CN105238555A - Antioxidation crystallization tank - Google Patents
Antioxidation crystallization tank Download PDFInfo
- Publication number
- CN105238555A CN105238555A CN201410250052.4A CN201410250052A CN105238555A CN 105238555 A CN105238555 A CN 105238555A CN 201410250052 A CN201410250052 A CN 201410250052A CN 105238555 A CN105238555 A CN 105238555A
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- pipe
- tank body
- oil
- heat exchange
- lower cone
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- Fats And Perfumes (AREA)
- Edible Oils And Fats (AREA)
Abstract
The invention discloses an antioxidation crystallization tank. According to the antioxidation crystallization tank, a semielliptical sealing head arranged on an upper cover of a tank body is capable of suffering from certain pressure; when oil is delivered into the tank body, valves on a oil inlet pipe and a pressurizing pipe are unsealed so as to delivery edible oil into the tank body; air is discharged via the pressurizing pipe; valves on a refrigerant inlet pipe and a refrigerant outlet pipe of a heat exchange cage tube are unsealed, so that continuous entering of refrigerant liquid into the heat exchange cage tube and continuous cycling are realized; heat energy is taken away, and oil temperature is reduced; when crystallization and grain growing of edible oil are capable of satisfying requirements, the vales on the oil inlet pipe are unsealed, and the valves on the pressurizing pipe are switched so as to increase nitrogen pressure and delivery edible oil to a filter for filtering; inert gas-nitrogen are used for insulating air and edible oil so as to prevent edible oil oxidation caused by contact with oxygen in the air, and solve problems of oil oxidative rancidity; crystallization tank ancillary facility is simplified, production cost and energy consumption are reduced, and production economic benefit is increased.
Description
Technical field:
The product that the present invention relates to, is widely used in the winterization technique of food oils engineering, utilizes rare gas element to completely cut off air, the crystallization preventing from being oxidized in edible oil preservation process, growing the grain technical field.
Background technology:
Food oils, except supplier's body heat energy and required lipid acid, still can provide the look of food, perfume and taste, promote palatability and satietion, send the lipid-soluble substance of human body needs as vitamin A. D. E and K etc.Grease, on human physiological functions, especially to the prevention of cancer, coronary artery disease, or promotes that hematoblastic aggegation, the formation of thrombus and the increase and decrease etc. of courage cholesterol and triacylglycerol all have just negative effect.Therefore food oils are before processed finished products oil is added, high-grade primary oil must by coming unstuck, decolouring, depickling, deodorization, dewaxing, the objectionable impuritiess such as technique such as degreasing remove.Dewaxing, degreasing process are by after input edible oil crystallizer, inject refrigerant and carry out cooling and crystallization it; Separate out in oil after crystallization from edible oil containing high-melting-point wax and high melting solid fat, then adopt the operation of filtration to be removed.At edible oil in the process of dewaxing, degreasing filtration, the crystallizer of most of enterprise, adopts normal pressure flat head; Therefore spiral pump, high level tank that winterization auxiliary facility need adopt, utilize the height pressure difference of high level tank and filter to carry out filtration wax, lipid to edible oil.Need like this to increase other off-set facility such as e-quipment and pipe, also need to consume the energy, its filter effect is also undesirable simultaneously.
Summary of the invention:
Product involved by this project, spiral pump, high level tank that the winterization equipment for above-mentioned routine need adopt; The height pressure difference of high level tank and filter is utilized to carry out filtration wax, lipid to edible oil.Other off-set facility such as the e-quipment and pipe that such needs increase, also need to consume the problems such as the energy simultaneously; There is provided a kind of anti-oxidant crystallizer, tank body upper cover adopts semiellipse end socket; Certain pressure can be born.Utilize rare gas element-nitrogen, be isolated between air and edible oil, to ensure the quality of edible oil; By increasing the pressure of rare gas element, edible oil being transported to filter and filtering; Reach the winterization effect of high-quality.
Anti-oxidant crystallizer, comprising: supporting leg, tank body, lower cone, semiellipse end socket, heat exchange cage pipe, oil inlet pipe, motor reducer and drive disk assembly.Drive disk assembly comprises: reducer pedestal, shaft coupling, main shaft, mountain font stir cutter, level stirs cutter, base bearing seat support.The top of tank body is provided with semiellipse end socket, and semiellipse end socket is provided with oil inlet pipe, forcing pipe, reducer pedestal; The top of reducer pedestal is provided with motor reducer.Forcing pipe has two kinds of functions: when tank body needs oil-feed, opens valve that forcing pipe is provided with and discharges air in tank body; When the oil require in tank body filters, the unlatching of switch valve, makes nitrogen enter in tank body.The below of tank body is provided with lower cone, and the bottom of lower cone is provided with oil outlet pipe.The inside of lower cone is provided with base bearing seat support, and base bearing seat support is provided with bearing support.The top of main shaft is connected by shaft coupling with motor reducer, and the below of main shaft is provided with bearing support with base bearing seat support and is connected.Be provided with columnar heat exchange cage pipe in tank body, by strut member, heat exchange cage pipe be fixed in inner tank wall.The refrigerant inlet pipe of heat exchange cage pipe is opened on lower cone, and refrigerant goes out tube opening on tank wall.Main shaft is erected at the central authorities in tank body, coaxially passes with heat exchange cage pipe; Main shaft is provided with in heat exchange cage scope tube 3 levels and stirs cutter, the main shaft being positioned at the position of lower cone is provided with mountain font and stirs cutter; When main shaft works, drive level stirs cutter, mountain font stirs swivel and moves, the effect making edible oil reach crystalline particle to mix.Tank body and lower cone junction are provided with 4 supporting legs, and crystallizer is erected in winterization system.
When edible oil carries out the crystallization of winterization operation, growing the grain, open valve that on semiellipse end socket, oil inlet pipe is provided with and the valve that forcing pipe is provided with, make edible oil enter in tank body; Air in tank body is discharged through forcing pipe.When the oil level of the edible oil in tank body reaches certain height, starter motor step-down gear makes that main shaft drive level stirs cutter, mountain font stirs that swivel is dynamic makes edible oil mix.Refrigerant inlet pipe, the refrigerant of opening heat exchange cage pipe go out the valve that pipe is provided with, and make cooling medium liquid continuously enter heat exchange cage pipe and in interior continuous circulation; Take away the heat of edible oil, oil temperature is declined; Thus reach the effect of crystallization, growing the grain.Through sampling, after the crystallization of edible oil, the processing parameter of growing the grain reach requirement, the valve that on closedown semiellipse end socket, oil inlet pipe is provided with and the valve that switching forcing pipe is provided with, make nitrogen enter in tank body.First utilize edible oil gravity pressure in crystallizer to filter, the pressure then increasing rare gas element-nitrogen filters complete to edible oil.
By the improvement of above-mentioned crystallizer, both prevented because the oxygen in air contacts with edible oil and be oxidized, fundamentally having ensure that grease oxidation rancid problem.Simplify the auxiliary facility of crystallizer simultaneously, decrease production cost and energy expenditure, thus improve the economic benefit of production.
Accompanying drawing illustrates:
Below in conjunction with drawings and Examples, the present invention is further described, and Fig. 1 is a kind of structural representation of anti-oxidant crystallizer.
As shown in Figure 1:
Supporting leg 1, lower cone 2, heat exchange cage pipe 3, level stir cutter 4, tank body 5, refrigerant go out pipe 6, upper support frame 7, main shaft 8, semiellipse end socket 9, oil inlet pipe 10, reducer pedestal 11, motor reducer 12, shaft coupling 13, forcing pipe 14, anchor ear 15, lower support frame 16, refrigerant inlet pipe 17, mountain font stir cutter 18, base bearing seat support 19, oil outlet pipe 20.
Embodiment:
As shown in Figure 1, the top of tank body 5 is provided with semiellipse end socket 9 to product involved by this project, and semiellipse end socket 9 is provided with oil inlet pipe 10, forcing pipe 14, reducer pedestal 11; The top of reducer pedestal 11 is provided with motor reducer 12.The below of tank body 5 is provided with lower cone 2, and the bottom of lower cone 2 is provided with oil outlet pipe 20.The inside of lower cone 2 is provided with base bearing seat support 19, and base bearing seat support 19 is provided with bearing support.The top of main shaft 8 is connected by shaft coupling 13 with motor reducer 12, and the below of main shaft 8 is provided with bearing support with base bearing seat support 19 and is connected.Be provided with columnar heat exchange cage pipe 3 in tank body 5, by upper support frame 7, lower support frame 16, heat exchange cage pipe 3 be fixed on tank body 5 inwall.The refrigerant inlet pipe 17 of heat exchange cage pipe 3 is opened on lower cone, and refrigerant goes out pipe 6 and is opened on tank body 5 wall.Main shaft 8 is erected at the central authorities in tank body 5, coaxially passes with heat exchange cage pipe 3; Main shaft 8 is provided with in heat exchange cage scope tube 3 levels and stirs cutter 4, the main shaft 8 being positioned at the position of lower cone 2 is provided with mountain font and stirs cutter 18; When main shaft 7 works, drive level stirs cutter 4, mountain font stirs cutter 18 and rotates.Tank body 5 and lower cone 2 junction are provided with 4 supporting legs 1, and crystallizer is erected in winterization system.
When edible oil carries out the crystallization of winterization operation, growing the grain, open valve that on semiellipse end socket 9, oil inlet pipe 10 is provided with and the valve that forcing pipe 14 is provided with, make edible oil enter in tank body 5; Air in tank body 5 is discharged through forcing pipe 14.When the oil level of the edible oil in tank body 5 reaches certain height, starter motor step-down gear 12 makes that main shaft 8 drive level stirs cutter 4, mountain font stirs cutter 18 and rotates edible oil is mixed.Refrigerant inlet pipe 17, the refrigerant of opening heat exchange cage pipe 3 go out the valve that pipe 6 is provided with, and make cooling medium liquid continuously enter heat exchange cage pipe 3 and in interior continuous circulation; Take away the heat of edible oil, oil temperature is declined; Thus reach the effect of crystallization, growing the grain.Through sampling, after the crystallization of edible oil, the processing parameter of growing the grain reach requirement, the valve that on closedown semiellipse end socket 9, oil inlet pipe 10 is provided with and the valve that switching forcing pipe 14 is provided with, make nitrogen enter in tank body 5.First utilize edible oil gravity pressure in crystallizer to filter, the pressure then increasing rare gas element-nitrogen filters complete to edible oil.
Claims (4)
1. anti-oxidant crystallizer, comprising: supporting leg (1), tank body (5), lower cone (2), semiellipse end socket (9), heat exchange cage pipe (3), oil inlet pipe (10) and drive disk assembly; Described drive disk assembly comprises: motor reducer (12), reducer pedestal (11), shaft coupling (13), main shaft (8), mountain font stir cutter (18), level stirs cutter (4), base bearing seat support (19); The top of described tank body (5) is provided with semiellipse end socket (9), and end socket is provided with oil inlet pipe (10), forcing pipe (14), reducer pedestal (11); The top of described reducer pedestal (11) is provided with motor reducer (12); The below of described tank body is provided with lower cone (2), and the bottom of lower cone is provided with oil outlet pipe (20); The inside of described lower cone (2) is provided with base bearing seat support (19), and support is provided with bearing support; The top of described main shaft (8) is connected by shaft coupling (13) with motor reducer (12), and the bearing support that below and the base bearing seat support (19) of main shaft are provided with is connected; Described main shaft (8) is erected at the central authorities in tank body (5), passes with heat exchange cage pipe (3) is concentric; Described tank body (5) and lower cone (2) junction are provided with 4 supporting legs (1).
2. anti-oxidant crystallizer according to claim 1, its feature: the refrigerant inlet pipe (17) of described heat exchange cage pipe (3) is opened on lower cone (2), refrigerant goes out pipe (6) and is opened on tank body (5) wall.
3. anti-oxidant crystallizer according to claim 1, its feature: described main shaft (8) is provided with in heat exchange cage pipe (3) scope 3 levels and stirs cutter (4), the position being positioned at lower cone (2) is provided with 1 mountain font and stirs cutter (18).
4. anti-oxidant crystallizer according to claim 1, its feature: be provided with columnar heat exchange cage pipe (3) in described tank body (5), is fixed on inwall by upper support frame (7), lower support frame (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410250052.4A CN105238555A (en) | 2014-06-09 | 2014-06-09 | Antioxidation crystallization tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410250052.4A CN105238555A (en) | 2014-06-09 | 2014-06-09 | Antioxidation crystallization tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105238555A true CN105238555A (en) | 2016-01-13 |
Family
ID=55036380
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410250052.4A Pending CN105238555A (en) | 2014-06-09 | 2014-06-09 | Antioxidation crystallization tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105238555A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701314A (en) * | 2017-02-17 | 2017-05-24 | 无锡市新耀生物工程技术有限公司 | Fish oil winterizing, fractioning, crystallizing and growing reaction tank |
| CN109631613A (en) * | 2018-11-26 | 2019-04-16 | 杨胜明 | For building the low noise cross flow cooling tower of HVAC |
-
2014
- 2014-06-09 CN CN201410250052.4A patent/CN105238555A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701314A (en) * | 2017-02-17 | 2017-05-24 | 无锡市新耀生物工程技术有限公司 | Fish oil winterizing, fractioning, crystallizing and growing reaction tank |
| CN106701314B (en) * | 2017-02-17 | 2023-10-27 | 无锡市新耀生物工程技术有限公司 | Crystal growing reaction tank for winterization, fractionation and crystallization of fish oil |
| CN109631613A (en) * | 2018-11-26 | 2019-04-16 | 杨胜明 | For building the low noise cross flow cooling tower of HVAC |
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Legal Events
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| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160113 |
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| WD01 | Invention patent application deemed withdrawn after publication |