CN205974461U - Vegetable wool olein smelts equipment of using - Google Patents

Vegetable wool olein smelts equipment of using Download PDF

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Publication number
CN205974461U
CN205974461U CN201620961169.8U CN201620961169U CN205974461U CN 205974461 U CN205974461 U CN 205974461U CN 201620961169 U CN201620961169 U CN 201620961169U CN 205974461 U CN205974461 U CN 205974461U
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CN
China
Prior art keywords
tank
oil
aquation
crude oil
water washing
Prior art date
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
Application number
CN201620961169.8U
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Chinese (zh)
Inventor
马振国
常乐
王馨
马建国
张甜甜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ningxia Somiya Eco Agriculture Technology Co Ltd
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Ningxia Somiya Eco Agriculture Technology Co Ltd
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Priority to CN201620961169.8U priority Critical patent/CN205974461U/en
Application granted granted Critical
Publication of CN205974461U publication Critical patent/CN205974461U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model provides a vegetable wool olein smelts equipment of using, including the intermittent type aquation device that comes unstuck, dehydration discoloring device and deacidification deodorization device, the intermittent type aquation is come unstuck the device and is included the aquation jar, the alkali refining jar, water washing tank, water tank and alkali case, the aquation jar, the alkali refining jar, it connects to pass through oil pipe with water washing tank, the water tank leads to pipe with aquation jar and water washing tank to be connected, dehydration discoloring device is including the decoloration jar, heating device and sediment piece filter, heating device's heat is supplied with by the boiler room, the decoloration jar is connected with sediment piece filter through oil pipe, water washing tank passes through oil pipe and is connected with the decoloration jar, deacidification deodorization device includes deacidification deodorization tower, the gassing ware, oil oil heat exchanger and heat conduction oil furnace, the decoloration jar is connected with deacidification deodorization tower through oil pipe, the gassing ware, oil oil enthalpy exchanger, the dress is joined in marriage with deacidification deodorization tower respectively to the heat conduction oil furnace. Adopt the utility model discloses a concise plant crude oil of physics, whole equipment fixing compact structure is perfect, and concise vegetable wool oil colours pool and taste are all relatively good.

Description

Vegetable crude oil refine equipment
Technical field:
This utility model is related to vegetable crude oil refining techniques field, particularly to a kind of vegetable crude oil refine equipment, should Equipment is mainly used in refine Semen Lini oil.
Technical background:
Form vegetable crude oil, the Main Ingredients and Appearance of Vegetable oil lipoprotein is mixed glycerol three after the primary squeezing of plant seed such as Semen Lini etc. The mixture of fatty acid, is the necessary nutrient substance of human body, and is often mixed with the non-sweet three ester compositions that quantity does not wait in crude oil, such as Free fatty, resin, pigment flavacin, tocopherol, protein, phospholipid etc., some are favourable to human body for these impurity, such as egg White matter, phospholipid etc., some are then harmful, such as flavacin.No matter favourable to human body or harmful, these materials with Greases, majority can affect grease color, abnormal smells from the patient, acid value and nutrition, and for this, squeezing or Extractive crudeoil have to pass through essence Refining, can eat for people.
Oil refining process popular in the world at present has chemical refining and two kinds of techniques of physical refining, so-called chemistry Refine refers to occur neutralization reaction to remove the fat in oil removing in oily pretreatment stage by adding a certain amount of alkali and free fatty Fat acid, forms soap stock and discharges;Physical refining refers to that P elements remove in oily pretreatment stage is to oil, and fatty acid is placed on Water vapour is used to remove the free fatty in degreasing under high temperature high vacuum state by way of distillation, in oils and fatss in deodorising process There is not chemical change in refining process, also known as distill acid stripping method.
Chemical refining deacidification, has oil while acid-base neutralization process and alkali occurs chemical reaction to generate soap, can cause The loss of oil, the soap of generation and oil also will take away part oil when separating, so the loss of oil is more during chemical refining deacidification; The side-product that chemical refining technique produces is soap stock, is not only worth and low also can produce sour odor pollution environment;Using chemistry essence Certain waste water and soap stock can be produced, the discharge of waste water brings certain impact to environmental protection during refining production technology;So most plant Thing oil processing businessman adopts the method refine crude oil of physical refining, but current physical refining process is not very ripe, refine The protection of the crude oil color and luster going out and mouthfeel and nutritional labeling is not fine, and the refinery practice of crude oil need to be improved.
Content of the invention:
In view of this it is necessary to provide a kind of vegetable crude oil refine equipment.
A kind of vegetable crude oil refine equipment, including batch hydration degumming device, dehydration and decolorization device and deacid-deodoring dress Put, batch hydration degumming device includes aquation glue kettle, alkali refining tank, water washing tank, water tank and alkali case, aquation glue kettle, alkali refining tank, Connected by oil pipe with water washing tank, water tank is connected by water pipe with aquation glue kettle and water washing tank, dehydration and decolorization device includes taking off Water decolorization tank, heater and slag piece filter, the heat of heater is supplied by boiler room, dehydration and decolorization tank pass through oil pipe with Slag piece filter connects, and water washing tank is connected with dehydration and decolorization tank by oil pipe, and deacid-deodoring device includes deacid-deodoring tower, gassing Device, oil-oil heat exchanger and heat-conducting oil furnace, dehydration and decolorization tank is connected with deacid-deodoring tower by oil pipe, and deaerator, oil-oil heat is changed Hot device, heat-conducting oil furnace are equipped with deacid-deodoring tower respectively.
Preferably, batch hydration degumming device also includes degumming filter, and degumming filter passes through oil pipe and aquation degumming Tank connects.
Preferably, vegetable crude oil refine equipment also include fridge, first dewaxing tank and second dewaxing tank, fridge with First dewaxing tank and the second dewaxing tank are equipped with, and the first dewaxing tank and the second dewaxing tank are passed through oil pipe and be equipped with deacid-deodoring tower.
Preferably, vegetable crude oil refine equipment also includes saltout tank and pump of saltouing, and saltouts tank with pump of saltouing and passes through oil pipe It is connected with water washing tank.
Preferably, vegetable crude oil refine equipment also includes precipitation tank, and precipitation tank is top and bottom is dished lid Cylindrical structure, is provided with heater in tank, top dished lid is provided with vacuum tube, manhole and illuminating lamp, dished lid also sets It is equipped with vacuum meter interface, in tank, bottom is additionally provided with live (open) steam jet pipe.
Preferably, the main body of aquation glue kettle, alkali refining tank and water washing tank is a cone bottomed cylinder tank body of band, internal It is respectively arranged with shaft, equipped with 2~4 pairs of paddle formula stirring wings on axle;Equipped with a stirring wing inside conical bottom, shaft is by installing Drive on cover.
Preferably, the transmission speed of the actuating device on the cover of aquation glue kettle, alkali refining tank and water washing tank is two grades, leans on At nearly tank wall inner edge, it is equiped with indirect steam heating pipe arranged vertically.
Preferably, the saltout bottom of tank is conical shell, and tank body is provided with agitating device, is provided with heating coil in tank.
Refine can be carried out to Semen Lini crude oil using this utility model, the Semen Lini oil color and luster that refine goes out is not bright muddy, And remain the nutritional labeling of Semen Lini oil.
Brief description:
Fig. 1 is the structural representation of vegetable crude oil refine equipment.
In figure:Aquation glue kettle 10, alkali refining tank 11, water washing tank 12, water tank 13, alkali case 14, degumming filter 15, dehydration are de- Color tank 20, heater 21, slag piece filter 22, deacid-deodoring tower 30, tank 40 of saltouing, pump 41 of saltouing.
Specific embodiment:
Refer to Fig. 1, vegetable crude oil refine equipment includes batch hydration degumming device, dehydration and decolorization device and deacidification and takes off Smelly device, batch hydration degumming device includes aquation glue kettle 10, alkali refining tank 11, water washing tank 12, water tank 13 and alkali case 14, aquation Glue kettle 10, alkali refining tank 11 and water washing tank 12 are connected by oil pipe, and water tank 13 passes through water with aquation glue kettle 10 and water washing tank 12 Pipe connects, and dehydration and decolorization device includes dehydration and decolorization tank 20, heater 21 and slag piece filter 22, the heat of heater 21 Supplied by boiler room, dehydration and decolorization tank 20 is connected with slag piece filter 22 by oil pipe, it is de- with dehydration that water washing tank 12 passes through oil pipe Color tank 20 connects, and deacid-deodoring device includes deacid-deodoring tower 30, deaerator, oil-oil heat exchanger and heat-conducting oil furnace, dehydration and decolorization Tank 20 is connected with deacid-deodoring tower 30 by oil pipe, deaerator, oil-oil heat exchanger, heat-conducting oil furnace respectively with deacid-deodoring tower Join 30 dresses.
Batch hydration degumming device also includes degumming filter 15, and degumming filter 15 passes through oil pipe and aquation glue kettle 10 Connect.
Vegetable crude oil refine equipment also includes saltout tank 40 and pump 41 of saltouing, and saltouts tank 40 with pump 41 of saltouing and passes through oil pipe It is connected with water washing tank 12.The saltout bottom of tank 40 is conical shell, and tank body is provided with agitating device, is provided with heating dish in tank Pipe.Vegetable crude oil refine equipment also include fridge, first dewaxing tank and second dewaxing tank, fridge with first dewax tank and Second dewaxing tank is equipped with, and the first dewaxing tank and the second dewaxing tank are passed through oil pipe and be equipped with deacid-deodoring tower 30.
Vegetable crude oil refine equipment also includes precipitation tank, and precipitation tank is the cylinder knot that top and bottom are dished lid Structure, is provided with heater in tank, top dished lid is provided with vacuum tube, manhole and illuminating lamp, and dished lid is additionally provided with vacuum Table interface, in tank, bottom is additionally provided with live (open) steam jet pipe.The main body of hydration tank glue kettle 10, alkali refining tank 11 and water washing tank 12 is One cone bottomed cylinder tank body of band, inside is respectively arranged with shaft, equipped with 2~4 pairs of paddle formula stirring wings on axle;In conical bottom Equipped with a stirring wing, shaft is by the drive being arranged on cover in portion.
The transmission speed of the actuating device on the cover of aquation glue kettle 10, alkali refining tank 11 and water washing tank 12 is two grades, leans on At nearly tank wall inner edge, it is equiped with indirect steam heating pipe arranged vertically.
Vegetable crude oil first passes through crude oil filter, removes well cuts, is then sent to aquation glue kettle 10, and phosphoric acid is simultaneously fixed Amount injection wherein, is fully reacted after mixing, makes non-hydratable phospholipid be converted into hydrated phospholipid, be then quantitatively adding water or light alkali warp Standing separation after mixing.The heavy phase isolated pumps out workshop through soap stock and removes soap stock basin;Light phase oil divides after hot water washing, point Go after oil after water to decolour.Oil after decolouring pumps in deaerator by pump with constant flow, and the flow of oil passes through effusion meter To adjust.In deaerator, oil is sprayed by the multiple nozzles on feed pipe, maintains the absolute pressure of about 3mmHg in deaerator The condition of high vacuum degree of power is so that a small amount of air penetrating in oil is released.Oil out, is pumped to oil from deaerator -- oily heat exchange Device, carries out heat exchange with the deep fat out from deacid-deodoring tower 30, is heated at least 120 DEG C.From oil -- oil heat exchanger goes out Come, oil flows into hotline heater, is heated to 260 DEG C, conduction oil is heated to 290 DEG C in heat-conducting oil furnace, in whole process Middle recycling.Hot treats that deodorised oil enters into assembled deacid-deodoring tower 30 from hotline heater, uses in packing section Directly vapour is stripped off fatty acid volatile stink substance relative with other, then from board-like section of deodorize of inflow and heat decoloring.Deacidification Deodorize operates under the vacuum state of high temperature and 3mmHg absolute pressure, and vacuum is passed through a level Four vacuum pump system and produced and protect Hold.Oil after deacid-deodoring is discharged from combination type deodorizing tower, pumps into heat exchanger and treats deodorised oil and carry out heat exchange, enters back into Cooler, is cooled directly with water, not higher than 70 DEG C of oil temperature after cooling, finally by fine filter, carries out insurance and filters, product oil of restoring Holding vessel.
Refine can be carried out to Semen Lini crude oil using this utility model, the Semen Lini oil color and luster that refine goes out is not bright muddy, And remain the nutritional labeling of Semen Lini oil.

Claims (8)

1. a kind of vegetable crude oil refine equipment it is characterised in that:Vegetable crude oil refine equipment includes batch hydration degumming dress Put, dehydration and decolorization device and deacid-deodoring device, batch hydration degumming device includes aquation glue kettle, alkali refining tank, water washing tank, water Case and alkali case, aquation glue kettle, alkali refining tank and water washing tank are connected by oil pipe, and water tank is passed through with aquation glue kettle and water washing tank Water pipe connects, and dehydration and decolorization device includes dehydration and decolorization tank, heater and slag piece filter, and the heat of heater is by boiler Room supplies, and dehydration and decolorization tank is connected with slag piece filter by oil pipe, and water washing tank is connected with dehydration and decolorization tank by oil pipe, deacidification Deodorization device includes deacid-deodoring tower, deaerator, oil-oil heat exchanger and heat-conducting oil furnace, and dehydration and decolorization tank passes through oil pipe and deacidification Deodorizing tower connects, and deaerator, oil-oil heat exchanger, heat-conducting oil furnace are equipped with deacid-deodoring tower respectively.
2. vegetable crude oil refine equipment as claimed in claim 1 it is characterised in that:Batch hydration degumming device also includes taking off Glue filter, degumming filter is connected with aquation glue kettle by oil pipe.
3. vegetable crude oil refine equipment as claimed in claim 1 or 2 it is characterised in that:Vegetable crude oil refine equipment is also Including fridge, the first dewaxing tank and the second dewaxing tank, fridge and the first dewaxing tank and the second dewaxing tank are equipped with, the first dewaxing Tank and the second dewaxing tank are passed through oil pipe and are equipped with deacid-deodoring tower.
4. vegetable crude oil refine equipment as claimed in claim 3 it is characterised in that:Vegetable crude oil refine equipment also includes Saltout tank and pump of saltouing, saltout tank and be connected with water washing tank by oil pipe with pump of saltouing.
5. vegetable crude oil refine equipment as claimed in claim 4 it is characterised in that:Vegetable crude oil refine equipment also includes Precipitation tank, precipitation tank is the cylindrical structure that top and bottom are dished lid, is provided with heater, on the dished lid of top in tank It is provided with vacuum tube, manhole and illuminating lamp, dished lid is additionally provided with vacuum meter interface, in tank, bottom is additionally provided with live (open) steam spray Pipe.
6. vegetable crude oil refine equipment as claimed in claim 5 it is characterised in that:Aquation glue kettle, alkali refining tank and washing The main body of tank is a cone bottomed cylinder tank body of band, and inside is respectively arranged with shaft, axle stirs equipped with 2~4 pairs of paddle formulas Wing;Equipped with a stirring wing inside conical bottom, shaft is by the drive being arranged on cover.
7. vegetable crude oil refine equipment as claimed in claim 6 it is characterised in that:Aquation glue kettle, alkali refining tank and washing The transmission speed of the actuating device on the cover of tank is two grades, at tank wall inner edge, is equiped with indirect steaming arranged vertically Vapour heating tube.
8. vegetable crude oil refine equipment as claimed in claim 4 it is characterised in that:Saltout tank bottom be conical shell, And tank body is provided with agitating device, in tank, it is provided with heating coil.
CN201620961169.8U 2016-08-28 2016-08-28 Vegetable wool olein smelts equipment of using Expired - Fee Related CN205974461U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620961169.8U CN205974461U (en) 2016-08-28 2016-08-28 Vegetable wool olein smelts equipment of using

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620961169.8U CN205974461U (en) 2016-08-28 2016-08-28 Vegetable wool olein smelts equipment of using

Publications (1)

Publication Number Publication Date
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107118845A (en) * 2017-05-15 2017-09-01 邵阳学院 A kind of food engineering oil refining process and its device
CN109181792A (en) * 2018-11-01 2019-01-11 广西南宁高斯特科贸有限公司 A kind of biofuel oil process equipment
CN111635820A (en) * 2020-05-11 2020-09-08 益海(连云港)粮油工业有限公司 Automatic unloading and automatic conveying system for materials in refining workshop

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107118845A (en) * 2017-05-15 2017-09-01 邵阳学院 A kind of food engineering oil refining process and its device
CN109181792A (en) * 2018-11-01 2019-01-11 广西南宁高斯特科贸有限公司 A kind of biofuel oil process equipment
CN111635820A (en) * 2020-05-11 2020-09-08 益海(连云港)粮油工业有限公司 Automatic unloading and automatic conveying system for materials in refining workshop
CN111635820B (en) * 2020-05-11 2023-03-14 益海(连云港)粮油工业有限公司 Automatic unloading and automatic conveying system for materials in refining workshop

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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

Granted publication date: 20170222

Termination date: 20200828

CF01 Termination of patent right due to non-payment of annual fee