CN103834471A - Multifunctional efficient edible oil decolorizing pot - Google Patents
Multifunctional efficient edible oil decolorizing pot Download PDFInfo
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- CN103834471A CN103834471A CN201210484563.3A CN201210484563A CN103834471A CN 103834471 A CN103834471 A CN 103834471A CN 201210484563 A CN201210484563 A CN 201210484563A CN 103834471 A CN103834471 A CN 103834471A
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- pipe
- oil
- tank body
- stirring
- decolorizing
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Abstract
The invention discloses a multifunctional efficient edible oil decolorizing pot. According to the decolorizing pot, the mechanical stirring is replaced with the hydraulic rotation principle and the pneumatic composite flow-mixing stirring; meanwhile, the superheated steam stirring is adopted, so that hazardous substances during a heating process are discharged through a vacuum pipe. Thus, a simple deodorization effect is obtained. Edible crude oil with high quality can be eaten after being dehydrated by the decolorizing pot. A carclazyte pipe is arranged at a pot body and can be applied to a continuous or intermittent decolorizing process. After the edible oil enters the pot body, the rotational energy of the edible oil is generated through a fixed rotator; the switching is carried out by utilizing an arranged decolorizing pump through a by-pass pipe, so that the purposes of circulatory decolorizing and oil discharging are realized. When the edible oil passes through a dynamic stirring device, the flowing mixing function of the edible oil in the pot body is carried out. The superheated steam is taken as a direct steam for stirring, so that the hazardous substances and peculiar odors generated during the stirring process are discharged through the vacuum pipe; meanwhile, the deodorization effect is obtained.
Description
Technical field:
The product the present invention relates to, is widely used in the decolouring technology field in food oils engineering refining procedure.
Background technology:
The grease processing enterprise food oils refining procedure edible oil dewaxing degreasing of domestic various scales is not ideal enough; Dewaxing degreasing is poor easily causes that edible oil color is partially dark, transparency is low, congealing point is low, affects edible oil quality.In food oils refining process, need to decolour to grease; Decolouring pot is the necessaries of bleaching process.The shortcomings such as Decolouring pot is all to adopt mechanical stirring at present, and this traditional alr mode cost is high, and easily bad, maintenance bothers, vacuum keep difficulty is large; The product that this project is related, can address the above problem generation.
Summary of the invention:
The product that this project is related, adopts surge Principle of Rotating and pneumatic compound mixed flow stirring replacement mechanical stirring; The maintenance of its vacuum tightness is guaranteed.Adopt superheated vapour to stir simultaneously, discharge by valve tube owing to producing objectionable impurities in heat-processed; Can reach simple deodorising effect.If the edible crude oil of high-quality, by being edible after Decolouring pot vacuum hydro-extraction.This equipment tank body is provided with carclazyte pipe, can be used for continuity or intermittent decoloration process.Edible oil enters in tank body, makes it produce rotation energy by fixing turner.The decolouring pump that utilization is provided with, switches by bypass pipe, makes to reach circulation decolouring and fuel-displaced object, when by Pneumatic mixing device, makes the edible oil in tank body produce mixed flow effect.Due to adopt superheated vapour be open steam as stirring, the objectionable impurities producing in whipping process and gas with foreign flavor; Valve tube through being provided with is discharged, and reaches the effect of deodorization simultaneously.
Accompanying drawing explanation:
Below in conjunction with drawings and Examples, the present invention is further described, and Fig. 1 is the related product structure schematic diagram of this project; Fig. 2 is the structure iron of fixing turner.
As shown in Figure 1: oil outlet pipe 1, lower cone 2, special-shaped open steam jet pipe 3, fixing turner 4, oil-feed are responsible for that 5 temperature meter bases 6, open steam jet pipe 7, heating cage pipe 8, tank body 9, carclazyte pipe 10, visor 11, valve tube 12, vacuum meter take over 13, access opening 14, end socket 15, feet 16, cage pipe support 17, exhaust steam goes out pipe 18, flow deflector 19, nozzle 20, ring pipe 21, pipe connecting 22.
Embodiment:
As shown in Figure 1, tank body 9 outsides are provided with temperature meter base 6, feet 16 to the related product of this project.Tank body 9 inside are provided with heating cage pipe 8, and steam inlet is located at tank body 9 outsides and is convenient to steam connection; Exhaust steam goes out pipe 18 and is arranged on heating cage pipe 8 belows, is opened on lower cone 2.Heating cage pipe 8 supports 17 by cage pipe and is fixed on tank interior.Tank body 9 inside are provided with three fixing turners 4, and interface is on oil-feed supervisor 5; The below of every fixing turner 4 is provided with open steam jet pipe 7; Open steam jet pipe 7 is opened on tank body 9 outsides and is convenient to steam connection.Tank body 9 upper ends are connected to end socket 15, and end socket 15 is provided with carclazyte pipe 10, visor 11, valve tube 12, vacuum meter adapter 13, access opening 14; Tank body 9 lower ends are connected to lower cone 2, and lower cone 2 inside are provided with special-shaped open steam jet pipe 3, are opened on lower cone 2 outsides and are convenient to steam connection; Lower cone 2 lower ends are provided with oil outlet pipe 1, and edible oil decolouring circulation and bleached oil are exported through oil outlet pipe 1.Equipment, by feet 16, is arranged in system in vertical mode with horizontal plane.When batch technology, when utilizing vacuum system that edible oil is responsible for to 5 from oil-feed; Atlapulgite sucks in tank body 9 from carclazyte pipe 10.When continuous processing, through the mixing oil of premix, inject in tank body 9 from oil-feed supervisor 5 by oil pump.The decolouring pump that utilizes oil outlet pipe 1 to be provided with, injects oil-feed supervisor 5 by bypass pipe and circulates; Export from fixing turner 4, make mixing oil at the interior generation stirring action of tank body 9.Be input to special-shaped open steam jet pipe 3, open steam jet pipe 7 by superheated vapour simultaneously, through be arranged on open steam jet pipe 7 upwards with the downward nozzle of special-shaped open steam jet pipe 3; Carry out airflow stirring.The mix and blend that the Stirring producing with fixing turner 4 forms, makes to mix more evenly, decolorizing effect is more perfect.Mixing effect, can observe by the visor 11 being arranged on end socket 15.In decolorization, superheated vapour is carried at the objectionable impurities and the gas with foreign flavor that in whipping process, produce; Valve tube 12 through being provided with is discharged.Made the vacuum environment of tank body 9 interior generations by vacuum system, the height of vacuum tightness is taken over 13 vacuum meters that are provided with by vacuum meter, observes control.Because special-shaped open steam jet pipe 3 is provided with downward nozzle, atlapulgite can not cause job failure because of precipitation blocking pipe.Mixing oil heats cage pipe 8 steam heats by input, carries out indirect heating and open steam jet pipe 7 and upwards heats with the overheated open steam of special-shaped open steam jet pipe 3; By the effect of vacuum system, after atlapulgite adsorption; Qualified mixing oil after sampling, filters to leaf-type filter through the decolouring pump delivery being arranged on oil outlet pipe 1; Filter after bleached oil, enter subsequent processing depickling, deodorization procedures.
As shown in Figure 2, edible mixing oil enters from oil-feed supervisor 5 principle of fixing turner; Pipe connecting 22 enters ring pipe 21.At 8 spray orifices that are evenly distributed in of ring pipe 21, spray orifice front is provided with the flow deflector 19 that is centrifugal; In the time that edible mixing oil sprays from spray orifice, run into flow deflector and just form rotation and can be rotated stirring.
Claims (7)
1. multifunctional edible innage effect Decolouring pot, its feature: adopt surge Principle of Rotating and pneumatic compound mixed flow stirring replacement mechanical stirring; Owing to there being open steam in heat-processed, produce objectionable impurities and discharge by valve tube.Tank body is provided with carclazyte pipe, can be used for continuity or intermittent decoloration process.The decolouring pump that utilization is provided with, switches by bypass pipe, makes to reach circulation decolouring and fuel-displaced object.
2. device according to claim 1, tank body (9) outside is provided with temperature meter base (6), feet (16).
3. device according to claim 1, tank body (9) inside is provided with heating cage pipe 8, and steam inlet is located at tank body outside and is convenient to steam connection; Exhaust steam goes out pipe (18) and is arranged on heating cage pipe (8) below, is opened on lower cone (2).Support (17) by cage pipe and be fixed on tank interior.
4. device according to claim 1, tank body (9) inside is provided with three fixing turners (4), and interface is on oil-feed supervisor (5); Turner below is provided with open steam jet pipe (7); Open steam jet pipe is opened on tank body outside.
5. device according to claim 1, tank body (9) upper end is connected to end socket (15), and end socket is provided with carclazyte pipe (10), visor (11), valve tube (12), vacuum meter adapter (13), access opening (14).
6. device according to claim 1, tank body (9) lower end is connected to lower cone (2), lower cone inside is provided with special-shaped open steam jet pipe (3), and lower cone lower end is provided with oil outlet pipe (1), and edible oil decolouring circulation and bleached oil are exported through oil outlet pipe.
7. device according to claim 1, edible mixing oil enters from oil-feed supervisor (5); Pipe connecting (22) enters ring pipe (21).At 8 spray orifices that are evenly distributed in of ring pipe, spray orifice front is provided with the flow deflector (19) that is centrifugal; In the time that edible mixing oil sprays from spray orifice, run into flow deflector and just form rotation and can be rotated stirring.
Priority Applications (1)
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CN201210484563.3A CN103834471A (en) | 2012-11-26 | 2012-11-26 | Multifunctional efficient edible oil decolorizing pot |
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CN201210484563.3A CN103834471A (en) | 2012-11-26 | 2012-11-26 | Multifunctional efficient edible oil decolorizing pot |
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CN103834471A true CN103834471A (en) | 2014-06-04 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105254593A (en) * | 2015-09-21 | 2016-01-20 | 丹阳市助剂化工厂有限公司 | Two-stage efficient comprehensive decolorizing tank for epoxidized soybean oil production |
CN105597607A (en) * | 2016-03-14 | 2016-05-25 | 肖纯庆 | Oil and carclazyte mixer with carclazyte vacuum suction and automatic pre-blending mechanism |
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CN2258875Y (en) * | 1996-07-09 | 1997-08-06 | 满时勇 | Double layer secondary gas evolving and decolouriziing tower |
WO2007079981A2 (en) * | 2005-12-29 | 2007-07-19 | Süd-Chemie AG | Natural method for bleaching oils |
CN101185466A (en) * | 2007-12-18 | 2008-05-28 | 杨孟君 | Alkalization, decolorizing and deodorization integration pan for camellia oil precision machining |
CN101698643A (en) * | 2009-10-27 | 2010-04-28 | 天津市东大化工有限公司 | Boiling bleacher used in production process of sodium benzoate and operating process |
CN201686673U (en) * | 2010-04-16 | 2010-12-29 | 武汉友谊食品工程有限公司 | Steam-stirring layered continuous vacuum bleaching tower |
CN102277232A (en) * | 2011-06-29 | 2011-12-14 | 连云港通元机械有限公司 | Decoloration pot |
CN202181295U (en) * | 2011-08-16 | 2012-04-04 | 山东渤海实业股份有限公司 | Decoloration device for vegetable oil decoloration |
CN102676296A (en) * | 2012-06-05 | 2012-09-19 | 太仓市宝马油脂设备有限公司 | Grease decoloring system and continuous grease decoloring method |
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2012
- 2012-11-26 CN CN201210484563.3A patent/CN103834471A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
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CN2258875Y (en) * | 1996-07-09 | 1997-08-06 | 满时勇 | Double layer secondary gas evolving and decolouriziing tower |
WO2007079981A2 (en) * | 2005-12-29 | 2007-07-19 | Süd-Chemie AG | Natural method for bleaching oils |
CN101185466A (en) * | 2007-12-18 | 2008-05-28 | 杨孟君 | Alkalization, decolorizing and deodorization integration pan for camellia oil precision machining |
CN101698643A (en) * | 2009-10-27 | 2010-04-28 | 天津市东大化工有限公司 | Boiling bleacher used in production process of sodium benzoate and operating process |
CN201686673U (en) * | 2010-04-16 | 2010-12-29 | 武汉友谊食品工程有限公司 | Steam-stirring layered continuous vacuum bleaching tower |
CN102277232A (en) * | 2011-06-29 | 2011-12-14 | 连云港通元机械有限公司 | Decoloration pot |
CN202181295U (en) * | 2011-08-16 | 2012-04-04 | 山东渤海实业股份有限公司 | Decoloration device for vegetable oil decoloration |
CN102676296A (en) * | 2012-06-05 | 2012-09-19 | 太仓市宝马油脂设备有限公司 | Grease decoloring system and continuous grease decoloring method |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105254593A (en) * | 2015-09-21 | 2016-01-20 | 丹阳市助剂化工厂有限公司 | Two-stage efficient comprehensive decolorizing tank for epoxidized soybean oil production |
CN105254593B (en) * | 2015-09-21 | 2018-03-30 | 丹阳市助剂化工厂有限公司 | Epoxidized soybean oil production efficiently integrates bleacher with two level |
CN105597607A (en) * | 2016-03-14 | 2016-05-25 | 肖纯庆 | Oil and carclazyte mixer with carclazyte vacuum suction and automatic pre-blending mechanism |
CN105597607B (en) * | 2016-03-14 | 2018-01-02 | 肖纯庆 | Oil product and coated mixer with the automatic pre- blending mechanism of carclazyte vacuum suction |
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Application publication date: 20140604 |