CN204999873U - Maize oil dewaxing device - Google Patents
Maize oil dewaxing device Download PDFInfo
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- CN204999873U CN204999873U CN201520623216.3U CN201520623216U CN204999873U CN 204999873 U CN204999873 U CN 204999873U CN 201520623216 U CN201520623216 U CN 201520623216U CN 204999873 U CN204999873 U CN 204999873U
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- oil
- dewaxing
- feed pump
- agitator motor
- fixedly connected
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Abstract
The utility model relates to a maize oil dewaxing device belongs to the corn processing technology field, including heat exchanger, blending tank, dewaxing crystallizer, growing the grain jar, oil -feed pump, filter, controller, wherein the blending tank is including a jar body, diatomaceous earth pan feeding mouth, agitator motor, stirring speed reducer, stirring wing, level gauge, thermometer. The utility model discloses an agitator motor, stirring speed reducer and the stirring wing of setting on the blending tank not only make fully homogeneous mixing of oil and diatomaceous earth, have still increased about 15 minutes of the time of dewaxed oil crystallization, the oil -feed pump changes traditional centrifugal pump for the screw pump, and the screw pump can not rub crystal grain in the oil, has guaranteed further that national trade fixed standard newly can be reachd to the freezing time of maize oil. Use the utility model discloses the maize oil of producing, 30 hours are brought up to to the freezing time, have reached country and market and have required the index to using of screw pump belongs to the first in the same trade, bring the profound influence to the same trade.
Description
Technical field
The utility model belongs to corn deep processing technology field, particularly relates to a kind of Semen Maydis oil dewaxing device.
Background technology
In corn deep processing industry, essential oil workshop dewaxing technique has been maturation process at present in the whole nation, and the Semen Maydis oil that various new installation is produced can reach the newly fixed standard of national industry completely.But for development corn deep processing factory comparatively early, cost of updating the equipment is high, but the Semen Maydis oil that old equipment and process is produced does not reach the newly fixed standard of national industry on freezing time.Therefore transforming dewaxing technique and equipment, is develop the new developing direction of corn deep processing factory one comparatively early.The leading portion that dewaxes in traditional dewaxing technique sends into dewaxing at transfer oil depot decolouring oil tank, and after plate-type heat exchanger, directly enter dewaxing crystallizer, then add diatomite, causing diatomite to stir unevenly affects freezing time.The oil-feed pump of filter is impeller pump in addition, is easily rubbed by crystal grain, affect the freezing time of Semen Maydis oil during work.
Therefore need badly in the middle of prior art and want a kind of novel technical scheme to solve this problem.
Utility model content
Technical problem to be solved in the utility model is: provide a kind of Semen Maydis oil dewaxing device Semen Maydis oil solving old equipment and process production on freezing time, do not reach the newly fixed standard of national industry; The leading portion that dewaxes in traditional dewaxing technique sends into dewaxing at transfer oil depot decolouring oil tank directly to enter dewaxing crystallizer after plate-type heat exchanger, and then add diatomite, causing diatomite to stir unevenly affects freezing time; The oil-feed pump of filter is impeller pump, is easily rubbed by crystal grain, affect the technical problems such as the freezing time of Semen Maydis oil during work.
A kind of Semen Maydis oil dewaxing device, is characterized in that: comprise interchanger, mixing tank, dewaxing crystallizer, maturator, oil-feed pump, filter, controller,
Described mixing tank comprises tank body, diatomite feeding mouth, agitator motor, stirring step-down gear, stirring wing, liquidometer, thermometer, and described diatomite feeding mouth is positioned at the top of tank body; Described agitator motor and stirring step-down gear are all positioned at the outside of tank body, and agitator motor is connected with stirring step-down gear by gears meshing; One end of described stirring wing is rod-like structure, and this end is fixedly connected with stirring step-down gear, and the other end of stirring wing is provided with foliated lamellar whipping appts, and this end is arranged on the inside of tank body; Described liquidometer is fixedly mounted on the middle part of inner tank wall; Described thermometer is fixedly mounted on the bottom of inner tank wall;
Described interchanger is fixedly connected with the oil-in of mixing tank by pipeline; The discharge port of described mixing tank is fixedly connected with dewaxing crystallizer opening for feed by pipeline; The described discharge port of dewaxing crystallizer is fixedly connected with the opening for feed of maturator; The discharge port of described maturator and being fixedly connected with of oil-feed pump; Described oil-feed pump is fixedly connected with filter; Described controller is connected with interchanger, agitator motor, liquidometer, thermometer and oil-feed pump respectively by wire.
Described oil-feed pump is spiral pump.
By above-mentioned design, the utility model can bring following beneficial effect:
The utility model does not change traditional corn deep processing technique, only simply transforms existing equipment, adds a mixing tank at Semen Maydis oil after interchanger.
The agitator motor that mixing tank is arranged, stirring step-down gear and stirring wing, not only enable oil mix with diatomite is full and uniform, also add the about 15 minutes time of pressed oil crystallization; Mixing tank is provided with liquidometer and thermometer, controller can regulate oil-feed flow according to the liquidometer information of mixing tank, inlet oil temperature is regulated by the temperature information of thermometer, thus control oil-feed flow and the temperature of dewaxing crystallizer, reach the object of fine adjustments crystallization time and crystallization effect.
Oil-feed pump of the present utility model in addition, is replaced by spiral pump by traditional impeller pump, and spiral pump can not rub crystal grain in oil, and the freezing time further ensuring Semen Maydis oil can arrive the newly fixed standard of national industry.
Use the Semen Maydis oil that the utility model is produced, freezing time brings up to 30 hours, reaches country and market demands index, and being applied in the same industry of spiral pump belongs to the first, brings profound influence to the same industry.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is further described:
Fig. 1 is the structured flowchart of a kind of Semen Maydis oil dewaxing device of the utility model.
Fig. 2 is the structural representation of mixing tank in the utility model.
In figure, 1-interchanger, 2-mixing tank, 3-dewaxing crystallizer, 4-maturator, 5-oil-feed pump, 6-filter, 7-controller, 201-tank body, 202-diatomite feeding mouth, 203-agitator motor, 204-stir step-down gear, 205-stirring wing, 206-liquidometer, 207-thermometer.
Embodiment
As shown in the figure, a kind of Semen Maydis oil dewaxing device, is characterized in that: comprise interchanger 1, mixing tank 2, dewaxing crystallizer 3, maturator 4, oil-feed pump 5, filter 6, controller 7,
Described mixing tank 2 comprises tank body 201, diatomite feeding mouth 202, agitator motor 203, stirs step-down gear 204, stirring wing 205, liquidometer 206, thermometer 207, and described diatomite feeding mouth 202 is positioned at the top of tank body 201; Described agitator motor 203 and stirring step-down gear 204 are all positioned at the outside of tank body 201, and agitator motor 203 is connected with stirring step-down gear 204 by gears meshing; One end of described stirring wing 205 is rod-like structure, and this end is fixedly connected with stirring step-down gear 204, and the other end of stirring wing 205 is provided with foliated lamellar whipping appts, and this end is arranged on the inside of tank body 201; Described liquidometer 206 is fixedly mounted on the middle part of tank body 201 inwall; Described thermometer 207 is fixedly mounted on the bottom of tank body 201 inwall;
Described interchanger 1 is fixedly connected with by the oil-in of pipeline with mixing tank 2; The discharge port of described mixing tank 2 is that opening for feed is fixedly connected with by pipeline with, the crystallizer 3 that dewaxes; The discharge port of described dewaxing crystallizer 3 is fixedly connected with the opening for feed of maturator 4; The discharge port of described maturator 4 and being fixedly connected with of oil-feed pump 5; Described oil-feed pump 5 is fixedly connected with filter 6; Described controller 7 is connected with interchanger 1, agitator motor 203, liquidometer 206, thermometer 207 and oil-feed pump 5 respectively by wire.
Described oil-feed pump 5 is spiral pump.
Technical process of the present utility model is as follows: bleached oil enters in mixing tank 2 through plate-type heat exchanger 1 after under meter is quantitative, and diatomite is added device and evenly added in mixing tank 2 by diatomite by diatomite feeding mouth 202.Agitator motor 203 drives and stirs step-down gear 204, stirring step-down gear 204 drives stirring wing 205 to stir, mixing tank is provided with liquidometer 206 and thermometer 207, controller 7 can regulate oil-feed flow and inlet oil temperature respectively according to the temperature information of the liquidometer information of mixing tank and thermometer, and then control oil-feed flow and the temperature of dewaxing crystallizer 3, reach the object of fine adjustments crystallization time and crystallization effect.Semen Maydis oil enters in three maturators 4 after automatically entering full three dewaxing crystallizers 3 successively more successively, and Semen Maydis oil progressively decrease temperature crystalline crystallization when successively through dewaxing crystallizer 3, enters in maturator 4 and carry out protecting brilliant growing the grain.Then by spiral pump, the oil in last maturator 4 is sent into horizontal filter 6 and carry out dewaxing filtration.The flow that whole process focuses on oil will reach balanced.
Claims (2)
1. a Semen Maydis oil dewaxing device, it is characterized in that: comprise interchanger (1), mixing tank (2), dewaxing crystallizer (3), maturator (4), oil-feed pump (5), filter (6), controller (7)
Described mixing tank (2) comprises tank body (201), diatomite feeding mouth (202), agitator motor (203), stirs step-down gear (204), stirring wing (205), liquidometer (206), thermometer (207), and described diatomite feeding mouth (202) is positioned at the top of tank body (201); Described agitator motor (203) and stirring step-down gear (204) are all positioned at the outside of tank body (201), and agitator motor (203) is connected with stirring step-down gear (204) by gears meshing; One end of described stirring wing (205) is rod-like structure, this end is fixedly connected with stirring step-down gear (204), the other end of stirring wing (205) is provided with foliated lamellar whipping appts, and this end is arranged on the inside of tank body (201); Described liquidometer (206) is fixedly mounted on the middle part of tank body (201) inwall; Described thermometer (207) is fixedly mounted on the bottom of tank body (201) inwall;
Described interchanger (1) is fixedly connected with by the oil-in of pipeline with mixing tank (2); The discharge port of described mixing tank (2) is fixedly connected with by the opening for feed of pipeline with dewaxing crystallizer (3); The discharge port of described dewaxing crystallizer (3) is fixedly connected with the opening for feed of maturator (4); The discharge port of described maturator (4) and being fixedly connected with of oil-feed pump (5); Described oil-feed pump (5) is fixedly connected with filter (6); Described controller (7) is connected with interchanger (1), agitator motor (203), liquidometer (206), thermometer (207) and oil-feed pump (5) respectively by wire.
2. a kind of Semen Maydis oil dewaxing device according to claim 1, is characterized in that: described oil-feed pump (5) is spiral pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520623216.3U CN204999873U (en) | 2015-08-18 | 2015-08-18 | Maize oil dewaxing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520623216.3U CN204999873U (en) | 2015-08-18 | 2015-08-18 | Maize oil dewaxing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204999873U true CN204999873U (en) | 2016-01-27 |
Family
ID=55156770
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520623216.3U Expired - Fee Related CN204999873U (en) | 2015-08-18 | 2015-08-18 | Maize oil dewaxing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204999873U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107746746A (en) * | 2017-10-17 | 2018-03-02 | 山东西王食品有限公司 | A kind of continuous crystallisation, growing the grain, the method and apparatus of dewaxing refining raising Vegetable Oil Quality |
-
2015
- 2015-08-18 CN CN201520623216.3U patent/CN204999873U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107746746A (en) * | 2017-10-17 | 2018-03-02 | 山东西王食品有限公司 | A kind of continuous crystallisation, growing the grain, the method and apparatus of dewaxing refining raising Vegetable Oil Quality |
| CN107746746B (en) * | 2017-10-17 | 2021-01-19 | 山东西王食品有限公司 | Method and equipment for improving vegetable oil quality through continuous crystallization, crystal growing and dewaxing refining |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 136001, Siping City, Jilin Province, East flat, East Street, the old city 1 to 2, 101 Patentee after: Jiale food Limited by Share Ltd Address before: 136001 Siping Road, Siping City, Jilin Province, 6122, Nanning Road, old industrial zone, Siping City Patentee before: CAREPAL FOOD CO., LTD. |
|
| 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: 20160127 Termination date: 20190818 |