CN105169775B - A kind of sewage-treatment plant that COD ss suspended solid is effectively reduced - Google Patents
A kind of sewage-treatment plant that COD ss suspended solid is effectively reduced Download PDFInfo
- Publication number
- CN105169775B CN105169775B CN201510590505.2A CN201510590505A CN105169775B CN 105169775 B CN105169775 B CN 105169775B CN 201510590505 A CN201510590505 A CN 201510590505A CN 105169775 B CN105169775 B CN 105169775B
- Authority
- CN
- China
- Prior art keywords
- filter
- tee tube
- sewage
- plate
- cod
- 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
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The invention discloses a kind of sewage-treatment plants that COD ss suspended solid is effectively reduced, including filter, hydraulic workstation, electric cabinet, cesspool, sludge-tank and clean solution tank, filter is equipped with thrust plate and pressure plate, and filter plate and filter cloth are equipped between thrust plate and pressure plate;Filter is equipped with oil cylinder seat, and oil cylinder seat is equipped with oil cylinder;Filter is equipped with crossbeam, and crossbeam is equipped with drawing-plate mechanism;The first tee tube is equipped between inlet and cesspool, first tee tube connects sludge-tank, spoil disposal slag valve is equipped between first tee tube and sludge-tank, exhalant canal is equipped with the second tee tube, one end of second tee tube is connected with backwashing pump, the other end of second tee tube is connected to clean solution tank, and outlet valve is equipped between the second tee tube and clean solution tank.The present invention has the function of continuous filtration, and combined filtering machine is filtered effect to sewage, and filter plates area is big, has the effect of increasing water flow, COD ss suspended solid content is effectively reduced.
Description
Technical field
The invention belongs to technical field of sewage more particularly to a kind of sewage treatments that COD ss suspended solid is effectively reduced
Device.
Background technique
Trade effluent refers to the sewage and waste liquid generated in industrial processes, wherein containing the industrial production outflowed with water
The pollutant generated in materials, intermediate product and product and production process.With industry rapid development, the type of sewage and
Quantity rapidly increases, also increasingly extensively and serious to the pollution of water body, threatens the health and safety of the mankind.Therefore, for protection
For environment, the processing of trade effluent is more even more important than the processing of municipal sewage.With economic fast development, people's lives water
Flat constantly to be promoted, the requirement to ecological environment also increasingly improves, therefore more and more trade effluent needs are up to standard by handling
After discharge.
Dyeing and printing sewage processing is exactly one kind of Industrial Waste Water Treatments.Dyeing and printing sewage water quality is complicated, pollutant main source are as follows:
Entrainment of the one kind from fibrous raw material itself;Another kind of is slurry used in process, finish, dyestuff, chemical assistant
Deng.Dyeing and printing sewage water is big, organic pollutant content is high, coloration is deep, alkalinity and pH value variation greatly, change of water quality it is violent, suspension
Object content is high.Currently, the common method of processing sewage is roughly divided into three kinds: 1, utilizing the organic matter in microorganism removal sewage
Biological mode;2, using coagulation, air bearing, precipitating, filters mechanical treatment;3, the life of film, bag, porous material absorption is utilized
Change the materilization freatment method combined with physics to reduce COD, meets discharge standard.Currently, plate and frame pressure mud machine be it is a kind of with
The machinery that sludge is major function is squeezed, mechanical force is applied by side and realizes squeeze and filter process, mud is carried out to sewage-mud
Water separation.It is mainly characterized by that occupied area is small, and squeezing area is big, the disadvantage is that exhalant canal is not smooth, discontinuous work,
It cannot be used in the technique of drainage as the main purpose.
Summary of the invention
Above-mentioned technical problem present in present invention aims to solve the prior art, providing one kind, that COD is effectively reduced is outstanding
The sewage-treatment plant of floating object SS, has the function of continuous filtration, and combined filtering machine is filtered effect, filter plate to sewage
In be additionally arranged rhone, filter area is big, has the effect of increasing water flow, improves filtering accuracy, it is outstanding that COD is effectively reduced
Floating object SS content.
In order to solve the above-mentioned technical problem, the present invention adopts the following technical scheme:
A kind of sewage-treatment plant that COD ss suspended solid is effectively reduced, including filter, hydraulic workstation, electric cabinet, dirt
Pond, sludge-tank and clean solution tank, it is characterised in that: filter is equipped with thrust plate and pressure plate, between thrust plate and pressure plate
Equipped with filter plate and filter cloth, filter chamber is formed between filter plate, filter cloth is set in filter chamber, and filter plate is equipped with inlet, apopore and water outlet
Channel;Filter is equipped with oil cylinder seat, and oil cylinder seat is equipped with oil cylinder, and oil cylinder connects pressure plate;Filter is equipped with crossbeam, crossbeam
It is equipped with drawing-plate mechanism;Inlet is connect with cesspool, and the first tee tube, the first tee tube are equipped between inlet and cesspool
Connect sludge-tank, between the first tee tube and sludge-tank be equipped with spoil disposal slag valve, exhalant canal be equipped with the second tee tube, second
One end of tee tube is connected with backwashing pump, and backwashing pump connects clean solution tank, and the other end of the second tee tube is connected to clean solution tank, the
It is equipped with outlet valve between two tee tubes and clean solution tank, has the function of continuous filtration, filter area is big, increases water flow out
Amount, improves filtering accuracy, COD ss suspended solid content is effectively reduced.
Further, cesspool is connected with feed pump, and feed pump connects the first tee tube, and feed pump is by the sewage in cesspool
It is pumped into the first tee tube.
Further, between feed pump and the first tee tube be equipped with first check-valve, first check-valve control feed pump into
Material process.
Further, second check-valve is equipped between the second tee tube and backwashing pump, second check-valve controls backwashing pump
Backwash process.
Further, third tee tube is equipped between the first tee tube and inlet, third tee tube is connected with feed pressure
Table, feed pressure table show that feed pump is pumped into the flow of sewage in pipeline.
Further, filter plate is equipped with rhone, and rhone is uniformly distributed on filter plate in " 1 " font or so, improves water outlet
Fluency.
Further, the section of rhone is semicircular arc, and the radius in the section of rhone is 1~2mm, and body refuse is intercepted at
Outside rhone, filtrate is drained into exhalant canal along rhone, can be improved water yield, while improving water outlet fluency.
Further, filter cloth uses two-layer fabric structure, and it is fine and closely woven to have an interlacing point, and intensity is high, captures energy to fine particle
Power is strong, and stripping performance is good, acidproof, alkaline-resisting feature.
Further, inlet is set to the lower half portion of filter plate, and sewage enters in filter chamber from inlet, passes through turning for valve
It changes, inlet can be not only used for feed liquor, and can be used for deslagging.
The present invention is by adopting the above-described technical solution, have the advantages that
1, during the filtration process, under the action of drawing-plate mechanism, filter loads upper filter plate to the present invention, in the force of oil cylinder
Under effect, thrust plate and pressure plate compress filter plate, and filter chamber is formed between filter plate, and filter cloth is clamped in filter chamber, complete filter
After installation, spoil disposal slag valve is closed, opens outlet valve, the sewage in cesspool passes through feed pump, first check-valve, from feed liquor
Mouth flows in the filter chamber of filter, and filter cloth and filter plate are filtered sewage, and clear liquid flows to water outlet along filter plate and rhone and leads to
In road, then from exhalant canal reach clean solution tank, subsidence settling, when the discharge of sewage is reduced in pipeline, will close automatically in filter chamber
Feed pump is closed, spoil disposal slag valve is opened, closes outlet valve, opens backwashing pump, clear liquid is through second check-valve, then passes through the two or three
Siphunculus enters in filter chamber from exhalant canal, cooperation backwash effect by filter chamber filter cloth and filter plate clean, to attached
The body refuse separation in filter cloth and filter chamber, by inlet discharge, body refuse is discharged into the body refuse in filter chamber by spoil disposal slag valve
In sludge-tank, achieve the effect that clean filter cloth and filter plate, so that the discharge of sewage restores normal in pipeline, after flushing, this hair
It is bright to continue back at filter process.The present invention has the function of continuous filtration, and combined filtering machine is filtered effect to sewage,
COD ss suspended solid content is effectively reduced, COD20% or more can be reduced, suspended matter is removed substantially.
2, the semicircular arc rhone in section is added on the filter plate of filter of the present invention, the radius in the section of rhone is
1~2mm, during the filtration process, body refuse are filtered in filter chamber, are intercepted outside rhone, and clear liquid enters in rhone, for
The direction of rhone is arranged, and is uniformly distributed on filter plate in " 1 " font or so, such clear liquid is just drained into out along rhone
In water hole, water outlet fluency can be improved, while improving exhalant canal water yield, avoid the body refuse on filter plate to the shadow of draining
It rings, improves filtering accuracy, COD ss suspended solid content is effectively reduced.
3, filter cloth uses two-layer fabric structure, and it is fine and closely woven to have an interlacing point, and intensity is high, strong to fine particle capturing ability,
Stripping performance is good, acidproof, alkaline-resisting feature.
4, the inlet of filter of the present invention is set to the lower portion of filter plate, and sewage enters in filter chamber from inlet, passes through
The conversion of valve, inlet can be not only used for feed liquor, and can be used for deslagging.
Detailed description of the invention
The present invention will be further explained below with reference to the attached drawings:
Fig. 1 is a kind of structural schematic diagram for the sewage-treatment plant that COD ss suspended solid is effectively reduced of the present invention;
Fig. 2 is the structural schematic diagram of sewage disposal process of the present invention;
Fig. 3 is the structural schematic diagram of filter plate in the present invention;
Fig. 4 is the structural schematic diagram of A-A in Fig. 3;
Fig. 5 be Fig. 3 in C to structural schematic diagram;
Fig. 6 is the structure enlargement diagram in Fig. 4 at Z.
Specific embodiment
It as shown in Figures 1 to 6, is a kind of sewage-treatment plant that COD ss suspended solid is effectively reduced of the present invention, including filtering
Machine 1, hydraulic workstation 2, electric cabinet 3, cesspool 4, sludge-tank 5 and clean solution tank 6, hydraulic workstation 2 are the energy supply of filter 1, electricity
Control case 3 be equipped with power on light, pressure maintaining indicator light, allow backhaul indicator light, compress button, backhaul button, pulling plate button and
Scram button, 3 pairs of electric cabinet whole sewage-treatment plants carry out control and display working condition.Filter 1 is equipped with thrust plate 7
With pressure plate 8, it is equipped with filter plate 9 and filter cloth 10 between thrust plate 7 and pressure plate 8, forms filter chamber between filter plate 9, filter cloth 10 is set to
In filter chamber, filter plate 9 is equipped with inlet 11, apopore 28 and exhalant canal 12, and inlet 11 is set to the lower half portion of filter plate 9,
Sewage enters in filter chamber from inlet 11, and by the conversion of valve, inlet 11 can be not only used for feed liquor, and can be used for deslagging.Increase
Add filter plate 9 to the filter area of body refuse in sewage, improves filtration.Filter plate 9 is equipped with rhone 27, and rhone 27 is in " 1 "
Font or so is uniformly distributed on filter plate 9, improves water outlet fluency.The section of rhone 27 is semicircular arc, rhone 27
The radius in section is 1~2mm, and body refuse is intercepted at outside rhone 27, and filtrate is drained into exhalant canal 12 along rhone 27,
It can be improved water yield, while improving water outlet fluency.For technical requirements, the boss on filter plate 9 is not allow for scar and change
Shape, two sealing surface thickness deviation dimensional discrepancy ± 0.5mm, thickness difference≤0.4mm of two sealing surfaces.Filter cloth 10 uses two-layer fabric
Structure, it is fine and closely woven to have an interlacing point, and intensity is high, and strong to fine particle capturing ability, stripping performance is good, acidproof, alkaline-resisting feature.
Filter 1 is equipped with oil cylinder seat 13, and oil cylinder seat 13 is equipped with oil cylinder 14, and oil cylinder 14 connects pressure plate 8.Filter 1 is equipped with cross
Beam 15, crossbeam 15 are equipped with drawing-plate mechanism 16.Inlet 11 is connect with cesspool 4, and the is equipped between inlet 11 and cesspool 4
One tee tube 17, the first tee tube 17 connect sludge-tank 5, and cesspool 4 is connected with feed pump 22, and feed pump 22 connects the first threeway
Sewage in cesspool 4 is pumped into the first tee tube 17 by pipe 17, feed pump 22, between feed pump 22 and the first tee tube 17
Equipped with first check-valve 23, first check-valve 23 controls the fill process of feed pump 22.Between first tee tube 17 and sludge-tank 5
Equipped with spoil disposal slag valve 18.Third tee tube 25 is equipped between first tee tube 17 and inlet 11, third tee tube 25 connects
There is feed pressure table 26, feed pressure table 26 shows that feed pump 22 is pumped into the flow of sewage in pipeline.Exhalant canal 12 is equipped with
Second tee tube 19, one end of the second tee tube 19 are connected with backwashing pump 20, and backwashing pump 20 connects clean solution tank the 6, the 2nd 3
Second check-valve 24 is equipped between siphunculus 19 and backwashing pump 20, second check-valve 24 controls the backwashed of backwashing pump 20
Journey.The other end of second tee tube 19 is connected to clean solution tank 6, and outlet valve 21 is equipped between the second tee tube 19 and clean solution tank 6.
During the filtration process, under the action of drawing-plate mechanism 16, filter 1 loads upper filter plate 9 to the present invention, in oil cylinder 14
Under force effect, thrust plate 7 and pressure plate 8 compress filter plate 9, and filter chamber is formed between filter plate 9, and filter cloth 10 is clamped in filter chamber,
After completing the installation of filter 1, spoil disposal slag valve 18 is closed, opens outlet valve 21, the sewage in cesspool 4 passes through feed pump
22, first check-valve 23 and the first tee tube 17, from the filter chamber that inlet 11 flows to filter 1, the 9 pairs of dirts of filter cloth 10 and filter plate
Water is filtered, and clear liquid flows in apopore 28 along filter plate 9 and rhone 27, and clear liquid flows into exhalant canal from apopore 28 again
In 12, clear liquid reaches clean solution tank 6 from exhalant canal 12, and subsidence settling is in filter chamber, will be certainly when the discharge of sewage is reduced in pipeline
It is dynamic to close feed pump 22, spoil disposal slag valve 18 is opened, outlet valve 21 is closed, opens backwashing pump 20, clear liquid is through second check-valve
24, then by the second tee tube 19, entered in filter chamber from exhalant canal 12, cooperation backwash is acted on the filter cloth in filter chamber
10 and filter plate 9 cleaned, the body refuse that is attached on filter cloth 10 and filter plate 9 is separated, the body refuse in filter chamber passes through inlet 11
Discharge, body refuse are discharged into sludge-tank 5 by spoil disposal slag valve 18, achieve the effect that clean filter cloth 10 and filter plate 9, so that in pipeline
The discharge of sewage restores normal, and after flushing, the present invention continues back at filter process.The present invention has continuous filterer's work
Can, combined filtering machine is filtered effect to sewage, COD ss suspended solid content is effectively reduced, can reduce COD20% or more, hangs
Floating object is removed substantially.
The above is only specific embodiments of the present invention, but technical characteristic of the invention is not limited thereto.It is any with this hair
Based on bright, to solve essentially identical technical problem, essentially identical technical effect is realized, made simple change, etc.
With replacement or modification etc., all it is covered by among protection scope of the present invention.
Claims (5)
1. a kind of sewage-treatment plant that COD ss suspended solid is effectively reduced, including filter, hydraulic workstation, electric cabinet, sewage
Pond, sludge-tank and clean solution tank, it is characterised in that: the filter is equipped with thrust plate and pressure plate, the thrust plate and described
Filter plate and filter cloth are equipped between pressure plate, the filter plate is equipped with rhone, and the rhone is uniformly distributed in " 1 " font or so
In on the filter plate, the section of the rhone is semicircular arc, and the radius in the section of the rhone is 1~2mm, the filter
Filter chamber is formed between plate, the filter cloth is set in the filter chamber, and the filter plate is equipped with inlet, apopore and exhalant canal;
The filter is equipped with oil cylinder seat, and the oil cylinder seat is equipped with oil cylinder, and the oil cylinder connects the pressure plate;The filter
It is equipped with crossbeam, the crossbeam is equipped with drawing-plate mechanism;The inlet is connect with the cesspool, the inlet with it is described
The first tee tube is equipped between cesspool, first tee tube connects the sludge-tank, first tee tube and the dirt
Spoil disposal slag valve is equipped between mud sump, the cesspool is connected with feed pump, and the feed pump connects first tee tube, institute
Exhalant canal is stated equipped with the second tee tube, one end of second tee tube is connected with backwashing pump, second tee tube
Second check-valve is equipped between the backwashing pump, the second check-valve controls the backwash process of the backwashing pump,
The backwashing pump connects the clean solution tank, and the other end of second tee tube is connected to the clean solution tank, second threeway
Outlet valve is equipped between pipe and the clean solution tank.
2. a kind of sewage-treatment plant that COD ss suspended solid is effectively reduced according to claim 1, it is characterised in that: institute
It states and is equipped with first check-valve between feed pump and first tee tube, the first check-valve controls the charging of the feed pump
Process.
3. a kind of sewage-treatment plant that COD ss suspended solid is effectively reduced according to claim 1, it is characterised in that: institute
It states and is equipped with third tee tube between the first tee tube and the inlet, the third tee tube is connected with feed pressure table.
4. a kind of sewage-treatment plant that COD ss suspended solid is effectively reduced according to claim 1, it is characterised in that: institute
Filter cloth is stated using two-layer fabric structure.
5. a kind of sewage-treatment plant that COD ss suspended solid is effectively reduced according to claim 1, it is characterised in that: institute
State the lower half portion that inlet is set to the filter plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510590505.2A CN105169775B (en) | 2015-09-15 | 2015-09-15 | A kind of sewage-treatment plant that COD ss suspended solid is effectively reduced |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510590505.2A CN105169775B (en) | 2015-09-15 | 2015-09-15 | A kind of sewage-treatment plant that COD ss suspended solid is effectively reduced |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105169775A CN105169775A (en) | 2015-12-23 |
CN105169775B true CN105169775B (en) | 2019-06-28 |
Family
ID=54892494
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510590505.2A Expired - Fee Related CN105169775B (en) | 2015-09-15 | 2015-09-15 | A kind of sewage-treatment plant that COD ss suspended solid is effectively reduced |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105169775B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105727609A (en) * | 2016-04-13 | 2016-07-06 | 湖北合加环境设备有限公司 | Electroosmosis high-voltage sludge elastic squeezing filter plate, filter-press assembly and presser |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2706217Y (en) * | 2004-05-20 | 2005-06-29 | 周明远 | Suspension liquid material filter pressing drying dewatering equipment |
CN201171941Y (en) * | 2008-04-15 | 2008-12-31 | 顾宝炎 | Filter press cloth |
CN201823361U (en) * | 2010-10-19 | 2011-05-11 | 超彩钛白科技(安徽)有限公司 | Plate and frame type filter press capable of improving filter pressing effect |
CN204952387U (en) * | 2015-09-15 | 2016-01-13 | 浙江锦港纺织印染有限公司 | Effectively reduce COD suspended solid SS's sewage treatment plant |
-
2015
- 2015-09-15 CN CN201510590505.2A patent/CN105169775B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2706217Y (en) * | 2004-05-20 | 2005-06-29 | 周明远 | Suspension liquid material filter pressing drying dewatering equipment |
CN201171941Y (en) * | 2008-04-15 | 2008-12-31 | 顾宝炎 | Filter press cloth |
CN201823361U (en) * | 2010-10-19 | 2011-05-11 | 超彩钛白科技(安徽)有限公司 | Plate and frame type filter press capable of improving filter pressing effect |
CN204952387U (en) * | 2015-09-15 | 2016-01-13 | 浙江锦港纺织印染有限公司 | Effectively reduce COD suspended solid SS's sewage treatment plant |
Also Published As
Publication number | Publication date |
---|---|
CN105169775A (en) | 2015-12-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201002003Y (en) | Membrane filter | |
CN101333055B (en) | Complete plant for treating and recovering printing light polluted waste liquid | |
CN101113042A (en) | Novel integral sewage water purifier | |
CN109264922A (en) | A kind of device and method of natural feather waste water recycling device | |
CN204798987U (en) | Novel water treatment pond | |
CN204952387U (en) | Effectively reduce COD suspended solid SS's sewage treatment plant | |
CN105169775B (en) | A kind of sewage-treatment plant that COD ss suspended solid is effectively reduced | |
CN104208941A (en) | Fiber rotary disk filtration tank | |
CN102847351A (en) | Novel quartz sand filter | |
CN104973711A (en) | Sewage impurity separation method | |
CN111762904A (en) | High-efficiency cyclone multistage purification device for mine wastewater treatment | |
CN206635150U (en) | A kind of industrial wastewater pollution processing unit | |
CN206466978U (en) | A kind of floor filter of three Room four with backwashing function | |
CN210855585U (en) | High-recovery-rate seawater desalination pretreatment device | |
CN204952394U (en) | Be equipped with sewage treatment system of filter | |
CN203043687U (en) | Floc self-filtering device for sewage treatment | |
CN207619098U (en) | A kind of Air flotation biological filter tank | |
CN204952442U (en) | A filter plate for filter | |
CN106007085A (en) | Textile wastewater processing device | |
CN206279057U (en) | A kind of reservoir aquaculture wastewater processing unit | |
CN214735232U (en) | Printing and dyeing wastewater treatment system | |
CN2247656Y (en) | Undershaft water purifier for coal mine | |
CN219885845U (en) | Device for treating powder spraying wastewater | |
CN211864073U (en) | White water filter | |
CN106807127A (en) | A kind of sewage-treatment plant |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
CB02 | Change of applicant information | ||
CB02 | Change of applicant information |
Address after: 312400 Chengbei District, Shengzhou Economic Development Zone, Shaoxing City, Zhejiang Province Applicant after: Zhejiang Jingang Textile Co., Ltd. Address before: 312400 Chengbei District, Shengzhou Economic Development Zone, Shaoxing City, Zhejiang Province Applicant before: ZHEJIANG JINGANG TEXTILE PRINTING AND DYEING CO., LTD. |
|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190628 Termination date: 20200915 |