CN205473638U - Crystallization growing grain jar - Google Patents
Crystallization growing grain jar Download PDFInfo
- Publication number
- CN205473638U CN205473638U CN201620223989.7U CN201620223989U CN205473638U CN 205473638 U CN205473638 U CN 205473638U CN 201620223989 U CN201620223989 U CN 201620223989U CN 205473638 U CN205473638 U CN 205473638U
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- CN
- China
- Prior art keywords
- cylinder
- agitator
- barrel
- crystallization
- oil
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- 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
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- Fats And Perfumes (AREA)
- Edible Oils And Fats (AREA)
Abstract
The utility model discloses a crystallization growing grain jar, including the landing leg, the barrel is installed on the landing leg, is provided with the charge door in the upper end of barrel, is equipped with the oil -out in the bottom of barrel, installs a plurality of cooling coil of group on the inner wall of barrel, and the agitator is installed to cooling coil's import and the outwardly directed barrel of export difference in the barrel, and the agitator is connected with transmission, and transmission installs the upper end at the barrel. The utility model discloses low in manufacturing cost, simple structure, convenient operation, the suitability is strong, is favorable to the energy saving and consumption reduction of enterprise.
Description
Technical field
This utility model belongs to edible oil technical field of processing equipment, is specifically related to a kind of crystallization maturator fat dystectic in edible oil and fat or wax separated with the fat of low melting point.
Background technology
In edible oil and fat process of manufacture, oils and fats contains the fat of dystectic fat or wax and low melting point, dystectic fat or the existence of wax, edible oil dulling can be caused at low temperatures or solid crystal phenomenon occurs, having a strong impact on mouthfeel and the edibility of edible oil；Therefore, utilize the difference of its fusing point height, by regular cooling down, separate after dystectic fat or wax are condensed into solid fine grain, so obtain the edible oil that can deposit at a lower temperature；The agitator of the crystallization growing the grain device agitating device that China uses at present is mostly paddle, actuating device can not speed governing, jacket type cooling (heating) does not control cooling rate, and this crystallization growing the grain device is uneven due to edible oil cooling, and the crystal grain formed easily is blended；Under these conditions, the crystalline particle that edible oil is formed is loose, irregular, and this causes operating difficulties to the filtration in later stage, and the neutral oil content in tristearin is high, causes yield low.
For realizing in edible oil and fat crystallization growing the grain separation process, the crystalline particle of dystectic fat or wax is solid full, it is simple to filter；Thus improve product oil yield, increase the economic benefit of fats and oils processing factory；Engineers and technicians, device fabrication and manufacturer design and test multiple eating oil crystallization growing the grain device, one is that oil-groove crystallizes growing the grain device, edible oil cools in oil groove step by step, the crystallization growing the grain device of this kind of structure does not has agitator, heat transfer efficiency is low, wastes the energy, and floor space is big simultaneously, be not suitable for large-scale production demand, the most superseded；Another kind be pot type crystallize growing the grain device, use jacket type cool, can not speed-regulating actuator, dasher；The crystallization growing the grain device of this kind of structure, cooling medium and edible oil and fat are insufficient contact, easily form local overcooling phenomenon, are unfavorable for the formation of crystal grain, grow up；In temperature-fall period, rate of cooling and mixing speed cannot adjust, and the crystalline particle resulted in is loose, irregular, are unfavorable for filtration during later stage solid-liquid separation, cause product oil yield low, increase production cost.
Utility model content
For above-mentioned deficiency described in the prior, the purpose of this utility model is to provide a kind of simple in construction, easy to operate, efficient energy-saving, and the speed that cools and mixing speed can control the most flexibly, and low cost of manufacture forms the solid full crystallization maturator of crystal grain.
For realizing above-mentioned technical purpose, the technical scheme that this utility model is used is as follows:
A kind of crystallization maturator, including supporting leg, cylinder is arranged on supporting leg, the upper end of cylinder is provided with charge door, is provided with oil-out in the bottom of cylinder, the inwall of cylinder is provided with some groups of cooling coils, the import of cooling coil and outlet protruding cylinder respectively, being provided with agitator in cylinder, agitator is connected with actuating device, and actuating device is arranged on the upper end of cylinder.
The bottom of described cylinder is conical bottom, is provided with oil-out and manhole in conical bottom.
Described actuating device is arranged on the upper end of cylinder by steelframe, and described actuating device includes motor and speed reducer, and the output shaft of motor is through being connected with the rotation bar of agitator with reductor.
If described agitator is for including rotating bar with dried layer every paddle group, paddle group is fixed on rotation bar, and every layer of paddle group includes three paddles respectively, and one end of paddle is fixed on rotation bar, and paddle angle each other is 120 degree.
The lower end of described rotation bar is arranged on fixture, and rotates in the hole, location of fixture, and fixture is arranged on cylinder inboard wall.
This utility model controls the speed of agitator stirring by controlling the rotating speed of motor in actuating device, by the flow velocity of cooling media in control cooling coil, it is possible to achieve cooling medium and the speed of edible oil heat exchange, cooling medium is without short circuit phenomenon, good effect of heat exchange.The multiple layers of stirring blades group structure of agitator ensures edible oil mix homogeneously, it is simple to the generation of crystal grain and growing up.This utility model controls the mixing speed of agitator by actuating device, realizes growing up of the control of edible oil cooling rate, beneficially crystal grain in conjunction with the flow velocity of cooling medium in control cooling coil, it is achieved optimal crystallization growing the grain effect.The manhole arranged in the conical bottom of cylinder and oil-out, manhole just overhaul of the equipments, the fuel-displaced mode of oil-out is totally thorough, noresidue.
This utility model low cost of manufacture, simple in construction, easy to operate, the suitability is strong, beneficially industry energy conservation consumption reduction.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the A-A sectional view in Fig. 1.
Detailed description of the invention
As shown in Figure 1-2, a kind of crystallization maturator, including supporting leg 1, cylinder 4 is arranged on supporting leg 1.The upper end of cylinder 4 being provided with charge door, is provided with oil-out in the bottom of cylinder 4, for the ease of fuel-displaced, the bottom of described cylinder 4 is conical bottom, is provided with oil-out and manhole 3 in conical bottom, and the setting of manhole 3 is convenient for overhaul of the equipments.
The inwall of cylinder 4 is provided with some groups of cooling coils 5, the import of cooling coil 5 and outlet protruding cylinder 4 respectively.Cooling coil 5 is fixed on cylinder 4 inwall by U-steel frame 7, and the quantity of cooling coil is set according to practical situation.
Being provided with agitator 6 in cylinder 4, agitator 6 is connected with actuating device 10, and actuating device 10 is arranged on the upper end of cylinder 4 by steelframe 8.Described actuating device 10 includes motor 11 and reductor 9, and the output shaft of motor 11 is through being connected with the rotation bar 6-1 of agitator 6 with reductor 9.
If described agitator 6 is for including rotating bar 6-1 and dried layer paddle group, paddle group is fixed on rotation bar 6-1, every layer of paddle group includes three paddle 6-2 respectively, and one end of paddle 6-2 is fixed on rotation bar 6-1, and paddle 6-2 angle each other is 120 degree.
The lower end of described rotation bar 6-1 is arranged on fixture 12, and rotates in the hole, location of fixture 12, and fixture 12 is arranged on cylinder 4 inwall.
In the present embodiment, described paddle group is three layers.
Pending edible oil is proceeded to from charging aperture, control the rotating speed of motor 11 in actuating device 10, thus control the mixing speed of agitator 6, and by the flow velocity of cooling medium in control cooling coil 5, control the exchange rate of cooling medium and edible oil, by mixing speed and the control of rate of heat exchange, realize the control of edible oil cooling rate, be conducive to the generation of crystal grain and grow up, it is achieved optimal growing the grain effect, improve oil yield.
Claims (5)
1. a crystallization maturator, it is characterized in that: include supporting leg (1), cylinder (4) is arranged on supporting leg (1), the upper end of cylinder (4) is provided with charge door, it is provided with oil-out in the bottom of cylinder (4), some groups of cooling coils (5) are installed on the inwall of cylinder (4), the import of cooling coil (5) and outlet protruding cylinder (4) respectively, agitator (6) is installed in cylinder (4), agitator (6) is connected with actuating device (10), and actuating device (10) is arranged on the upper end of cylinder (4).
Crystallization maturator the most according to claim 1, it is characterised in that: the bottom of described cylinder (4) is conical bottom, is provided with oil-out and manhole (3) in conical bottom.
Crystallization maturator the most according to claim 1 and 2, it is characterized in that: described actuating device (10) is arranged on the upper end of cylinder (4) by steelframe (8), described actuating device (10) includes motor (11) and reductor (9), and the output shaft of motor (11) is through being connected with the rotation bar (6-1) of agitator (6) with reductor (9).
Crystallization maturator the most according to claim 3, it is characterized in that: described agitator (6) for include rotate bar (6-1) and if dried layer is every paddle group, paddle group is fixed in rotation bar (6-1), every layer of paddle group includes three paddles (6-2) respectively, one end of paddle (6-2) is fixed in rotation bar (6-1), and paddle (6-2) angle each other is 120 degree.
Crystallization maturator the most according to claim 4, it is characterised in that: the lower end of described rotation bar (6-1) is arranged on fixture (12), and rotates in the hole, location of fixture (12), and fixture (12) is arranged on cylinder (4) inwall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620223989.7U CN205473638U (en) | 2016-03-22 | 2016-03-22 | Crystallization growing grain jar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620223989.7U CN205473638U (en) | 2016-03-22 | 2016-03-22 | Crystallization growing grain jar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205473638U true CN205473638U (en) | 2016-08-17 |
Family
ID=56651366
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620223989.7U Expired - Fee Related CN205473638U (en) | 2016-03-22 | 2016-03-22 | Crystallization growing grain jar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205473638U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106281671A (en) * | 2016-10-17 | 2017-01-04 | 内蒙古万利福生物科技有限公司 | The cold refinement technique of cold pressed flax seed oil and refining equipment thereof |
| CN107715494A (en) * | 2017-11-17 | 2018-02-23 | 扬州永锋工业设备安装有限公司 | A kind of self-powered crystallizing tower based on solar energy photovoltaic panel |
| CN112662471A (en) * | 2020-12-31 | 2021-04-16 | 郑州远洋油脂工程技术有限公司 | Energy-saving and consumption-reducing process in grease dewaxing fractionation process |
-
2016
- 2016-03-22 CN CN201620223989.7U patent/CN205473638U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106281671A (en) * | 2016-10-17 | 2017-01-04 | 内蒙古万利福生物科技有限公司 | The cold refinement technique of cold pressed flax seed oil and refining equipment thereof |
| CN107715494A (en) * | 2017-11-17 | 2018-02-23 | 扬州永锋工业设备安装有限公司 | A kind of self-powered crystallizing tower based on solar energy photovoltaic panel |
| CN112662471A (en) * | 2020-12-31 | 2021-04-16 | 郑州远洋油脂工程技术有限公司 | Energy-saving and consumption-reducing process in grease dewaxing fractionation process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20160817 Termination date: 20170322 |