CN208200600U - Thermoelectricity station-service garbage leachate treatment device - Google Patents
Thermoelectricity station-service garbage leachate treatment device Download PDFInfo
- Publication number
- CN208200600U CN208200600U CN201820535752.1U CN201820535752U CN208200600U CN 208200600 U CN208200600 U CN 208200600U CN 201820535752 U CN201820535752 U CN 201820535752U CN 208200600 U CN208200600 U CN 208200600U
- Authority
- CN
- China
- Prior art keywords
- pipe
- reverse osmosis
- outlet pipe
- reaction chamber
- dope
- 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
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses thermoelectricity station-service garbage leachate treatment devices, it includes continuous filter (1), and continuous filter (1) bottom is connected with reaction chamber (3) by first pipe (2)；It is provided with partition (4) in reaction chamber (3), is provided with agitating shaft (6) above partition (4), mixing arm (7) are connected on agitating shaft (6)；The first filtering layer (8) and the second filtering layer (9) are provided with below partition (4), reaction chamber (3) top surface is equipped with opening for pouring medicine (10) and motor (12)；Disc tube reverse osmosis (dt-ro) cylinder (14) are connected with by second pipe (13) on reaction chamber (3) one side, it is provided with outlet pipe (15), inlet tube (16) and dope outlet pipe (17) on the bottom surface of disc tube reverse osmosis (dt-ro) cylinder (14), analysis salt device (18) is connected in dope outlet pipe (17).The utility model can not only improve recovery utilization rate, also have the advantages that low energy consumption, occupied area is small, filter effect is good and percolate good treatment efficiency.
Description
Technical field
The utility model relates to a kind of diafiltration liquid processing devices, especially thermoelectricity station-service garbage leachate treatment device.
Background technique
Landfill leachate is a kind of high concentrated organic wastewater for complicated component that rubbish generates during landfill, main next
Generated derived from precipitation infiltration, rubbish itself and organic matter degradation etc., currently, domestic mainly have the method for landfill leachate treatment
Physico-chemical process, bioanalysis and land treatment systems method etc., and due to the ingredient properties of percolate, if to be reached using the above method
To ideal treatment effect, used diafiltration liquid processing device needs to spend biggish energy consumption, and energy consumption is higher；And percolate
In there is much recyclable inorganic salts, and existing diafiltration liquid processing device cannot recycle these inorganic salts, time
It is lower to receive utilization rate.Therefore, there is recovery utilization rate is lower and the higher problem of energy consumption for existing diafiltration liquid processing device.
Utility model content
The purpose of the utility model is to provide a kind of thermoelectricity station-service garbage leachate treatment devices.The utility model is not
It only can be improved recovery utilization rate, also have the advantages that low energy consumption.
The technical solution of the utility model includes: thermoelectricity station-service garbage leachate treatment device, including continuous filter, the bottom of continuous filter
Portion is provided with first pipe；First pipe one end is connected with reaction chamber, and partition is provided in reaction chamber, and partition is equipped with through-hole；
It is vertically arranged with agitating shaft above partition, a plurality of mixing arm is connected on agitating shaft；It is provided with below partition in hemisphere face
First filtering layer of shape, the first filtering layer bottom are connected with the second filtering layer；The reaction chamber top surface is equipped with opening for pouring medicine, opening for pouring medicine top
Baffle is installed；Opening for pouring medicine side is provided with motor, motor and stirring axis connection；Reaction chamber one side bottom is connected with the second pipe
Road, second pipe one end are connected with disc tube reverse osmosis (dt-ro) cylinder；Outlet pipe, outlet pipe are provided on the bottom surface of disc tube reverse osmosis (dt-ro) cylinder
Side be provided with inlet tube, the other side of outlet pipe is provided with dope outlet pipe, be connected in dope outlet pipe analysis salt device.
In thermoelectricity station-service garbage leachate treatment device above-mentioned, strut, strut are set in the disc tube reverse osmosis (dt-ro) cylinder
On be connected with the equally distributed disc tube reverse osmosis (dt-ro) film of multilayer, be provided with deflector between adjacent two layers disc tube reverse osmosis (dt-ro) film.
In thermoelectricity station-service garbage leachate treatment device above-mentioned, it is socketed with rubber ring outside the strut, rubber ring is located at
Between strut and deflector, light sap cavity is equipped between strut and rubber ring；The disc tube reverse osmosis (dt-ro) cylinder side wall and deflector it
Between be equipped with flow into chamber, between strut and deflector be equipped with dope chamber.
In thermoelectricity station-service garbage leachate treatment device above-mentioned, described inlet tube one end is connect with second pipe, another
End is connect with chamber is flowed into；Dope outlet pipe is connect with dope chamber, and outlet pipe is connect with light sap cavity.
In thermoelectricity station-service garbage leachate treatment device above-mentioned, the analysis salt device includes catalysis oxidation case, is catalyzed oxygen
Change case one side to connect with dope outlet pipe, third pipeline is provided on the another side of catalysis oxidation case；Third pipeline one end connects
It connects and is provided with evaporation tank, evaporation tank one end is provided with salt discharging pipe.
Compared with prior art, the utility model improves existing diafiltration liquid processing device, by setting reaction chamber and
Disc tube reverse osmosis (dt-ro) cylinder carries out preliminary treatment to percolate using reaction chamber, then passes through the dish tubular type in disc tube reverse osmosis (dt-ro) cylinder
Reverse osmosis membrane, so that filter membrane is handled again by the percolate of preliminary treatment, water up to standard is discharged；And condensed water enters
Catalytic oxidizing equipment, and the solid inside condensed water is salted out to and is discharged recycling in vaporising device, not only simplify work
Skill process, reduces energy consumption, also improves the recovery utilization rate of organic matter in percolate, more environmentally-friendly energy conservation；Pass through setting the
One filtering layer and the second filtering layer, and the first filtering layer and the second filtering layer are in arc-shaped, are that the bulky grain on the first filtering layer can filter
It can enter in the second filtering layer under the collective effect of liquid and gravity, the filter opening of the first filtering layer is prevented to be blocked, guarantee filter effect；Together
When, it is mutually compact between each device process, reduce occupied area.In addition, the utility model is also by dish tubular type reverse osmosis
Multilayer disc tube reverse osmosis (dt-ro) film is set on saturating cylinder, is provided with deflector between adjacent two layers disc tube reverse osmosis (dt-ro) film, increases
Contact area between percolate and disc tube reverse osmosis (dt-ro) film improves percolate treatment effeciency；By in strut and deflector
Between be provided with rubber ring, prevent percolate from entering in light sap cavity, further DIA filtration effect.Therefore, the utility model
It can not only improve recovery utilization rate, also have that low energy consumption, occupied area is small, filter effect is good and percolate good treatment efficiency
Advantage.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the structural schematic diagram of disc tube reverse osmosis (dt-ro) cylinder；
Fig. 3 is the structural schematic diagram of reaction chamber top surface；
Fig. 4 is the cross-sectional view in Fig. 2 at A-A；
Fig. 5 is the cross-sectional view in Fig. 2 at B-B.
The label in accompanying drawing is: the continuous filter 1-, 2- first pipe, 3- reaction chamber, 4- partition, 5- through-hole, 6- agitating shaft, 7-
Mixing arm, the first filtering layer of 8-, the second filtering layer of 9-, 10- opening for pouring medicine, 11- baffle, 12- motor, 13- second pipe, 14- dish tubular type
Reverse osmosis cartridge, 15- outlet pipe, 16- inlet tube, 17- dope outlet pipe, 18- analyse salt device, 19- strut, 20- disc tube reverse osmosis (dt-ro)
Film, 21- deflector, 22- rubber ring, 23- catalysis oxidation case, 24- third pipeline, 25- evaporation tank, 26- salt discharging pipe, the light liquid of 27-
Chamber, 28- flow into chamber, 29- dope chamber.
Specific embodiment
The utility model is further described with reference to the accompanying drawings and examples, but is not intended as to the utility model
The foundation of limitation.
Embodiment.Thermoelectricity station-service garbage leachate treatment device is constituted as shown in Fig. 1 to 5, including continuous filter 1, continuous filter
1 bottom is provided with first pipe 2；2 one end of first pipe is connected with reaction chamber 3, and partition 4, partition 4 are provided in reaction chamber 3
It is equipped with through-hole 5；The top of partition 4 is vertically arranged with agitating shaft 6, and a plurality of mixing arm 7 is connected on agitating shaft 6；Under partition 4
Side is provided with the first filtering layer 8 in hemisphere planar, and 8 bottom of the first filtering layer is connected with the second filtering layer 9；On 3 top surface of reaction chamber
Equipped with opening for pouring medicine 10, baffle 11 is installed above opening for pouring medicine 10；10 side of opening for pouring medicine is provided with motor 12, motor 12 and agitating shaft
6 connections；3 one side bottom of reaction chamber is connected with second pipe 13, and 13 one end of second pipe is connected with disc tube reverse osmosis (dt-ro) cylinder 14；
Outlet pipe 15 is provided on the bottom surface of disc tube reverse osmosis (dt-ro) cylinder 14, the side of outlet pipe 15 is provided with inlet tube 16, outlet pipe 15
The other side be provided with dope outlet pipe 17, be connected in dope outlet pipe 17 analysis salt device 18.
Strut 19 is set in the disc tube reverse osmosis (dt-ro) cylinder 14, and it is anti-to be connected with the equally distributed dish tubular type of multilayer on strut 19
Permeable membrane 20 is provided with deflector 21 between adjacent two layers disc tube reverse osmosis (dt-ro) film 20；Rubber ring is socketed with outside the strut 19
22, rubber ring 22 is equipped with light sap cavity 27 between strut 19 and deflector 21 between strut 19 and rubber ring 22；The dish pipe
It is equipped between 14 side wall of formula reverse osmosis cartridge and deflector 21 and flows into chamber 28, dope chamber 29 is equipped between strut 19 and deflector 21；
Described 16 one end of inlet tube is connect with second pipe 2, and the other end is connect with chamber 28 is flowed into；Dope outlet pipe 17 and dope chamber 29 connect
It connects, outlet pipe 15 is connect with light sap cavity 27；The analysis salt device 18 include catalysis oxidation case 23,23 one side of catalysis oxidation case with
Dope outlet pipe 17 connects, and is provided with third pipeline 24 on the another side of catalysis oxidation case 23；The connection of 24 one end of third pipeline is set
It is equipped with evaporation tank 25,25 one end of evaporation tank is provided with salt discharging pipe 26.
Working principle: rubbish is placed into continuous filter 1, and is placed 3 to 5 days, and the percolate of generation can pass through the first pipe
Road 2 enters in reaction chamber 3, then opens motor 12, opens simultaneously baffle 11, and treatment of pharmaceutical products is passed through the investment reaction of opening for pouring medicine 10
Flocculation sedimentation is carried out to percolate in case 3；Motor 12 will drive the rotation of agitating shaft 6 after opening, the rotation of agitating shaft 6 will drive stirring
Arm 7 rotates, and is sufficiently mixed treatment of pharmaceutical products with percolate, accelerates reaction speed；Stir complete percolate can by every
Through-hole 5 on plate 4 flows on the first filtering layer 8, and the bulky grain in percolate is filtered out and stays in the first filtering layer 8 by the first filtering layer 8
On, since the first filtering layer 8 is in arc-shaped, and the diameter of the filter opening of the first filtering layer 8 is bigger than the diameter of the filter opening of the second filtering layer 9, makes
The bulky grain filtered out is rolled under the collective effect of percolate and gravity in the second filtering layer 9；Filtered percolate can pass through
Second pipe 13 and inlet tube 16 enter in the inflow chamber 28 of disc tube reverse osmosis (dt-ro) cylinder 14, into the percolate meeting flowed into chamber 28
Moving up subsequently into dope chamber 29 slowly, can be one under the action of deflector 21 into the percolate in dope chamber 29
Side is contacted with disc tube reverse osmosis (dt-ro) film 20, one side flow down, after percolate is contacted with disc tube reverse osmosis (dt-ro) film 20, in percolate
Fresh water can under the osmosis of disc tube reverse osmosis (dt-ro) film 20 enter light sap cavity 27 in, can go out into the light liquid in light sap cavity 27
Water pipe 15 emits, and can not flow into dope under the action of deflector 21 by the percolate of disc tube reverse osmosis (dt-ro) film 20
Then 29 bottom of chamber is entered in analysis salt device 18 by dope outlet pipe 17；It can be introduced into the percolate in analysis salt device 18
In catalysis oxidation case 23, dope is reacted in catalysis oxidation case 23, and the liquid after reaction is entered by third pipeline 24 to be steamed
It is evaporated crystallization in hair case 25, the salt being finally precipitated can be discharged from salt discharging pipe 26.
Claims (5)
1. thermoelectricity station-service garbage leachate treatment device, it is characterised in that: including continuous filter (1), the bottom of continuous filter (1) is arranged
There are first pipe (2)；First pipe (2) one end is connected with reaction chamber (3), is provided with partition (4) in reaction chamber (3), partition (4)
It is equipped with through-hole (5)；It is vertically arranged with above partition (4) agitating shaft (6), agitating shaft is connected with a plurality of mixing arm on (6)
(7)；The first filtering layer (8) in hemisphere planar is provided with below partition (4), the first filtering layer (8) bottom is connected with the second filtering layer
(9)；Reaction chamber (3) top surface is equipped with opening for pouring medicine (10), is equipped with baffle (11) above opening for pouring medicine (10)；Opening for pouring medicine (10)
Side is provided with motor (12), and motor (12) is connect with agitating shaft (6)；Reaction chamber (3) one side bottom is connected with second pipe
(13), second pipe (13) one end is connected with disc tube reverse osmosis (dt-ro) cylinder (14)；It is arranged on the bottom surface of disc tube reverse osmosis (dt-ro) cylinder (14)
Have outlet pipe (15), the side of outlet pipe (15) is provided with inlet tube (16), and the other side of outlet pipe (15) is provided with dope and goes out
It manages (17), analysis salt device (18) is connected in dope outlet pipe (17).
2. thermoelectricity station-service garbage leachate treatment device according to claim 1, it is characterised in that: the dish tubular type reverse osmosis
Strut (19) are set in saturating cylinder (14), are connected with the equally distributed disc tube reverse osmosis (dt-ro) film (20) of multilayer on strut (19), it is adjacent
Deflector (21) are provided between two layers of disc tube reverse osmosis (dt-ro) film (20).
3. thermoelectricity station-service garbage leachate treatment device according to claim 2, it is characterised in that: the strut (19) is outside
It is socketed with rubber ring (22), rubber ring (22) is located between strut (19) and deflector (21), strut (19) and rubber ring (22)
Between be equipped with light sap cavity (27)；It is equipped between disc tube reverse osmosis (dt-ro) cylinder (14) side wall and deflector (21) and flows into chamber (28),
Dope chamber (29) are equipped between strut (19) and deflector (21).
4. thermoelectricity station-service garbage leachate treatment device according to claim 3, it is characterised in that: the inlet tube (16)
One end is connect with second pipe (13), and the other end is connect with chamber (28) are flowed into；Dope outlet pipe (17) is connect with dope chamber (29), out
Water pipe (15) is connect with light sap cavity (27).
5. thermoelectricity station-service garbage leachate treatment device according to claim 1,2,3 or 4, it is characterised in that: the analysis
Salt device (18) includes catalysis oxidation case (23), and catalysis oxidation case (23) one side is connect with dope outlet pipe (17), catalysis oxidation
Third pipeline (24) are provided on the another side of case (23)；Third pipeline (24) one end is connected with evaporation tank (25), is steamed
Hair case (25) one end is provided with salt discharging pipe (26).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820535752.1U CN208200600U (en) | 2018-04-16 | 2018-04-16 | Thermoelectricity station-service garbage leachate treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820535752.1U CN208200600U (en) | 2018-04-16 | 2018-04-16 | Thermoelectricity station-service garbage leachate treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208200600U true CN208200600U (en) | 2018-12-07 |
Family
ID=64523251
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820535752.1U Active CN208200600U (en) | 2018-04-16 | 2018-04-16 | Thermoelectricity station-service garbage leachate treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208200600U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112225352A (en) * | 2020-10-15 | 2021-01-15 | 蛋壳城矿环保科技发展(广州)有限公司 | High-efficient surplus leachate treatment facility in kitchen |
| CN113461208A (en) * | 2021-07-09 | 2021-10-01 | 寿光市祥云防水材料有限公司 | Effluent treatment plant is used in water proof coating production |
-
2018
- 2018-04-16 CN CN201820535752.1U patent/CN208200600U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112225352A (en) * | 2020-10-15 | 2021-01-15 | 蛋壳城矿环保科技发展(广州)有限公司 | High-efficient surplus leachate treatment facility in kitchen |
| CN113461208A (en) * | 2021-07-09 | 2021-10-01 | 寿光市祥云防水材料有限公司 | Effluent treatment plant is used in water proof coating production |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206927730U (en) | A kind of efficient sedimentation tank | |
| CN211419816U (en) | Solid-liquid separation's domestic sewage treatment plant | |
| CN208200600U (en) | Thermoelectricity station-service garbage leachate treatment device | |
| CN207137439U (en) | A kind of settler for life kind sewage | |
| CN108862705A (en) | A kind of chemical waste liquid secure processing device | |
| CN206604241U (en) | A kind of novel pressure formula mechanical filter | |
| CN207986877U (en) | A kind of settler of processing household sewage | |
| CN207143024U (en) | A kind of multifunction environment-protection type sewage purification processing system | |
| CN205088040U (en) | Sewage treatment plant carries mark technological transformation degree of depth filtration system | |
| CN205933455U (en) | Industrial waste water high -efficiency processing device | |
| CN210085201U (en) | Sewage treatment device capable of recycling | |
| CN109694163B (en) | Toilet flushing water treatment system | |
| CN209242840U (en) | A kind of landfill leachate resources processing complete set of equipments | |
| CN206415410U (en) | Fecal pollution processing is with smashing equipment and fecal pollution processing system | |
| CN101643302B (en) | Water treatment device | |
| CN205616718U (en) | A bioreaction system for handling beasts and birds breed waste water | |
| CN213803482U (en) | River sludge collecting and cleaning device | |
| CN108689555A (en) | A kind of rural sewage purification system of integration | |
| CN208485718U (en) | A kind of double purification sewage disposal devices | |
| CN211521928U (en) | Water treatment equipment | |
| CN206467074U (en) | Integrated reclaimed water and rainwater treatment device | |
| CN106746029A (en) | A kind of coagulation device for sewage disposal | |
| CN113213667A (en) | Leachate treatment equipment and use method thereof | |
| CN208151108U (en) | A kind of intermediate water reuse system for recirculated cooling water | |
| CN207024734U (en) | Sewage treatment and recovery pond |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |