CN206500145U - A kind of organic silicon slurry slag neutralizing hydrolysis processing unit - Google Patents
A kind of organic silicon slurry slag neutralizing hydrolysis processing unit Download PDFInfo
- Publication number
- CN206500145U CN206500145U CN201720201070.2U CN201720201070U CN206500145U CN 206500145 U CN206500145 U CN 206500145U CN 201720201070 U CN201720201070 U CN 201720201070U CN 206500145 U CN206500145 U CN 206500145U
- Authority
- CN
- China
- Prior art keywords
- treatment device
- reaction treatment
- organic silicon
- slurry slag
- silicon slurry
- 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
Abstract
The utility model discloses a kind of organic silicon slurry slag neutralizing hydrolysis processing unit, including reaction treatment device, support frame, effluent trough, stirring motor, high-pressure hydraulic pump, diaphragm air pump, aeration pump, grid plate, refrigerator and condenser jacket, support frame is provided with above the reaction treatment device, the reaction treatment device bottom is connected with above effluent trough, support frame as described above and is provided with stirring motor and diaphragm air pump.The utility model high-pressure hydraulic pump is squeezed into buck in reaction treatment device with certain speed by buck input pipe, while being squeezed into organic silicon slurry slag in reaction treatment device with certain speed by machine silicon screenings input pipe with diaphragm air pump；Buck enters in reaction treatment device with organic silicon slurry slag to be reacted, and reaction, which is finished, is brought organic silicon slurry slag hydrolysate in effluent trough into by buck, and the water conservancy for reacting incomplete organic silicon slurry slag with reaction generation is separated with grid plate.
Description
Technical field
The utility model is related to a kind of organic silicon slurry slag neutralizing hydrolysis processing unit.
Background technology
The screenings produced in organic silicon monomer building-up process, i.e. organic silicon slurry slag, are that a kind of liquid with mobility is mixed admittedly
Compound, wherein high-boiling components are inflammable and explosive, have certain volatility, belong to hazardous waste, and severe contamination is caused to environment, therefore will
Harmless treatment is done to organic silicon slurry slag.
The processing of current organic silicon slurry slag, using upper, also have many deficiencies and had much room for improvement mainly at it, such as water
Solution will increase waste disposal expense due to can also add material in hydrolytic process, and produce new pollution sources；Cracking
Have the disadvantage that all components can not be cracked, catalyst is expensive, and production cost is higher.
Disclosed in Chinese patent literature CN1618840《The processing method of waste residue slurry in organic silicon monomer building-up process》、
Disclosed in CN101659672A《A kind of method for cracking treatment of organic silicon waste residue slurry》And disclosed in CN102390860B《It is a kind of
The environment-friendly treatment method and device of organosilicon slag slurry》Etc. be required for using other materials processing, complex technical process, processing cost
Height, treatment effeciency is low, is also easy to produce other pollution sources, it is impossible to be truly realized harmless treatment.
Utility model content
To solve the above problems, the utility model provides a kind of organic silicon slurry slag neutralizing hydrolysis processing unit.
To achieve the above object, the technical scheme that the utility model is taken is：
A kind of organic silicon slurry slag neutralizing hydrolysis processing unit, is operated specific as follows：Including reaction treatment device, support frame, go out
On tank, stirring motor, high-pressure hydraulic pump, diaphragm air pump, aeration pump, grid plate, refrigerator and condenser jacket, the reaction treatment device
Side is provided with support frame, and the reaction treatment device bottom, which is connected with above effluent trough, support frame as described above, is provided with stirring electricity
Machine and diaphragm air pump, the reaction treatment device are internally provided with the puddler being connected with stirring motor, the puddler and set
There is setting organic silicon slurry slag input pipe on paddle, the diaphragm air pump, the organic silicon slurry slag input pipe is extended at reaction
Manage to be provided with high-pressure hydraulic pump, the high-pressure hydraulic pump on the inside of device, the both sides of support frame as described above and be provided with buck input pipe, institute
State and be provided with condenser jacket and refrigeration on the inside that buck input pipe extends to reaction treatment device, the outer wall of the reaction treatment device
Device, the refrigerator is connected with the condenser pipe being arranged on inside condenser jacket, and exposure is provided with the reaction treatment device bottom end side wall
Air pump, the reaction treatment device bottom sets grid plate with effluent trough junction.
Preferably, being provided with outlet valve below the effluent trough.
Preferably, the aeration pump is connected with being arranged on the aeration tube of reaction treatment device inner bottom part.
Preferably, being provided with controller, the stirring motor, high-pressure hydraulic pump, barrier film on the reaction treatment device back side
Air pump, aeration pump and refrigerator are connected with controller respectively by signal wire.
The utility model is simple in construction, easy to operate, and stirring motor, barrier film are set by support frame above reaction treatment device
Air pump and high-pressure hydraulic pump；Stirring motor is stirred operation by puddler inside reaction treatment device, and high-pressure hydraulic pump passes through alkali
Water inlet pipe squeezes into buck in reaction treatment device with certain speed, while will by machine silicon screenings input pipe with diaphragm air pump
Organic silicon slurry slag is squeezed into reaction treatment device with certain speed；Buck enters in reaction treatment device with organic silicon slurry slag to react,
Reaction, which is finished, is brought organic silicon slurry slag hydrolysate in effluent trough into by buck, reacts incomplete organic silicon slurry slag and reaction is given birth to
Into water conservancy separated with grid plate after；Treatment effeciency is high, and processing is thorough, and effect is good, and cost is low, reduces in organic silicon slurry slag and water
Solve processing cost, it is easy to subsequent treatment, can organic silicon slurry slag on a large scale.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the accompanying drawing used required in description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, is not paying the premise of creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings；
Fig. 1 is structural representation of the present utility model.
Embodiment
Preferred embodiment of the present utility model is described in detail below in conjunction with the accompanying drawings, so that advantage of the present utility model
It can be easier to be readily appreciated by one skilled in the art with feature, so as to make protection domain of the present utility model apparent clear and definite
Define.
As shown in figure 1, a kind of organic silicon slurry slag neutralizing hydrolysis processing unit of the utility model includes reaction treatment device 1, branch
Support 2, effluent trough 3, stirring motor 4, high-pressure hydraulic pump 5, diaphragm air pump 7, aeration pump 9, grid plate 10, refrigerator 11 and condenser jacket
12, the top of reaction treatment device 1 is provided with support frame 2, and the bottom of reaction treatment device 1 is connected with effluent trough 3, described
The top of support frame 2 is provided with stirring motor 4 and diaphragm air pump 7, and the reaction treatment device 1 is internally provided with and the phase of stirring motor 4
Setting organic silicon slurry slag input pipe on paddle 42, the diaphragm air pump 7 is provided with puddler 41 even, the puddler 41
8, the organic silicon slurry slag input pipe 8 extends on the inside of reaction treatment device 1, the both sides of support frame as described above 2 and is provided with high pressure
Buck input pipe 6 is provided with water pump 5, the high-pressure hydraulic pump 5, the buck input pipe 6 extends to the interior of reaction treatment device 1
Condenser jacket 12 and refrigerator 11 are provided with portion, the outer wall of the reaction treatment device 1, the refrigerator 11 is with being arranged on condenser jacket
Condenser pipe inside 12 is connected, and aeration pump 9, the bottom of reaction treatment device 1 are provided with the bottom end side wall of reaction treatment device 1
Grid plate 10 is set with the junction of effluent trough 3.
It is worth noting that, the lower section of effluent trough 3 is provided with outlet valve 13.
It is worth noting that, the aeration pump 9 is connected with being arranged on the aeration tube of the inner bottom part of reaction treatment device 1.
It is worth noting that, being provided with controller, the stirring motor 4, high-pressure hydraulic pump on the back side of reaction treatment device 1
5th, diaphragm air pump 7, aeration pump 9 and refrigerator 11 are connected with controller respectively by signal wire.
The utility model is simple in construction, easy to operate, and stirring motor, barrier film are set by support frame above reaction treatment device
Air pump and high-pressure hydraulic pump；Stirring motor is stirred operation by puddler inside reaction treatment device, and high-pressure hydraulic pump passes through alkali
Water inlet pipe squeezes into buck in reaction treatment device with certain speed, while will by machine silicon screenings input pipe with diaphragm air pump
Organic silicon slurry slag is squeezed into reaction treatment device with certain speed；Buck enters in reaction treatment device with organic silicon slurry slag to react,
Reaction, which is finished, is brought organic silicon slurry slag hydrolysate in effluent trough into by buck, reacts incomplete organic silicon slurry slag and reaction is given birth to
Into water conservancy separated with grid plate after；Treatment effeciency is high, and processing is thorough, and effect is good, and cost is low, reduces in organic silicon slurry slag and water
Solve processing cost, it is easy to subsequent treatment, can organic silicon slurry slag on a large scale.
The standardized element that the utility model is used can commercially, shaped piece according to specification and accompanying drawing
Record can carry out customized, the specific connected mode of each part is using bolt ripe in the prior art, rivet, weldering
The conventional meanses such as connect, machinery, part and equipment are using in the prior art, and conventional model adds circuit connection using existing
Conventional connected mode, will not be described in detail herein in technology.
Described above is only preferred embodiment of the present utility model, it is noted that for the common skill of the art
For art personnel, on the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these improve and
Retouching also should be regarded as protection domain of the present utility model.
Claims (4)
1. a kind of organic silicon slurry slag neutralizing hydrolysis processing unit, it is characterised in that：Including reaction treatment device (1), support frame (2),
Effluent trough (3), stirring motor (4), high-pressure hydraulic pump (5), diaphragm air pump (7), aeration pump (9), grid plate (10), refrigerator (11)
With condenser jacket (12), reaction treatment device (1) top is provided with support frame (2), and reaction treatment device (1) the bottom connection is set
It is equipped with above effluent trough (3), support frame as described above (2) and is provided with stirring motor (4) and diaphragm air pump (7), the reaction treatment device
(1) it is internally provided with the puddler (41) being connected with stirring motor (4), the puddler (41) and is provided with paddle (42),
Organic silicon slurry slag input pipe (8) is set on the diaphragm air pump (7), and the organic silicon slurry slag input pipe (8) is extended at reaction
Manage to be provided with high-pressure hydraulic pump (5), the high-pressure hydraulic pump (5) on the inside of device (1), the both sides of support frame as described above (2) and be provided with
Buck input pipe (6), the buck input pipe (6) extends to the inside of reaction treatment device (1), the reaction treatment device (1)
Condenser jacket (12) and refrigerator (11), the refrigerator (11) and the condensation for being arranged on condenser jacket (12) inside are provided with outer wall
Pipe is connected, and aeration pump (9), reaction treatment device (1) bottom and water outlet are provided with reaction treatment device (1) the bottom end side wall
Groove (3) junction sets grid plate (10).
2. a kind of organic silicon slurry slag neutralizing hydrolysis processing unit as claimed in claim 1, it is characterised in that：The effluent trough
(3) lower section is provided with outlet valve (13).
3. a kind of organic silicon slurry slag neutralizing hydrolysis processing unit as claimed in claim 1, it is characterised in that：The aeration pump
(9) it is connected with being arranged on the aeration tube of reaction treatment device (1) inner bottom part.
4. a kind of organic silicon slurry slag neutralizing hydrolysis processing unit as claimed in claim 1, it is characterised in that：The reaction treatment
Controller, the stirring motor (4), high-pressure hydraulic pump (5), diaphragm air pump (7), aeration pump (9) and system are provided with device (1) back side
Cooler (11) is connected with controller respectively by signal wire.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720201070.2U CN206500145U (en) | 2017-02-24 | 2017-02-24 | A kind of organic silicon slurry slag neutralizing hydrolysis processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720201070.2U CN206500145U (en) | 2017-02-24 | 2017-02-24 | A kind of organic silicon slurry slag neutralizing hydrolysis processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206500145U true CN206500145U (en) | 2017-09-19 |
Family
ID=59840511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720201070.2U Expired - Fee Related CN206500145U (en) | 2017-02-24 | 2017-02-24 | A kind of organic silicon slurry slag neutralizing hydrolysis processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206500145U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107937641A (en) * | 2017-11-23 | 2018-04-20 | 莫宝兰 | One kind refrigeration slag cooling device |
| CN109364860A (en) * | 2018-12-10 | 2019-02-22 | 徐春 | A kind of production process of trichlorosilane is mixed into agitating device at regular time and quantity |
-
2017
- 2017-02-24 CN CN201720201070.2U patent/CN206500145U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107937641A (en) * | 2017-11-23 | 2018-04-20 | 莫宝兰 | One kind refrigeration slag cooling device |
| CN109364860A (en) * | 2018-12-10 | 2019-02-22 | 徐春 | A kind of production process of trichlorosilane is mixed into agitating device at regular time and quantity |
| CN109364860B (en) * | 2018-12-10 | 2020-11-20 | 徐春 | Timing and quantitative mixing and stirring device in trichlorosilane production process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103523918B (en) | Air flow and machinery double-boosting internal circulation-type high suspension solid anaerobic digestion device | |
| CN206500145U (en) | A kind of organic silicon slurry slag neutralizing hydrolysis processing unit | |
| CN205528333U (en) | Sludge treatment system | |
| CN205295320U (en) | Mechanical stirring formula fermentation cylinder | |
| CN204768670U (en) | Water -reducing agent reation kettle | |
| CN207259283U (en) | A kind of retracting device of plant acidification oil hydrolysis sugar water | |
| CN205095708U (en) | Dedicated automatic mixer of sewage treatment | |
| CN216303845U (en) | Liquid anaerobic biogas fermentation experimental device | |
| CN209735590U (en) | Novel polyester resin polymerization cauldron | |
| CN205099556U (en) | CSBR sewage treatment pond | |
| CN210048521U (en) | Waste liquid recovery processing device that produces in 3-aminopropanol preparation process | |
| CN202606140U (en) | Waste heat recycling system for reaction kettle | |
| CN206837519U (en) | A kind of ammonia still process kettle | |
| CN202606053U (en) | Totally-closed static pipeline continuous precipitation system for rear earth precipitation and transformation | |
| CN207546449U (en) | A kind of plus pressure control power apparatus hydrothermal reaction kettle | |
| CN205953651U (en) | Fast anaerobic reactor of multistage unsteady flow | |
| CN208022940U (en) | A kind of device producing carbon black using tar slag | |
| CN205569873U (en) | Multistage siphon separator that hydrolysises of living beings | |
| CN208878589U (en) | Tween-80 synthesis reaction system | |
| CN204752569U (en) | Real standard teaching is with DOP cauldron formula reaction production facility | |
| CN208617561U (en) | A kind of silicon wafer Additive Production disposal unit | |
| CN209155792U (en) | A kind of waste liquid waste gas recovery reutilization system in PCO production process | |
| CN203382520U (en) | Environment-friendly polymeric aluminum chloride production system | |
| CN203474699U (en) | Rectification type esterification reaction system for polycarboxylate water reducer | |
| CN206843239U (en) | A kind of clothing factory effluent sewage recovery system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20170919 Termination date: 20180224 |