase separator 8 and two level three phase separator 10 from top to bottom on hollow flow-guiding vertical beam frame 9, three lead to
It connects 15 bottom of bolt and is provided with anaerobic reaction agent 16.
In above structure, pending high concentrated organic wastewater is injected by water inlet pipe 1 in retort 5, with retort 5
The anaerobic reaction agent 16 of bottom is reacted, and the biogas generated after reaction injects cyclone gas-liquid separator 12 by gas collecting tube 11,
And emitted by firedamp drainage pipe 13 after being detached with vapor, the vapor in anaerobic reaction passes through level-one three phase separator
8 and two level three phase separator 10 separation after enter in cyclone gas-liquid separator 12, and by cyclone gas-liquid separator 12 by its point
From rear vapor by recovery tube 14 import condenser 4 in condensed, condensed water by flow back force (forcing) pump 3 pressurize after by
Return duct 2 imports in water inlet pipe 1, carries out circular response, the diffusion area of sewage is improved, to improve its reaction speed.
In order to further increase the performance of the utility model, water inlet pipe 1 seals twist-on with return duct 2 by pipe collar,
Return duct 2 and reflux force (forcing) pump 3 seal twist-on by pipe collar, and reflux force (forcing) pump 3 is connected to condenser 4 by pipeline, and reflux adds
Press pump 3 imports after the water that condenser 4 condenses can pressurize in retort 5 again, and condenser 4 passes through pipe collar with threeway coupling bar 15
Twist-on is sealed, threeway coupling bar 15 can provide the effect of multi-stage sealed connection, and condenser 4 is connected with recovery tube 14 by gasket
It connects, recovery tube 14 seals twist-on with cyclone gas-liquid separator 12 by pipe collar, and retort 5 is welded to connect with fixed frame 6, fixed frame
6 can be used for the fixation of the utility model, and the interval between level-one three phase separator 8 and two level three phase separator 10 is not less than five
Ten centimetres, it is ensured that the effect of three phase separation, gas collecting tube 11 are tightly connected with cyclone gas-liquid separator 12, cyclone gas-liquid separation
Device 12 is tightly connected with firedamp drainage pipe 13, and cyclone gas-liquid separator 12 can detach biogas and vapor, and hollow flow-guiding is perpendicular
The sealing of roof beam structure 9 and cyclone gas-liquid separator 12 is connected to, and hollow flow-guiding vertical beam frame 9 can will condense in cyclone gas-liquid separator 12
Water imports in retort 5, and hollow flow-guiding vertical beam frame 9 is connected to the sealing of dispenser 7, and 7 bottom of dispenser is provided with through-hole, dispenser
7 are directly embedded to inside anaerobic reaction agent 16, can improve the contact area of waste water and anaerobic reaction agent 16, improve wastewater treatment effect
Rate.
The basic principles and main features and advantage of the utility model have been shown and described above.The technical staff of the industry
It should be appreciated that the present utility model is not limited to the above embodiments, the above embodiments and description only describe this
The principle of utility model, on the premise of not departing from the spirit and scope of the utility model, the utility model also has various change
And improvement, these various changes and improvements fall within the scope of the claimed invention.
Claims (7)
1. a kind of Two-way Cycle multistage anaerobic reaction unit, it is characterised in that：Including water inlet pipe and cyclone gas-liquid separator, it is described into
Water pipe is connected with the retort, and the water inlet pipe is connected by return duct with reflux force (forcing) pump, the reflux force (forcing) pump
It is connected with condenser, the condenser is by being provided with recovery tube, the condenser side between the cyclone gas-liquid separator
While being provided with threeway coupling bar, the cyclone gas-liquid separator is arranged in the top of the retort, the cyclone gas-liquid separation
Device is connected by gas collecting tube with the retort, and firedamp drainage pipe, the rotation are provided at the top of the cyclone gas-liquid separator
Gas liquid/gas separator bottom is provided with hollow flow-guiding vertical beam frame, and the hollow flow-guiding vertical beam frame bottom is provided with dispenser, described
The both sides of retort are provided with fixed frame, and level-one three phase separator is disposed with from top to bottom on the hollow flow-guiding vertical beam frame
With two level three phase separator, threeway coupling bar bottom is provided with anaerobic reaction agent.
2. a kind of Two-way Cycle multistage anaerobic reaction unit according to claim 1, it is characterised in that：The water inlet pipe and institute
It states return duct and twist-on is sealed by pipe collar, the return duct seals twist-on, the reflux with the reflux force (forcing) pump by pipe collar
Force (forcing) pump is connected to the condenser by pipeline.
3. a kind of Two-way Cycle multistage anaerobic reaction unit according to claim 1, it is characterised in that：The condenser and institute
It states threeway coupling bar and twist-on is sealed by pipe collar, the condenser is connect with the recovery tube by gasket, the recovery tube
Twist-on is sealed by pipe collar with the cyclone gas-liquid separator.
4. a kind of Two-way Cycle multistage anaerobic reaction unit according to claim 1, it is characterised in that：The retort and institute
It states fixed frame to be welded to connect, the interval between the level-one three phase separator and the two level three phase separator is not less than 50 lis
Rice.
5. a kind of Two-way Cycle multistage anaerobic reaction unit according to claim 1, it is characterised in that：The gas collecting tube and institute
Cyclone gas-liquid separator sealed connection is stated, the cyclone gas-liquid separator is connect with the firedamp drainage seal of tube.
6. a kind of Two-way Cycle multistage anaerobic reaction unit according to claim 1, it is characterised in that：The hollow flow-guiding is perpendicular
Roof beam structure is connected to cyclone gas-liquid separator sealing, and the hollow flow-guiding vertical beam frame is connected to dispenser sealing, described
Dispenser bottom is provided with through-hole.
7. a kind of Two-way Cycle multistage anaerobic reaction unit according to claim 1, it is characterised in that：The dispenser is direct
It is embedded to inside the anaerobic reaction agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820340717.4U CN208038269U (en) | 2018-03-13 | 2018-03-13 | A kind of Two-way Cycle multistage anaerobic reaction unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820340717.4U CN208038269U (en) | 2018-03-13 | 2018-03-13 | A kind of Two-way Cycle multistage anaerobic reaction unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208038269U true CN208038269U (en) | 2018-11-02 |
Family
ID=63951215
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820340717.4U Active CN208038269U (en) | 2018-03-13 | 2018-03-13 | A kind of Two-way Cycle multistage anaerobic reaction unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208038269U (en) |
-
2018
- 2018-03-13 CN CN201820340717.4U patent/CN208038269U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204474409U (en) | Rectilinear anaerobic aerobic integratedization reactor | |
| CN203699916U (en) | Phosphorus-containing tail gas washing and recycling device for yellow phosphorus production | |
| CN208038269U (en) | A kind of Two-way Cycle multistage anaerobic reaction unit | |
| CN208883660U (en) | A kind of sewage-treatment plant | |
| CN207435144U (en) | A kind of efficient double-cycling anaerobic reactor | |
| CN203222476U (en) | System for removing chloro-silane in HCl tail gas | |
| CN107720956A (en) | A kind of efficient double-cycling anaerobic reactor | |
| CN202315356U (en) | Step circulation recovery device of waste heat in xylose production | |
| CN201180698Y (en) | Water jet vacuum pump unit of condenser with embedded pipes | |
| CN203487061U (en) | Methanol recycling device for biodiesel production process | |
| CN206901870U (en) | A kind of efficient compound anaerobic reactor | |
| CN206783403U (en) | A kind of air lift and return decentralized type sewage processing equipment | |
| CN208898710U (en) | Floor-type metaplasia combines pond | |
| CN201424388Y (en) | Urea process wastewater recovering device | |
| CN203346241U (en) | Microwave-strengthening solar-energy reclaimed-water high-temperature double-source heat-pump sludge-drying system | |
| CN207699400U (en) | A kind of high-concentration waste water ion membrane treatment appts | |
| CN203474699U (en) | Rectification type esterification reaction system for polycarboxylate water reducer | |
| CN205635427U (en) | Continuous negative pressure of acetonitrile distillation extraction device | |
| CN214654713U (en) | Biogas pretreatment fine filtration-condensation dehydration integrated device | |
| CN214747342U (en) | Gas station stove bottom steam condensate water collection device | |
| CN213506674U (en) | Novel synthetic leather waste water treatment heat pump rectification system | |
| CN210251258U (en) | Energy-conserving efficient dilute acid liquid enrichment facility | |
| CN212833325U (en) | Landfill leachate evaporation treatment device | |
| CN204607766U (en) | A kind of Waste water concentrating system | |
| CN201554684U (en) | Water recycling device of water ring pump |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |