CN204865692U - Maize olein smelts decoloration with mixing jar in advance - Google Patents
Maize olein smelts decoloration with mixing jar in advance Download PDFInfo
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- CN204865692U CN204865692U CN201520666089.5U CN201520666089U CN204865692U CN 204865692 U CN204865692 U CN 204865692U CN 201520666089 U CN201520666089 U CN 201520666089U CN 204865692 U CN204865692 U CN 204865692U
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- premixing tank
- grease
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- carclazyte
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Abstract
The utility model provides a maize olein smelts decoloration with mixing jar in advance, vacuum pump -line pass the vacuum aspirating hole and mix a jar intercommunication in advance, carclazyte charge -in pipeline passes the carclazyte feed port and mixes a jar intercommunication in advance, it passes the inlet port and mixes a jar intercommunication in advance to advance the oil pipe way, flowline passes the oil outlet and mixes a jar intercommunication in advance. The grease is through upper and lower twice mixture, and a grease keeps in close touch with carclazyte, activated carbon in mixing in advance jar, misce bene, abundant reaction, has effectually restrained the carclazyte caking, has adhered to phenomenons such as a jar wall, deposit, jam to appear, has created good condition for the further processing utilization of grease. Should mix in advance simultaneously and jar utilize self kinetic energy of adding the grease to realize stirring function, and not need the motor to drive the stirring wing or let in the direct steam stirring, save the energy resource consumption.
Description
Technical field
The utility model relates to refining of maize oil field, particularly relates to a kind of refining of maize oil decolouring premixing tank.
Background technology
Grease-decolor also claims absorption method to decolour or adsorption treatment, the main purpose of edible oil decolouring is in order to the accessory substance (comprising multiple pollutant and harmful substance) in degrease, this not only can meet the demand of people to edible oil security guard, also for the further processing and utilization of grease creates good condition.The activated decoloration (additive is atlapulgite and appropriate activated carbon) occurred this year is comparatively advanced grease-decolor method, carclazyte, it is the key point that oil and fat refining decolours that active carbon and grease fully mix, if mix uneven, then grease-decolor effect is bad, but also there will be carclazyte caking, attachment tank skin, deposition, blockings etc. now, increase live (open) steam at the bottom of paddle on the shaft that existing blending tank passes through when stirring or tank to seethe and mix, these two kinds of hybrid modes all Shortcomings: shaft agitating mode can make the mixture homogeneity of carclazyte and grease not high, the live (open) steam mode of seething affects moisture removal in fats and oils processing, increases oil quality destabilizing factor, and above two kinds of modes need outside to provide electric power or steam in mixed process, increase energy resource consumption.
Summary of the invention
For existing equipment Problems existing and deficiency, the utility model provides a kind of refining of maize oil decolouring premixing tank, comprising: for the premixing tank that takes up rich mixture and the vacuum suction pipeline, carclazyte feed pipe, inflow pipeline, the flowline that are communicated with described premixing tank respectively; Described premixing tank top is provided with vacuum pumping hole, carclazyte charging hole, fuel feed hole, and described premixing tank sidewall is provided with oil outlet;
Described vacuum suction pipeline is communicated with described premixing tank through described vacuum pumping hole; Described carclazyte feed pipe is communicated with described premixing tank through described carclazyte charging hole; Described inflow pipeline is communicated with described premixing tank through described fuel feed hole; Described flowline is communicated with described premixing tank through described oil outlet.
Preferably, described vacuum suction pipeline is inserted in described premixing tank through described vacuum pumping hole, and described vacuum suction pipeline opening is arranged at grease ullage in described premixing tank.
Preferably, at the grease ullage of described premixing tank inside, be provided with baffle plate near described vacuum suction pipeline opening;
Described baffle plate is herringbone.
Preferably, described inflow pipeline is provided with straight length and arc-shaped coil section connected vertically with described straight length;
The straight length of described inflow pipeline to be vertically inserted in described premixing tank in grease liquid through described fuel feed hole, makes described arc-shaped coil section invade in grease;
The end seal of described arc-shaped coil section, the body of described arc-shaped coil section is provided with several lower nozzle, and described lower nozzle is to described premixing tank base injcction grease.
Preferably, described arc-shaped coil section is apart from 30-40 centimetre bottom described premixing tank.
Preferably, the quantity of described lower nozzle is 3-4, and is evenly distributed in described arc-shaped coil section;
The grease direction that described lower nozzle sprays is spray perpendicular to described premixing tank baseplane.
Preferably, described straight length is provided with top nozzle above grease liquid level;
The setting position of described top nozzle is positioned at described premixing tank when normally working, the 5-10 centimeters of grease ullage, and the opening of described top nozzle is towards the center line of described premixing tank.
Preferably, flowline comprises: horizontal segment and vertical section connected vertically with described horizontal segment;
Described vertical section to be divided in liquid level vertical section under vertical section and liquid level by the connecting portion of described horizontal segment and described vertical section;
Under described horizontal segment and described liquid level, vertical section is arranged at described premixing tank grease liquid level bottom, and in described liquid level, the upper shed of vertical section is extended outside grease liquid level.
Preferably, under described liquid level, the under shed of vertical section is positioned at 20-30 centimeters above arc-shaped coil section;
In described liquid level, the length of vertical section is 10-15 centimetre.
As can be seen from the above technical solutions, the utility model has the following advantages:
Grease is through upper and lower twice mixing, in premixing tank grease with carclazyte, activated carbon close contact, mix, fully react, effectively inhibit carclazyte to lump, adhere to the phenomenon appearance such as tank skin, deposition, blocking, for the further processing and utilization of grease creates good condition.This premixing tank utilizes self kinetic energy adding grease to realize agitating function simultaneously, does not need driven by motor stirring wing or pass into live (open) steam to stir, and saves energy resource consumption.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical solution of the utility model, be briefly described to the accompanying drawing used required in description below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the overall structure figure of refining of maize oil decolouring premixing tank.
Detailed description of the invention
For making the purpose of this utility model, feature, advantage can be more obvious and understandable, below in conjunction with the accompanying drawing in this specific embodiment, technical scheme in the utility model is clearly and completely described, obviously, the embodiments described below are only the utility model part embodiments, and the embodiment of not all.Based on the embodiment in this patent, those of ordinary skill in the art are not making other embodiments all obtained under creative work prerequisite, all belong to the scope of this patent protection.
The utility model provides a kind of refining of maize oil decolouring premixing tank, refer to shown in Fig. 1, comprising: for the premixing tank 1 that takes up rich mixture and the vacuum suction pipeline 3, carclazyte feed pipe 2, inflow pipeline 4, the flowline that are communicated with premixing tank 1 respectively; Premixing tank 1 top is provided with vacuum pumping hole, carclazyte charging hole, fuel feed hole, and premixing tank sidewall is provided with oil outlet;
Vacuum suction pipeline 3 is communicated with premixing tank 1 through vacuum pumping hole, and vacuum suction pipeline 3 connects vacuum extraction system, extracts air in premixing tank 1 out, keeps vacuum in premixing tank 2; Carclazyte feed pipe 2 is communicated with premixing tank 1 through carclazyte charging hole, carclazyte is entered in premixing tank 1 by carclazyte feed pipe 2 and mixes with grease; Inflow pipeline 4 is communicated with premixing tank 1 through fuel feed hole, preferably, is entered by premixing tank 1 top edge; Flowline is communicated with premixing tank 1 through oil outlet.
Inflow pipeline 4 is provided with straight length 41 and arc-shaped coil section 42 connected vertically with straight length 41; The straight length 41 of inflow pipeline to be vertically inserted in premixing tank 1 in grease liquid through fuel feed hole, makes arc-shaped coil section 42 invade in grease; The end seal of arc-shaped coil section 42, the body of arc-shaped coil section 42 is provided with several lower nozzle 8, and lower nozzle 8 is to premixing tank 1 base injcction grease.Grease to be processed pumps in premixing tank 1 from inflow pipeline 4 through oil pump, and is delivered to lower nozzle 8 place.Arc-shaped coil section 42 is apart from 30-40 centimetre bottom premixing tank 1.
The quantity of lower nozzle 8 is 3-4, and is evenly distributed in arc-shaped coil section 42; The grease direction that lower nozzle 8 sprays is spray perpendicular to premixing tank 1 baseplane.Grease sprays rear formation liquid stream from lower nozzle 8 can have layer to stir tank base, and grease in tank is fully mixed with the mixture of activated carbon with the carclazyte fallen into from carclazyte feed pipe, effectively prevents bottom settlings simultaneously.
Straight length 41 is provided with top nozzle 6 above grease liquid level 7;
The setting position of top nozzle 6 is positioned at premixing tank 1 when normally working, the 5-10 centimeters on grease liquid level 7 top, and the opening of top nozzle 6 is towards the center line of premixing tank 1.The quantity of top nozzle 6 is one, is mainly used in oil-feed and to the carclazyte spray that ullage newly adds, makes it mix with grease fast, reduce the generation of carclazyte attachment on tank skin.
Flowline comprises: horizontal segment 91 and vertical section connected vertically with horizontal segment 91; Vertical section to be divided in liquid level vertical section 93 under vertical section 92 and liquid level by horizontal segment 91 and the connecting portion of vertical section; Under horizontal segment 91 and liquid level, vertical section 93 is arranged at premixing tank 1 grease liquid level 7 bottom, and in liquid level, the upper shed of vertical section 92 is extended outside grease liquid level 7.
Under liquid level, the under shed of vertical section 93 is positioned at 20-30 centimeters above arc-shaped coil section 42; In liquid level, the length of vertical section 92 is 10-15 centimetre.
In liquid level, vertical section 92 extends outside grease liquid level 7, be communicated with the vacuum chamber of premixing tank 1, like this under the effect of negative pressure, the under shed of mixed grease from vertical section liquid level 93 is extracted to horizontal segment 91, flow into next operation from horizontal segment 91, horizontal segment 91 and vertical section adopt welding manner to be connected.
Vacuum suction pipeline 2 is inserted in premixing tank 1 through vacuum pumping hole, and 2 mouthfuls, vacuum suction pipeline to be arranged in premixing tank above grease liquid level 7.Above the grease liquid level 7 of premixing tank 1 inside, be provided with baffle plate 5 near vacuum suction pipeline opening; Baffle plate 5 is herringbone.Baffle plate 5 is mainly used in stopping that the carclazyte, grease etc. seethed in tank body splashes into vacuum suction pipeline 2, prevents foreign matter from entering vacuum extraction system.
The workflow of refining of maize oil decolouring premixing tank is:
After grease pumps into inflow pipeline, have that the nozzle on inflow pipeline 4 is spouting to be entered in premixing tank 1 respectively, top nozzle 6 falls into below pasta after spraying the carclazyte and activated carbon mixture adhesion that grease and carclazyte feed pipe road junction fall, and tentatively mixes.Meanwhile, spray grease in lower nozzle 8 and form liquid stream stirring tank base rich mixture, mixture fully mixes by the eddy current utilizing liquid to seethe formation.After mixing, grease is under the effect of seething, and enter flowline along flowline lower opening and upwards flow, on the left of flowline, opening flows into next operation.
Grease is through upper and lower twice mixing, in premixing tank grease with carclazyte, activated carbon close contact, mix, fully react, effectively inhibit carclazyte to lump, adhere to the phenomenon appearance such as tank skin, deposition, blocking, for the further processing and utilization of grease creates good condition.This premixing tank 1 utilizes self kinetic energy adding grease to realize agitating function simultaneously, does not need driven by motor stirring wing or pass into live (open) steam to stir, and saves energy resource consumption.
Energy-saving effect is estimated: according to 10m
3it is that 5kw calculates that tank body is equipped with stirring motor power, and power consumption per hour is 5kwh; Utilize live (open) steam to obtain above-mentioned effect, 0.8Mpa low-pressure steam 2000kg can be consumed when reality measuring and calculating every 24.
In this description, each embodiment adopts the mode of going forward one by one to describe, and what each embodiment stressed is the difference with other embodiments, between each embodiment identical similar portion mutually see.
To the above-mentioned explanation of the disclosed embodiments, professional and technical personnel in the field are realized or uses the utility model.To be apparent for those skilled in the art to the multiple amendment of these embodiments, General Principle as defined herein when not departing from spirit or scope of the present utility model, can realize in other embodiments.Therefore, the utility model can not be restricted to these embodiments shown in this article, but will meet the widest scope consistent with principle disclosed herein and features of novelty.
Claims (9)
1. a refining of maize oil decolouring premixing tank, is characterized in that, comprising: for the premixing tank that takes up rich mixture and the vacuum suction pipeline, carclazyte feed pipe, inflow pipeline, the flowline that are communicated with described premixing tank respectively; Described premixing tank top is provided with vacuum pumping hole, carclazyte charging hole, fuel feed hole, and described premixing tank sidewall is provided with oil outlet;
Described vacuum suction pipeline is communicated with described premixing tank through described vacuum pumping hole; Described carclazyte feed pipe is communicated with described premixing tank through described carclazyte charging hole; Described inflow pipeline is communicated with described premixing tank through described fuel feed hole; Described flowline is communicated with described premixing tank through described oil outlet.
2. refining of maize oil decolouring premixing tank according to claim 1, is characterized in that,
Described vacuum suction pipeline is inserted in described premixing tank through described vacuum pumping hole, and described vacuum suction pipeline opening is arranged at grease ullage in described premixing tank.
3. refining of maize oil decolouring premixing tank according to claim 2, is characterized in that,
At the grease ullage of described premixing tank inside, be provided with baffle plate near described vacuum suction pipeline opening;
Described baffle plate is herringbone.
4. refining of maize oil decolouring premixing tank according to claim 1, is characterized in that,
Described inflow pipeline is provided with straight length and arc-shaped coil section connected vertically with described straight length;
The straight length of described inflow pipeline to be vertically inserted in described premixing tank in grease liquid through described fuel feed hole, makes described arc-shaped coil section invade in grease;
The end seal of described arc-shaped coil section, the body of described arc-shaped coil section is provided with several lower nozzle, and described lower nozzle is to described premixing tank base injcction grease.
5. refining of maize oil decolouring premixing tank according to claim 4, is characterized in that,
Described arc-shaped coil section is apart from 30-40 centimetre bottom described premixing tank.
6. refining of maize oil decolouring premixing tank according to claim 4, is characterized in that,
The quantity of described lower nozzle is 3-4, and is evenly distributed in described arc-shaped coil section;
The grease direction that described lower nozzle sprays is spray perpendicular to described premixing tank baseplane.
7. refining of maize oil decolouring premixing tank according to claim 4, is characterized in that,
Described straight length is provided with top nozzle above grease liquid level;
The setting position of described top nozzle is positioned at described premixing tank when normally working, the 5-10 centimeters of grease ullage, and the opening of described top nozzle is towards the center line of described premixing tank.
8. refining of maize oil decolouring premixing tank according to claim 4, is characterized in that,
Flowline comprises: horizontal segment and vertical section connected vertically with described horizontal segment;
Described vertical section to be divided in liquid level vertical section under vertical section and liquid level by the connecting portion of described horizontal segment and described vertical section;
Under described horizontal segment and described liquid level, vertical section is arranged at described premixing tank grease liquid level bottom, and in described liquid level, the upper shed of vertical section is extended outside grease liquid level.
9. refining of maize oil decolouring premixing tank according to claim 8, is characterized in that,
Under described liquid level, the under shed of vertical section is positioned at 20-30 centimeters above arc-shaped coil section;
In described liquid level, the length of vertical section is 10-15 centimetre.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520666089.5U CN204865692U (en) | 2015-08-31 | 2015-08-31 | Maize olein smelts decoloration with mixing jar in advance |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520666089.5U CN204865692U (en) | 2015-08-31 | 2015-08-31 | Maize olein smelts decoloration with mixing jar in advance |
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| CN204865692U true CN204865692U (en) | 2015-12-16 |
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| CN201520666089.5U Active CN204865692U (en) | 2015-08-31 | 2015-08-31 | Maize olein smelts decoloration with mixing jar in advance |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105597607A (en) * | 2016-03-14 | 2016-05-25 | 肖纯庆 | Oil and carclazyte mixer with carclazyte vacuum suction and automatic pre-blending mechanism |
| CN115627195A (en) * | 2022-10-18 | 2023-01-20 | 河北三佳食用植物油有限公司 | Corn oil refining and decoloring device and process thereof |
-
2015
- 2015-08-31 CN CN201520666089.5U patent/CN204865692U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN115627195A (en) * | 2022-10-18 | 2023-01-20 | 河北三佳食用植物油有限公司 | Corn oil refining and decoloring device and process thereof |
| CN115627195B (en) * | 2022-10-18 | 2024-05-31 | 河北三佳食用植物油有限公司 | Corn oil refining and decoloring device and process thereof |
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