CN201686601U - Sludge stirring pot - Google Patents
Sludge stirring pot Download PDFInfo
- Publication number
- CN201686601U CN201686601U CN201020182442XU CN201020182442U CN201686601U CN 201686601 U CN201686601 U CN 201686601U CN 201020182442X U CN201020182442X U CN 201020182442XU CN 201020182442 U CN201020182442 U CN 201020182442U CN 201686601 U CN201686601 U CN 201686601U
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- Prior art keywords
- oil
- sludge
- central reactor
- tank body
- reactor
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Abstract
The utility model discloses a sludge stirring pot, which comprises a pot body, a center reactor, an oil collecting ring, a motor and a stirring paddle, wherein the motor is arranged at the top of pot body, an output shaft of the motor extends to the bottom portion in the pot body, the pot body is coaxially provided with a fixing type center reactor, a pipe port of a sludge conveying pipe is levelly and inclinedly inserted on the upper portion of the center reactor on the oblique direction, the hollow oil collection ring is arranged on the top end of the center reactor and is communicated with the inner portion of the center reactor, the oil collection ring is connected with an oil collection pipe to output collected light oil outside the pot body, and the stirring paddle is arranged on the bottom end of the output shaft of the motor. The sludge stirring pot has simple structure, simple and convenient operation, small volume, high automatic degree, less maintenance workload, convenient management, low energy consumption, and low operating cost.
Description
Technical field
The utility model relates to a kind of environmental protection equipment, specifically is a kind of sludge agitator tank, and it is visual plant in the dewatering technology of mud, and effect is that oil, oil-containing, sewage containing methanol mud that gas field development produced are stirred, for the operation of back creates conditions.
Background technology
At present, at oil, oil-containing that gas field development produced, contain in the pure sewage of low concentration mud, also there is not equipment from sludge water, mud to be separated.Be originally that the oil-containing that produces, sewage containing methanol mud are moved sludge sump to car in oil recovery, gas and oily(waste)water concentration technology, sewage mud in the sludge sump is by sun natural drying, water, methyl alcohol and condensate oil in the evaporation mud behind the evaporation airing, are transported mud the postpone burning or are buried ground with car again.This processing mode is contaminate environment not only, and processing efficiency is low, and methyl alcohol and condensate oil can not be recycled.
For this reason, the applicant has proposed a kind of novel method for sludge treatment, at first sewage mud is added coagulating agent and mix stirring, make medicament and sewage mud obtain the thorough mixing reaction, enter afterwards in the reactor and react with organic floculant, by forcing machine sewage mud is carried out solid-liquid separation at last, the solid outward transport is handled or is burned, and the oil of separating, water, methyl alcohol etc. enter oily water separation and extraction system is extracted.Wherein sewage mud adding coagulating agent being mixed stirring is committed step of present method, require the dosing of mixed sewage mud even, on the basis that meets the demands, must try one's best to reduce and add dose to save cost, simultaneously owing to solids in the sewage mud is more, and liquid state is constantly evaporated, must guarantee that the sewage mud after the dosing does not harden, can not meet the demands so tie enough stirrers usually.
The utility model content
Technical problem to be solved in the utility model provides a kind of dosing and sewage mud of making and mixes, and the sewage mud after the dosing does not produce the sludge agitator tank that hardens.
A kind of sludge agitator tank described in the utility model, it comprises tank body, central reactor, oil collecting ring, electric motor, stirring rake, described electric motor mounting is at the tank body top, the output shaft of electric motor extends to the tank body inner bottom part always, the coaxial central reactor that installs and fixes formula in tank body, the mouth of pipe of sludge carrier pipe is the oblique insertion central reactor of level top, the oil collecting ring of hollow be located at the central reactor top and with the central reactor internal communication, oil collecting ring is connected to oil header with the light oil output tank body of collecting; Stirring rake is installed in the motor output shaft bottom.
As improvement of the present utility model, central reactor is the stepped circular cone bench-type of thin-walled hollow at last, by some vertical grids water eliminator is installed in the central reactor bottom.
As further improvement of the utility model, stirring rake is preferably cross V-type stirring rake.
The beneficial effects of the utility model:
1, it is simple in structure, easy and simple to handle, and volume is little, automatic degree height, and maintenance workload is few, convenient management, energy consumption is low, and running cost is few.
2, the design by spout, make sewage mud horizontal plane with the off-centered oblique reaction chamber that sprays in the central reactor in, water inlet adds coagulating agent by chemicals dosing plant simultaneously, make medicament and water inlet obtain thorough mixing, sewage mud rotates into central reactor from top, in the reaction chamber of central reactor, be the eddy flow state to prolong current through line, guarantee the reaction times.
3, oil slick is drained the oil automatically by oil collecting ring in oil droplet and the water, recycles.
4, cross V-type stirring rake is set, rotating speed 3~5r/min turns on the contrary with the spirrillum water (flow) direction, and it is more even that sewage mud is stirred, and mixes more thorough.
Description of drawings
Fig. 1 is a structure iron of the present utility model.
Fig. 2 is that Figure 1A-A is to sectional view.
Embodiment
As Fig. 1, sludge agitator tank mainly is made up of tank body, central reactor 1, oil collecting ring 2, electric motor 3, stirring rake 5, wherein:
Concentration is squeezed into sludge agitator tank at the lower concentration oily(waste)water mud of 2000mg/L~60000mg/L by first sludge pump 9, design by spout, make sewage mud horizontal plane with the off-centered oblique reaction chamber 4 that sprays in the central reactor 1 in, water inlet begins to add coagulating agent by chemicals dosing plant simultaneously, make medicament and water inlet obtain filling a part hybrid reaction, sewage mud rotates into central reactor 1 from top, in the reaction chamber 4 of central reactor 1, be the eddy flow state to prolong current through line, guarantee the reaction times, the little oil droplet of dispersive passes through breakdown of emulsion in the water, contact-impact becomes big oil droplet, under buoyancy and sluicing, particle diameter become big oil droplet and water in oil slick be easy to be floated to the import top and form oil reservoir, the most oil slick that is gathered in the central reactor top is drained the oil automatically by oil collecting ring 2.The current spirrillum enters the negative area, bottom, fall and flow in the tank body again on grade water plate 8, directly do not wash away the mud of sludge agitator tank bottom by shelves water plate 8, solidliquid mixture in the equipment is laminar flow regime, be beneficial to the settlement separate of silt particle, in order not make sludge settling solid, the utility model is provided with cross V-type stirring rake, rotating speed 3~5r/min turns on the contrary with the spirrillum water (flow) direction, and it is more even that sewage mud is stirred, mix more thorough, treat to open motorized valve 6 automatically behind the even 10~15min of sludge water stirrer, open second sludge pump 10 of sludge agitator tank bottom in the time of opening of valves, the sewage mud that stirs is discharged.
Claims (4)
1. sludge agitator tank, it is characterized in that comprising tank body, central reactor (1), oil collecting ring (2), electric motor (3), stirring rake (5), described electric motor (3) is installed in the tank body top, the output shaft of electric motor (3) extends to the tank body inner bottom part always, the coaxial central reactor (1) that installs and fixes formula in tank body, the mouth of pipe of sludge carrier pipe is the oblique insertion central reactor of level (1) top, the oil collecting ring of hollow (2) be located at the central reactor top and with the central reactor internal communication, oil collecting ring (2) is connected to oil header with the light oil output tank body of collecting; Stirring rake (5) is installed in the motor output shaft bottom.
2. sludge agitator tank according to claim 1 is characterized in that described central reactor (1) is the stepped circular cone bench-type of thin-walled hollow.
3. sludge agitator tank according to claim 1 and 2 is characterized in that by some vertical grids (7) water eliminator (8) being installed in the central reactor bottom.
4. sludge agitator tank according to claim 1 and 2 is characterized in that described stirring rake (5) is a cross V-type stirring rake.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020182442XU CN201686601U (en) | 2010-05-07 | 2010-05-07 | Sludge stirring pot |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020182442XU CN201686601U (en) | 2010-05-07 | 2010-05-07 | Sludge stirring pot |
Publications (1)
Publication Number | Publication Date |
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CN201686601U true CN201686601U (en) | 2010-12-29 |
Family
ID=43374887
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201020182442XU Expired - Fee Related CN201686601U (en) | 2010-05-07 | 2010-05-07 | Sludge stirring pot |
Country Status (1)
Country | Link |
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CN (1) | CN201686601U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102173489A (en) * | 2011-03-02 | 2011-09-07 | 苏州顶裕节能设备有限公司 | Mixing reactor for water treatment |
CN102990523A (en) * | 2012-12-13 | 2013-03-27 | 孙树峰 | Abrasive particle stream flowing type polishing device based on tool orientation |
CN104667852A (en) * | 2013-11-27 | 2015-06-03 | 大连隆星新材料有限公司 | Paraffin wax stirring reaction device |
-
2010
- 2010-05-07 CN CN201020182442XU patent/CN201686601U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102173489A (en) * | 2011-03-02 | 2011-09-07 | 苏州顶裕节能设备有限公司 | Mixing reactor for water treatment |
CN102990523A (en) * | 2012-12-13 | 2013-03-27 | 孙树峰 | Abrasive particle stream flowing type polishing device based on tool orientation |
CN104667852A (en) * | 2013-11-27 | 2015-06-03 | 大连隆星新材料有限公司 | Paraffin wax stirring reaction device |
CN104667852B (en) * | 2013-11-27 | 2017-12-08 | 大连隆星新材料有限公司 | paraffin stirring reaction device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101229 Termination date: 20110507 |