CN208320772U - The automated production equipment of silicone oil - Google Patents
The automated production equipment of silicone oil Download PDFInfo
- Publication number
- CN208320772U CN208320772U CN201820690033.7U CN201820690033U CN208320772U CN 208320772 U CN208320772 U CN 208320772U CN 201820690033 U CN201820690033 U CN 201820690033U CN 208320772 U CN208320772 U CN 208320772U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- cylinder
- reaction kettle
- bucket
- silicone oil
- 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
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- 229920002545 silicone oil Polymers 0.000 title claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 25
- 239000002994 raw material Substances 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000003860 storage Methods 0.000 claims abstract description 17
- 239000000110 cooling liquid Substances 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 13
- 239000002826 coolant Substances 0.000 claims abstract description 11
- 238000003756 stirring Methods 0.000 claims description 26
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000000047 product Substances 0.000 description 12
- 238000001816 cooling Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000010924 continuous production Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 241000270295 Serpentes Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
Landscapes
- Polymerisation Methods In General (AREA)
Abstract
The utility model discloses a kind of automated production equipments of silicone oil, including raw material storage tanks, raw material storage tanks are connected with water removal reaction kettle through pipeline, it removes water reaction kettle and is connected with agitating device through pipeline, agitating device is connected with polymerization reaction kettle through pipeline, polymerization reaction kettle is connected with heat exchanger through pipeline, and heat exchanger is connected with product storage tank through pipeline；The heat exchanger includes the cylinder arranged vertically, cylinder upper and lower ends are respectively equipped with inlet port and outlet port, the upper and lower ends of inner barrel are respectively equipped with the shunting bucket and afflux bucket being connected with inlet port and outlet port, shunt and are equipped with the more snakelike conveying pipelines arranged vertically between bucket and afflux bucket；Coolant liquid is also filled in the cylinder, the upper and lower ends of cylinder side are respectively equipped with cooling liquid outlet and cooling liquid inlet, the deflector of screw arrangement is additionally provided on the inner wall of cylinder.The utility model has the characteristics that can be improved production efficiency.
Description
Technical field
The utility model relates to a kind of silicone oil production equipment, especially a kind of automated production equipment of silicone oil.
Background technique
Silicone oil both can be used as the production that additive carries out chemical raw material, can also be used as lubricating oil and carries out using quilt
It is widely used in every field.Silicone oil needs mainly to include dehydration kettle, polymerize using to many equipment in process of production
Reaction kettle, the cooling composition such as reaction kettle and finished pot, but each equipment is all independently to be produced, and is needed manually to centre
Product is transported through, and cannot achieve continuous production process, so that serious reduce silicone oil production efficiency.Moreover, cooling reaction kettle
Cooling effect it is bad, influence production efficiency.Meanwhile existing device mainly passes through in reaction kettle the stirring of reaction solution
Rabbling mechanism carry out, not only stirring efficiency is low, but also mixing effect is also bad.Therefore, there is productions for existing technology
The problem of low efficiency.
Utility model content
The purpose of the utility model is to provide a kind of automated production equipments of silicone oil.The utility model has can
The characteristics of improving production efficiency.
The technical solution of the utility model includes: the automated production equipment of silicone oil, including raw material storage tanks, raw material storage tanks warp
Pipeline is connected with water removal reaction kettle, removes water reaction kettle through pipeline and is connected with agitating device, agitating device is connected with polymerization through pipeline
Reaction kettle, polymerization reaction kettle are connected with heat exchanger through pipeline, and heat exchanger is connected with product storage tank through pipeline；The heat exchanger packet
The cylinder arranged vertically is included, cylinder upper and lower ends are respectively equipped with inlet port and outlet port, and the upper and lower ends of inner barrel are set respectively
There are the shunting bucket and afflux bucket being connected with inlet port and outlet port, shunts and be equipped with the more snakes arranged vertically between bucket and afflux bucket
Shape conveying pipeline；Coolant liquid is also filled in the cylinder, the upper and lower ends of cylinder side are respectively equipped with cooling liquid outlet and cooling
Liquid import is additionally provided with the deflector of screw arrangement on the inner wall of cylinder.
In the automated production equipment of silicone oil above-mentioned, stirrer paddle is additionally provided in the shunting bucket.
In the automated production equipment of silicone oil above-mentioned, the agitating device includes agitator, is equipped with and stirs at the top of agitator
Driving motor is mixed, stirring driving motor output end is equipped with agitating shaft, and the scraper plate in agitator is successively arranged on agitating shaft, is stirred
Mix cutter head and stirring blade；The stirring cutter head includes the cutter hub in frustum cone structure, and cutter hub outside wall surface is equipped with one group of blade, knife
Body upper end is additionally provided with ring baffle.
In the automated production equipment of silicone oil above-mentioned, the water removal reaction kettle is externally provided with heating jacket, heating jacket
It is connected between feed inlet and cooling liquid outlet through pipeline.
Compared with prior art, the utility model passes through raw material storage tanks, water removal reaction kettle, agitating device, polymerization is anti-
It answers kettle, heat exchanger to be connected with product storage tank through pipeline, realizes the continuous production of automation, eliminate man-handling of materials intermediate product
Link, greatly improve production efficiency；Moreover, by increasing agitating device before polymerization reaction kettle, in advance to reaction
Object is stirred, and can not only improve stirring efficiency, it is also possible that reactant reaction is more abundant, improves product quality.Together
When, heat exchanger is made of snakelike conveying pipeline, separate hopper and aggregate bin, extends material in heat exchanger using snakelike conveying pipeline
Flowing time improves cooling efficiency so as to improve cooling effect；Using the deflector of screw arrangement on cylinder inboard wall come cold
But liquid stream is dynamic, and coolant liquid can be made to come into full contact with snakelike conveying pipeline, improves cooling effect and efficiency, and can increase coolant liquid and disturb
It is dynamic, it radiates convenient for coolant liquid.In conclusion the utility model has the characteristics that can be improved production efficiency.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the structural schematic diagram of agitating device；
Fig. 3 is the structural schematic diagram of heat exchanger.
Description of symbols in attached drawing: 1- raw material storage tanks, 2- remove water reaction kettle, 3- agitating device, 4- polymerization reaction kettle, 5-
Heat exchanger, 6- product storage tank, 501- cylinder, 502- shunt bucket, 503- afflux bucket, the snakelike conveying pipeline of 504-, 505- coolant liquid
Outlet, 506- cooling liquid inlet, 507- deflector, 301- agitator, 302- stir driving motor, 303- agitating shaft, and 304- is scraped
Plate, 305- stir cutter head, 306- stirring blade, 307- cutter hub, 308- blade, 309- ring baffle.
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.The automated production equipment of silicone oil is constituted as shown in Figure 1 to Figure 3, including raw material storage tanks 1, raw material storage
It deposits tank 1 and is connected with water removal reaction kettle 2 through pipeline, remove water reaction kettle 2 through pipeline and be connected with agitating device 3, agitating device 3 is through pipeline
It is connected with polymerization reaction kettle 4, polymerization reaction kettle 4 is connected with heat exchanger 5 through pipeline, and heat exchanger 5 is connected with finished product through pipeline and stores
Tank 6；The heat exchanger 5 includes the cylinder 501 arranged vertically, and 501 upper and lower ends of cylinder are respectively equipped with inlet port and outlet port, cylinder
Upper and lower ends inside body 501 are respectively equipped with the shunting bucket 502 and afflux bucket 503 being connected with inlet port and outlet port, shunt bucket
The more snakelike conveying pipelines 504 arranged vertically are equipped between 502 and afflux bucket 503；Cooling is also filled in the cylinder 501
Liquid, the upper and lower ends of 501 side of cylinder are respectively equipped with cooling liquid outlet 505 and cooling liquid inlet 506, on the inner wall of cylinder 501
It is additionally provided with the deflector 507 of screw arrangement.
Stirrer paddle is additionally provided in the shunting bucket 502.
The agitating device 3 includes agitator 301, and stirring driving motor 302, stirring driving are equipped at the top of agitator 301
302 output end of motor is equipped with agitating shaft 303, is successively arranged scraper plate 304, stirring blade in agitator 301 on agitating shaft 303
First 305 and stirring blade 306；The stirring cutter head 305 includes the cutter hub 307 in frustum cone structure, and 307 outside wall surface of cutter hub is equipped with
One group of blade 308,307 upper end of cutter hub are additionally provided with ring baffle 309.
The water removal reaction kettle 2 is externally provided with heating jacket, through pipe between the feed inlet and cooling liquid outlet 505 of heating jacket
Road is connected.
The whipping process of agitating device: after raw material enters agitator, stirring driving motor work drives agitating shaft rotation,
Then agitating shaft drives scraper plate, stirring cutter head and stirring blade rotation, scraper plate to carry out scraping place to the raw material on agitator inner wall
Reason, stirring cutter head are stirred crushing to material, and stirring blade is stirred and mixes operation.
The course of work of heat exchanger: finished product is flowed out from polymerization reaction kettle, and the shunting bucket of cylinder upper end is entered through feed inlet,
It shunts bucket to shunt silicone oil finished product, so that silicone oil enters in each snakelike conveying pipeline, and exchange heat with coolant liquid, finally
It is concentrated out of bottom afflux bucket, outflow tube, into being stored in product storage tank.During this, effect of the coolant liquid in pump
Under from the cooling liquid inlet of cylinder lower part enter, and from the cooling liquid outlet on top flow out, coolant liquid can be along cylinder inboard wall
Spiral.The coolant liquid flowed out from the cooling liquid outlet on top is back to the charging of water removal reaction kettle external heating jacket through pipeline
Mouthful.
The course of work of the utility model: raw material is flowed out from raw material storage tanks, is pressurizeed through pump, is transmitted to water removal reaction kettle
It is interior, reaction kettle is removed water under the heat effect of heating jacket, and water removal operation is carried out to raw material, after raw material completes water removal operation, warp
Pump pressurization, raw material, which enters in agitating device, to be stirred, and the pressurization through pumping enters polymerization reaction kettle after raw material completes stirring,
Reaction obtains finished product, and finished product enters in product storage tank after heat exchanger is cooling to be stored.
Claims (4)
1. the automated production equipment of silicone oil, it is characterised in that: including raw material storage tanks (1), raw material storage tanks (1) connect through pipeline
It is connected to water removal reaction kettle (2), water removal reaction kettle (2) is connected with agitating device (3) through pipeline, and agitating device (3) is connected through pipeline
Have polymerization reaction kettle (4), polymerization reaction kettle (4) is connected with heat exchanger (5) through pipeline, and heat exchanger (5) is connected with finished product through pipeline
Holding vessel (6)；The heat exchanger (5) includes the cylinder (501) arranged vertically, and cylinder (501) upper and lower ends are respectively equipped with charging
Mouthful and discharge port, the internal upper and lower ends of cylinder (501) be respectively equipped with the shunting bucket (502) being connected with inlet port and outlet port and
Afflux bucket (503) shunts and is equipped with the more snakelike conveying pipelines (504) arranged vertically between bucket (502) and afflux bucket (503)；Institute
State and be also filled with coolant liquid in cylinder (501), the upper and lower ends of cylinder (501) side be respectively equipped with cooling liquid outlet (505) and
Cooling liquid inlet (506) is additionally provided with the deflector (507) of screw arrangement on the inner wall of cylinder (501).
2. the automated production equipment of silicone oil according to claim 1, it is characterised in that: in the shunting bucket (502) also
Equipped with stirrer paddle.
3. the automated production equipment of silicone oil according to claim 1, it is characterised in that: the agitating device (3) includes
Agitator (301), agitator (301) top are equipped with stirring driving motor (302), and stirring driving motor (302) output end is equipped with
Agitating shaft (303), be successively arranged on agitating shaft (303) scraper plate (304) in agitator (301), stirring cutter head (305) and
Stirring blade (306)；Stirring cutter head (305) includes the cutter hub (307) in frustum cone structure, is set in cutter hub (307) outside wall surface
There is one group of blade (308), cutter hub (307) upper end is additionally provided with ring baffle (309).
4. the automated production equipment of silicone oil according to claim 1, it is characterised in that: the water removal reaction kettle (2) is outside
Equipped with heating jacket, it is connected between the feed inlet and cooling liquid outlet (505) of heating jacket through pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820690033.7U CN208320772U (en) | 2018-05-09 | 2018-05-09 | The automated production equipment of silicone oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820690033.7U CN208320772U (en) | 2018-05-09 | 2018-05-09 | The automated production equipment of silicone oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208320772U true CN208320772U (en) | 2019-01-04 |
Family
ID=64777355
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820690033.7U Expired - Fee Related CN208320772U (en) | 2018-05-09 | 2018-05-09 | The automated production equipment of silicone oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208320772U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111151163A (en) * | 2020-01-04 | 2020-05-15 | 张惠文 | Multi-channel cooling and freshness-retaining detection mechanism for semi-fluid food processing |
| CN111533914A (en) * | 2020-04-13 | 2020-08-14 | 浙江衢州正邦有机硅有限公司 | Continuous production process of polymethyltriethoxysilane in pipeline mode |
-
2018
- 2018-05-09 CN CN201820690033.7U patent/CN208320772U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111151163A (en) * | 2020-01-04 | 2020-05-15 | 张惠文 | Multi-channel cooling and freshness-retaining detection mechanism for semi-fluid food processing |
| CN111533914A (en) * | 2020-04-13 | 2020-08-14 | 浙江衢州正邦有机硅有限公司 | Continuous production process of polymethyltriethoxysilane in pipeline mode |
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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: 20190104 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |