CN207046927U - A kind of flocculation passage of papermaking sewage treatment system - Google Patents

A kind of flocculation passage of papermaking sewage treatment system Download PDF

Info

Publication number
CN207046927U
CN207046927U CN201721000684.0U CN201721000684U CN207046927U CN 207046927 U CN207046927 U CN 207046927U CN 201721000684 U CN201721000684 U CN 201721000684U CN 207046927 U CN207046927 U CN 207046927U
Authority
CN
China
Prior art keywords
pipe
increaser
negative pressure
reducing
reducing pipe
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
Application number
CN201721000684.0U
Other languages
Chinese (zh)
Inventor
石晓斌
高荣
高文松
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU FENGCHENG PAPER Co Ltd
Original Assignee
JIANGSU FENGCHENG PAPER Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by JIANGSU FENGCHENG PAPER Co Ltd filed Critical JIANGSU FENGCHENG PAPER Co Ltd
Priority to CN201721000684.0U priority Critical patent/CN207046927U/en
Application granted granted Critical
Publication of CN207046927U publication Critical patent/CN207046927U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of flocculation passage of papermaking sewage treatment system, including the water inlet pipe for connecting setting pot and the outlet pipe for connecting settling tank, and the chemical feed pipe of connection flocculant case, it is connected with the first reducing pipe, the first increaser, negative pressure chamber, the second reducing pipe and the second increaser between the water inlet pipe and outlet pipe in turn, the second reducing pipe butt end is arranged at immediately ahead of the first increaser butt end, and second the butt diameter of reducing pipe be more than the first increaser butt diameter, the chemical feed pipe connects negative pressure chamber.According to Venturi effect, sewage is during through the first reducing pipe, the first increaser, negative pressure chamber, the second reducing pipe, the second increaser, negative pressure can be formed in negative pressure chamber, flocculant be drawn from flocculant case by chemical feed pipe, the flow velocity of sewage is faster, negative pressure value is higher, the flow velocity of flocculant is faster, and the automatic change in flow for adapting to sewage, promptness, accuracy are good, and be the mechanical structure of no abrasion, cost is low, fault rate is low.

Description

A kind of flocculation passage of papermaking sewage treatment system
Technical field
It the utility model is related to papermaking sewage treatment system field, and in particular to a kind of flocculation of papermaking sewage treatment system Passage.
Background technology
The manufacturing process of corrugated paper includes to be re-fed into paper machine as waste carton crushing, the slurrying of raw material and paper is made, Substantial amounts of sewage can be produced in the fabrication process, it is necessary to could be discharged or be reused after being handled;The passage that flocculates is papermaking An important step in sewage disposal system, its effect is to mix sewage with flocculant, so as to by the nuisance in sewage Matter is separated;Existing flocculation passage is generally directly to connect Sheng by chemical feed pipe with the pipeline of settling tank in connection setting pot The container of flocculant is put, the natural flowing of flocculant is realized by chemical feed pipe both ends difference in height, or conveyed by pump;Sewage Composition it is substantially stationary, also generally fixed with the adding proportion of flocculant, existing flocculation passage is sent out in the flow velocity of sewage Can only adjust flocculant flow velocity by changing the aperture of valve on chemical feed pipe during changing, the promptness of manual modulation valve door and Accuracy is all very poor, realizes that the cost for automatically adjusting valve is high by sensor to detect sewage and flocculant flow velocity, and adopt Electronic device is more, fault rate is higher.
The content of the invention
The technical problems to be solved in the utility model is to provide a kind of flocculation passage of papermaking sewage treatment system, can solve Certainly existing flocculation passage adjusts flocculant flow velocity by changing valve opening, and the promptness and accuracy of manual modulation valve door are all Very poor, cost height, the fault rate for automatically adjusting valve are higher.
The utility model is achieved through the following technical solutions:
A kind of flocculation passage of papermaking sewage treatment system, including connection setting pot water inlet pipe with connect going out for settling tank Water pipe, and the chemical feed pipe of connection flocculant case, the first reducing pipe, first are connected with turn between the water inlet pipe and outlet pipe Increaser, negative pressure chamber, the second reducing pipe and the second increaser, the second reducing pipe butt end are being arranged at the first increaser butt end just Front, and the butt diameter of the second reducing pipe is more than the first increaser butt diameter, the chemical feed pipe connects negative pressure chamber.
Further scheme of the present utility model is to be also provided at mixing between second reducing pipe and the second increaser Pipe.
Further scheme of the present utility model is that first reducing pipe, the first increaser, the second reducing pipe and second are gradually Expander is coaxially disposed in housing.
Further scheme of the present utility model is to be provided with valve on the chemical feed pipe.
The utility model compared with prior art the advantages of be:
First, according to Venturi effect, sewage through the first reducing pipe, the first increaser, negative pressure chamber, the second reducing pipe, During second increaser, negative pressure can be formed in negative pressure chamber, flocculant is drawn from flocculant case by chemical feed pipe, sewage Flow velocity is faster, and negative pressure value is higher, and the flow velocity of flocculant is faster, and the automatic change in flow for adapting to sewage, promptness, accuracy are good, And be the mechanical structure of no abrasion, cost is low, fault rate is low;
2nd, mixing tube extends the incorporation time of flocculant and sewage, strengthens mixed effect;
3rd, housing is realized to the first reducing pipe, the first increaser, the second reducing pipe and the second increaser and protected, it is ensured that is made Use the life-span.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
A kind of flocculation passage of papermaking sewage treatment system as shown in Figure 1, including connect the water inlet pipe 1 of setting pot and connect The outlet pipe 2 of logical settling tank, and the chemical feed pipe 4 of flocculant case 3 is connected, valve 5 is provided with the chemical feed pipe 4, in addition to The first connected reducing pipe 6 of coaxial order, the first increaser 7, negative pressure chamber 11, the second reducing pipe 8, mixing tube 9 in housing 12 With the second increaser 10, the butt end of the second reducing pipe 8 is arranged at immediately ahead of the butt end of the first increaser 7, and the second reducing pipe 8 Butt diameter is more than the butt diameter of the first increaser 7, and the water inlet pipe 1 connects the butt end of the first reducing pipe 6, and the outlet pipe 2 connects The logical butt end of second increaser 10, the chemical feed pipe 4 connect negative pressure chamber 11.

Claims (4)

1. a kind of flocculation passage of papermaking sewage treatment system, include the water inlet pipe of connection setting pot(1)With connect settling tank Outlet pipe(2), and connection flocculant case(3)Chemical feed pipe(4), it is characterised in that:The water inlet pipe(1)With outlet pipe(2) Between be connected with the first reducing pipe in turn(6), the first increaser(7), negative pressure chamber(11), the second reducing pipe(8)With the second flaring Pipe(10), second reducing pipe(8)Butt end is arranged at the first increaser(7)Immediately ahead of butt end, and the second reducing pipe(8)It is thick End diameter is more than the first increaser(7)Butt diameter, the chemical feed pipe(4)Connect negative pressure chamber(11).
A kind of 2. flocculation passage of papermaking sewage treatment system as claimed in claim 1, it is characterised in that:Described second is tapered Pipe(8)With the second increaser(10)Between be also provided at mixing tube(9).
A kind of 3. flocculation passage of papermaking sewage treatment system as claimed in claim 1, it is characterised in that:Described first is tapered Pipe(6), the first increaser(7), the second reducing pipe(8)With the second increaser(10)It is coaxially disposed in housing(12)In.
A kind of 4. flocculation passage of papermaking sewage treatment system as claimed in claim 1, it is characterised in that:The chemical feed pipe (4)On be provided with valve(5).
CN201721000684.0U 2017-08-11 2017-08-11 A kind of flocculation passage of papermaking sewage treatment system Expired - Fee Related CN207046927U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721000684.0U CN207046927U (en) 2017-08-11 2017-08-11 A kind of flocculation passage of papermaking sewage treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721000684.0U CN207046927U (en) 2017-08-11 2017-08-11 A kind of flocculation passage of papermaking sewage treatment system

Publications (1)

Publication Number Publication Date
CN207046927U true CN207046927U (en) 2018-02-27

Family

ID=61499612

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721000684.0U Expired - Fee Related CN207046927U (en) 2017-08-11 2017-08-11 A kind of flocculation passage of papermaking sewage treatment system

Country Status (1)

Country Link
CN (1) CN207046927U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108408861A (en) * 2018-05-03 2018-08-17 东华大学 A kind of multistage flco amplification mixing-reaction-sedimentation integrated device and technique
CN114409037A (en) * 2021-12-24 2022-04-29 河北省水文工程地质勘查院(河北省遥感中心、河北省地矿局科技信息中心) Saline-alkali soil saline-alkali water large-scale utilization system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108408861A (en) * 2018-05-03 2018-08-17 东华大学 A kind of multistage flco amplification mixing-reaction-sedimentation integrated device and technique
CN114409037A (en) * 2021-12-24 2022-04-29 河北省水文工程地质勘查院(河北省遥感中心、河北省地矿局科技信息中心) Saline-alkali soil saline-alkali water large-scale utilization system

Similar Documents

Publication Publication Date Title
CN206328202U (en) Ultra micro nano-bubble generator
CN207046927U (en) A kind of flocculation passage of papermaking sewage treatment system
CN103406049A (en) Powdered activated carbon charging method and powdered activated carbon charging device
CN209985343U (en) Guar gum auxiliary agent preparation is with throwing device
CN103790059A (en) Device and method for medium-concentration beating fed through medium-concentration pulp pump
CN203715985U (en) Medium-underflow pulping device adopting medium-underflow pump to charge
CN202705198U (en) Micropollution drinking water treatment device
CN205182267U (en) Defoamer
CN101254426B (en) Anti-splash device of conical dissolvers
CN205095471U (en) Flocculation and sedimentation tank
CN208787107U (en) A kind of easily blocking pipeline flushing device
CN202415337U (en) Pressurization treatment device for deodorizing and reducing sludge by electrolytic ozone
CN206853213U (en) Printing ink wastewater treatment device
CN113969230A (en) Sand and scum removing and breaking device for anaerobic fermentation tank and sand and scum removing and breaking method
CN219558812U (en) Kitchen garbage thick liquid sand removal device
CN205730488U (en) Flocculation sediment waterworks
CN206666208U (en) PH value governor motion is used in a kind of water boron removal processing
CN206173018U (en) Physics steady voltage dissolved air releaser
CN207726794U (en) A kind of chemicals dosing plant for sewage disposal system
CN205575812U (en) Starch maize effluent treatment plant
CN105755882B (en) Paper machine broke treatment pond
CN111075729A (en) Vertical self-priming pump
CN205412356U (en) Liquid eduction gear of sedimentation tank
CN204661367U (en) Corn starch wastewater extracts phi protein
CN109896669A (en) Mixed flocculation air bearing all-in-one machine

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180227

Termination date: 20190811

CF01 Termination of patent right due to non-payment of annual fee