CN108865428A - A kind of dewatering in oil and fat refining process - Google Patents

A kind of dewatering in oil and fat refining process Download PDF

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Publication number
CN108865428A
CN108865428A CN201810797880.8A CN201810797880A CN108865428A CN 108865428 A CN108865428 A CN 108865428A CN 201810797880 A CN201810797880 A CN 201810797880A CN 108865428 A CN108865428 A CN 108865428A
Authority
CN
China
Prior art keywords
grease
tubulation
salt
aqueous
dewatering
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.)
Pending
Application number
CN201810797880.8A
Other languages
Chinese (zh)
Inventor
谢其亮
熊维政
陈元明
李巧梅
杨治东
李维
张雁林
李蕾蕾
徐新莲
韩宗阳
夏建梅
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.)
Henan Lvda Camellia Oil Co Ltd
Henan Xinxian County Ling Rui Camellia Research Institute
Original Assignee
Henan Lvda Camellia Oil Co Ltd
Henan Xinxian County Ling Rui Camellia Research Institute
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Henan Lvda Camellia Oil Co Ltd, Henan Xinxian County Ling Rui Camellia Research Institute filed Critical Henan Lvda Camellia Oil Co Ltd
Priority to CN201810797880.8A priority Critical patent/CN108865428A/en
Publication of CN108865428A publication Critical patent/CN108865428A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Sewage (AREA)

Abstract

The present invention relates to the dewaterings in oil and fat refining process,It can effectively solve energy saving,Reduce production cost,Shorten the production cycle,Improve the quality problems of grease,Method is,By aqueous grease from the tubulation that dehydration lower box part is sent into bottom,There is fluid hole on tubulation,The partition with filter opening is laid flat above tubulation,Salt layer has been placed above in partition,Aqueous grease is by the salt layer on partition and partition constantly to top dewatering box output flow,Moisture in aqueous grease becomes common salt aqueous solution by salt absorption,Since the specific gravity of common salt aqueous solution is greater than grease,Common salt aqueous solution constantly flows downward,Grease constantly flows up,Make water-oil separating,The grease outlets that dewatered grease is dehydrated upper box part are sent into bleacher,Common salt aqueous solution collects discharge in dehydration lower box part,For the water scouring water after alkali refining,It economizes on resources,Reduce the pollution to environment.The method of the present invention is simple, easy to operate, high production efficiency, and dehydrating effect is good, and energy-saving and environmental protection.

Description

A kind of dewatering in oil and fat refining process
Technical field
The present invention relates to oil and fat refining fields, a kind of grease essence being especially dehydrated from the grease after alkali refining, washing Dewatering during refining.
Background technique
Currently, oil and fat refining includes physical refining and two kinds of chemical refining.Wherein, chemical refining includes alkali-refining deacidification, water Alkali, dehydration, decoloration, deodorization etc. are washed away, dehydration is essential in oil chemistry refining process.It mainly uses at present with lower section Method:
By after alkali refining, washing grease injection sealing heating tank in, be heated to 95~100 DEG C, be evacuated to -0.09mPa with Above, under the conditions of being stirred continuously, continue 3.5 hours or more, moisture is made constantly to volatilize to reach dehydration purpose(Standard provides moisture content Not higher than 0.10%).But the problem as present on method, dewatering time is long, and energy consumption is high, and at high cost, production efficiency is low, and protects Product quality is not demonstrate,proved, therefore improvement on dewatering and innovation are imperative.
Summary of the invention
For above situation, for the defect for overcoming the prior art, it is an object of the present invention to provide a kind of oil and fat refining process In dewatering, can effectively solve it is energy saving, reduce production cost, shorten the production cycle, improve the quality problems of grease.
The technical solution that the present invention solves is, the dewatering in a kind of oil and fat refining process is:It at room temperature, will be aqueous Grease has fluid hole, lays flat the partition with filter opening above tubulation from the tubulation that dehydration lower box part is sent into bottom on tubulation, every Plate has been placed above salt layer, aqueous grease by the salt layer on partition and partition constantly to top dewatering box output flow, Moisture in aqueous grease becomes common salt aqueous solution by salt absorption, since the specific gravity of common salt aqueous solution is greater than grease, saline solution Solution constantly flows downward, and grease constantly flows up, and makes water-oil separating, and dewatered grease goes out through being dehydrated the grease of upper box part Mouth is sent into bleacher, and common salt aqueous solution collects discharge in dehydration lower box part, for the water scouring water after alkali refining, economizes on resources, subtract Few pollution to environment.
The method of the present invention is simple, easy to operate, high production efficiency, and dehydrating effect is good, and energy-saving and environmental protection, it is economical and Social benefit is huge.
Detailed description of the invention
Fig. 1 is the structural front view of present device.
Fig. 2 is the sectional front view of present device.
Specific embodiment
Below in conjunction with concrete condition, elaborate to a specific embodiment of the invention.
In specific implementation, the dewatering in a kind of oil and fat refining process is the present invention, at room temperature, will with liquid pump Aqueous grease is placed in the tubulation that laterally there is gap in dewatering box bottom from bottom side feeding, and upward liquid out is evenly equipped on tubulation Hole is laid flat above tubulation equipped with the partition with filter opening, and the food at least occupying tank-volumes 9/10 is placed in cabinet above partition Salt, constitutes the salt layer that top is plane, and aqueous grease is constantly gone out to top dewatering box by the salt layer on partition and partition Mouthful flowing, for aqueous grease during coming into full contact with salt, it is water-soluble that moisture in aqueous grease by salt absorption becomes salt Liquid, since the specific gravity of common salt aqueous solution is greater than grease, common salt aqueous solution constantly flows downward, and grease constantly flows up, thus Making water-oil separating, water content≤0.03% of grease, the grease outlets that dewatered grease is dehydrated upper box part are sent into bleacher, Common salt aqueous solution collects in dehydration lower box part, and the sewage draining exit for being periodically dehydrated lower box part, which is discharged, to be collected, for the washing after alkali refining It with water, economizes on resources, reduces the pollution to environment.
The dewatering box includes the sealing cover 2 on cabinet 1 and cabinet top, is provided with sewage draining exit 3, cabinet among the bottom of box Bottom is equipped with horizontal tubulation 4, has uniformly upward fluid hole on tubulation 4, the level being closely packed together is placed above in tubulation 4 Partition 5 is evenly equipped with the through-hole communicated with fluid hole on horizontal baffle(It is not indicated in figure), cabinet side is equipped with to be connected with tubulation Aqueous grease inlet tube 6, have grease outlets pipe 7 in the middle part of sealing cover 2, be opened in sealing cover on alternate with grease outlets pipe 7 is provided with Mouth 10, the salt layer filled with the plane at least accounting for tank-volumes 9/10 above horizontal baffle is added in salt with helixseal lid 8, aqueous grease enters tubulation, sprays to horizontal baffle again through fluid hole, enters salt layer through through-hole uniformly distributed on horizontal baffle, food Salt deposit after the moisture absorption in aqueous grease, will flow down through tubulation gap, flows into dewatering box bottom, is discharged by sewage draining exit;
The bottom of box of the dewatering box is in downward inclined plane shape, and sewage draining exit 3 is opened in the lowest point at bottom of box center, with benefit In the discharge of common salt aqueous solution;
The sealing cover 2 is in upward inclined plane shape, and grease outlets pipe 7 is opened in the highest point at sealing cover center, in favor of grease Discharge;
First valve 9-1 is housed on the grease outlets pipe 7, second valve 9-2, aqueous grease import are housed on sewage draining exit 3 On pipe 6 be equipped with third valve 9-3, be respectively used to control grease outlets pipe 7, sewage draining exit 3, aqueous grease inlet tube 6 unlatching or It closes.
From the above, it is seen that the present invention be by aqueous grease under the action of liquid pump, by aqueous grease through tubulation and Horizontal baffle is pumped into dedicated dehydration equipment(Dewatering box)In come into full contact with salt, the moisture in grease by salt absorption become Aqueous solution just constantly flows downward since common salt aqueous solution specific gravity is greater than grease, and grease constantly flows up, and makes water-oil separating, Reach the purpose of grease dehydration.
Through on probation, the method for the present invention small investment energy saving 1 times or more, reduces life due to being not required to heating and vacuum condition Produce 50% or more cost;Since this process carries out during being transferred to decoloration oil tank from the oil tank after washing, eliminate heated Journey, shortens the production cycle, and production efficiency improves 2 times or more;Since this process is not required to heat, can effectively prevent in the process The lost or generation chemical change of fractions, greatly reduces the pollution to environment;The salt water generated during this can make alkali Oily washing is used after refining, does not increase new pollution sources, will not generate secondary pollution, is energy-saving and environment friendly, economy and society It can Benefit.

Claims (5)

1. the dewatering in a kind of oil and fat refining process, which is characterized in that at room temperature, with liquid pump by aqueous grease the bottom of from Portion side is sent into and is placed in dewatering box bottom laterally and has in the tubulation in gap, is evenly equipped with upward fluid hole on tubulation, above tubulation It lays flat and the partition with filter opening is housed, be placed with the salt at least occupying tank-volumes 9/10 above partition in cabinet, constitute top For the salt layer of plane, aqueous grease by the salt layer on partition and partition constantly to top dewatering box output flow, it is aqueous For grease during coming into full contact with salt, the moisture in aqueous grease becomes common salt aqueous solution by salt absorption, due to salt The specific gravity of aqueous solution is greater than grease, and common salt aqueous solution constantly flows downward, and grease constantly flows up, thus make water-oil separating, Water content≤0.03% of grease, the grease outlets that dewatered grease is dehydrated upper box part are sent into bleacher, and common salt aqueous solution exists Dehydration lower box part collects, and the sewage draining exit for being periodically dehydrated lower box part, which is discharged, to be collected, and for the water scouring water after alkali refining, saves money The pollution to environment is reduced in source.
2. the dewatering in oil and fat refining process according to claim 1, which is characterized in that the dewatering box includes Cabinet(1)With the sealing cover on cabinet top(2), sewage draining exit is provided among the bottom of box(3), the bottom of box is equipped with horizontal tubulation (4), tubulation(4)On have uniformly upward fluid hole, tubulation(4)The horizontal baffle being closely packed together is placed above(5), horizontal The through-hole communicated with fluid hole is evenly equipped on partition, cabinet side is equipped with the aqueous grease inlet tube being connected with tubulation(6), close Capping(2)There is grease outlets pipe at middle part(7), with grease outlets pipe(7)Alternate be opened in is provided with helixseal lid on sealing cover Mouth is added in salt(10), salt layer filled with the plane at least accounting for tank-volumes 9/10 above horizontal baffle(8), aqueous grease Into tubulation, horizontal baffle is sprayed to again through fluid hole, enters salt layer through through-hole uniformly distributed on horizontal baffle, salt layer will be aqueous After moisture absorption in grease, tubulation gap is flowed down through, dewatering box bottom is flowed into, is discharged by sewage draining exit.
3. the dewatering in oil and fat refining process according to claim 1, which is characterized in that the case of the dewatering box Body bottom is in downward inclined plane shape, sewage draining exit(3)It is opened in the lowest point at bottom of box center, in favor of the row of common salt aqueous solution Out.
4. the dewatering in oil and fat refining process according to claim 1, which is characterized in that the sealing cover(2) In upward inclined plane shape, grease outlets pipe(7)It is opened in the highest point at sealing cover center, in favor of the discharge of grease.
5. the dewatering in oil and fat refining process according to claim 1, which is characterized in that the grease outlets pipe (7)It is upper that first valve is housed(9-1), sewage draining exit(3)It is upper that second valve is housed(9-2), aqueous grease inlet tube(6)It is upper equipped with the Three valves(9-3), it is respectively used to control grease outlets pipe(7), sewage draining exit(3), aqueous grease inlet tube(6)Unlatching or pass It closes.
CN201810797880.8A 2018-07-19 2018-07-19 A kind of dewatering in oil and fat refining process Pending CN108865428A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810797880.8A CN108865428A (en) 2018-07-19 2018-07-19 A kind of dewatering in oil and fat refining process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810797880.8A CN108865428A (en) 2018-07-19 2018-07-19 A kind of dewatering in oil and fat refining process

Publications (1)

Publication Number Publication Date
CN108865428A true CN108865428A (en) 2018-11-23

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112391228A (en) * 2020-11-10 2021-02-23 夏楚健 Animal oil refining method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102234525A (en) * 2010-05-07 2011-11-09 北京安耐吉能源工程技术有限公司 Method for reducing water content in hydrocarbon oil
CN204193565U (en) * 2014-10-28 2015-03-11 山东一诺生化科技有限公司 Distillation dehydration pretreatment unit
CN104893755A (en) * 2015-06-11 2015-09-09 洛阳绿景环保科技有限公司 Diesel oil dehydration device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102234525A (en) * 2010-05-07 2011-11-09 北京安耐吉能源工程技术有限公司 Method for reducing water content in hydrocarbon oil
CN204193565U (en) * 2014-10-28 2015-03-11 山东一诺生化科技有限公司 Distillation dehydration pretreatment unit
CN104893755A (en) * 2015-06-11 2015-09-09 洛阳绿景环保科技有限公司 Diesel oil dehydration device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112391228A (en) * 2020-11-10 2021-02-23 夏楚健 Animal oil refining method

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Application publication date: 20181123

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