CN110029020A - A kind of continuous fat melting of animal oil, dewatering process - Google Patents
A kind of continuous fat melting of animal oil, dewatering process Download PDFInfo
- Publication number
- CN110029020A CN110029020A CN201910294325.8A CN201910294325A CN110029020A CN 110029020 A CN110029020 A CN 110029020A CN 201910294325 A CN201910294325 A CN 201910294325A CN 110029020 A CN110029020 A CN 110029020A
- Authority
- CN
- China
- Prior art keywords
- dehydrator
- fat melting
- stir chamber
- melting
- fat
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/12—Production of fats or fatty oils from raw materials by melting out
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/12—Production of fats or fatty oils from raw materials by melting out
- C11B1/16—Production of fats or fatty oils from raw materials by melting out with steam
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Microbiology (AREA)
- Fats And Perfumes (AREA)
Abstract
The invention belongs to animal oil refining technical fields, more particularly to a kind of continuous fat melting of animal oil, dewatering process, it comprises the steps of: (1) by animal tallow Particle Breakage, animal tallow is delivered in mulser again and heats and stirs into slurries, then it sequentially enters in three fat melting dehydrators and further heats melting, three fat melting dehydrators are respectively the first fat melting dehydrator, second fat melting dehydrator, third fat melting dehydrator, the steam of second fat melting dehydrator is delivered to steam in the first fat melting dehydrator and heats as heat source into the first fat melting dehydrator, third fat melting dehydrator steam is delivered to steam in the second fat melting dehydrator and heats as heat source into the second fat melting dehydrator, degreasing is carried out by the slurries of third fat melting dehydrator to separate grease with the dregs of fat；The present invention conveys convenient, energy-saving and environmental protection, realizes the completely continuous manufacturing of animal oil tanning --- it is easy to implement computer automatic control.
Description
Technical field
The invention belongs to animal oil refining technical fields, and in particular to a kind of continuous fat melting of animal oil, dewatering process.
Background technique
The refinement of conventional animal grease has decoction method, solvent method, enzymatic isolation method, supercritical liquid extraction technique, and decoction method is
Grease will be made to release from adipose tissue by heating, and the technological temperature is lower, but long-time heating is needed, and
Since its fat lump is larger during tanning, it is difficult to it conveys, but semi-successive cultivation.Solvent rule will be moved by organic solvent
Object lipolyse, but the technique can make to be mixed into a large amount of chemical substance in fat, influence the quality of later period generation grease, enzymatic hydrolysis
Method is to be decomposed using animal fat, but the time required for the technique is longer, and supercritical liquid extraction technique is to utilize CO2Stream
Body extraction, but technique is cumbersome, and grease color extracted is poor, therefore the prior art needs further improve.
Summary of the invention
The purpose of the present invention is to provide a kind of conveyings convenient, the continuous fat melting of animal oil of energy-saving and environmental protection, dewatering process.
Based on above-mentioned purpose, the present invention is adopted the following technical scheme that:
A kind of continuous fat melting of animal oil, dewatering process, comprise the steps of:
(1) by animal tallow Particle Breakage, then animal tallow is delivered in mulser and heats and stir into slurries, then according to
Melting is further heated in three fat melting dehydrators of secondary entrance, three fat melting dehydrators are respectively the first fat melting dehydrator, second
Fat melting dehydrator, third fat melting dehydrator, the steam of the second fat melting dehydrator are delivered to steam conduct in the first fat melting dehydrator
Heat source is heated into the first fat melting dehydrator, and third fat melting dehydrator steam is delivered to steam in the second fat melting dehydrator
As heat source to heating into the second fat melting dehydrator, by the slurries of third fat melting dehydrator carry out degreasing by grease with
Dregs of fat separation；
(2) a portion grease in step (1) is reentered in mulser and animal tallow particle is mixed, wherein should
Amount of grease enters mulser as heat source and dilution, and another part grease is cooled to finished product.
Further, the mulser includes stir chamber, stirring cavity by baffle plate be divided into the first stir chamber with
Second stir chamber, the first stir chamber upper surface are equipped with emulsification machine inlet, and the first stir chamber upper surface is additionally provided with mulser oil inlet
Mouthful, baffle plate is equipped with overflow hole, is additionally provided with first motor above the first stir chamber upper surface, the output end of first motor protrudes into
Inside first stir chamber and the first impeller of connection, be additionally provided with the second motor above the second stir chamber upper surface, the second motor it is defeated
Outlet protrudes into and connects the second blade wheel inside the second stir chamber, and the second impeller outer is also arranged third stir chamber, and third stir chamber is solid
It is scheduled in the second stir chamber, third stirring chamber discharge port is additionally provided with below third stir chamber, the lower section of the second stir chamber is also set
There is mulser discharge port, the first stir chamber is also connected to the 4th heat exchanger feed inlet, the first stir chamber and the 4th heat exchanger feed inlet
Between be equipped with delivery pump, the 4th heat exchanger discharge port be connected to third stir chamber.
Further, the fat melting dehydrator includes seal casinghousing, and in a tubular form, lower part is in cavity type, shell for upper part of the housing
Sealing plate, respectively upper sealing panel and lower sealing plate, the edge and shell of the sealing plate are equipped with above and below in body top
Inner sidewall connection, by tubulation connection between upper sealing and lower sealing plate plate face, the upper end opening of tubulation is located at upper sealing panel,
The lower ending opening of tubulation is located at lower sealing plate, and fat melting dehydrator feed inlet is additionally provided on shell and the feed inlet is located at upper sealing panel
Top, be additionally provided with fat melting dehydrator steam inlet on shell and the steam inlet be located between upper sealing panel and lower sealing plate,
Be additionally provided with fat melting dehydrator drain port on shell, fat melting dehydrator drain port be located on lower sealing plate and with lower sealing plate phase
Neighbour, lower part of the housing top is additionally provided with fat melting dehydrator steam (vapor) outlet and the steam (vapor) outlet is located at the lower section of lower sealing plate, shell bottom
Portion is equipped with fat melting dehydrator discharge port.
Further, the diameter of the broken animal tallow particle is 3-10mm3, it is in the mulser plus
Hot temperature is 30-50 DEG C.
The steam of material can be passed through in the second fat melting dehydrator as heat source simultaneously in third fat melting dehydrator in the present invention
The material entered in the second fat melting dehydrator is heated, similarly, the vapor that the second fat melting is dehydrated interior material can be passed through
Material is heated as heat source in first fat melting dehydrator, thus reach energy saving, the purpose repeatedly utilized.The present invention
The middle finished product oil temperature by defatting machine separation is higher,, will in order to energy saving just needing to cool down can be delivered in product tank
The grease of part high temperature is passed through mulser, as mulser heat source, the efficiency for the emulsification not only accelerated, and also reduction thermal losses.
Detailed description of the invention
Fig. 1 is process flow chart of the invention；
Fig. 2 is the structural schematic diagram of emulsifier in the present invention；
Fig. 3 is the structural schematic diagram of fat melting dehydrator in the present invention；
Fig. 4 is upper sealing panel and tubulation aperture position relational graph.
Specific embodiment
The continuous fat melting of a kind of animal oil picture 1-4, dewatering process, comprise the steps of:
(1) by animal tallow Particle Breakage, then animal tallow is delivered in mulser and heats and stir into slurries, then according to
It is further heated in three fat melting dehydrators of secondary entrance, three fat melting dehydrators are respectively the first fat melting dehydrator, the second fat melting
Dehydrator, third fat melting dehydrator, the steam of the second fat melting dehydrator are delivered in the first fat melting dehydrator steam as heat source
It is heated into the first fat melting dehydrator, third fat melting dehydrator steam is delivered to steam conduct in the second fat melting dehydrator
Heat source is heated into the second fat melting dehydrator, carries out degreasing for grease and the dregs of fat by the slurries of third fat melting dehydrator
Separation；
(2) a portion grease in step (1) is reentered in mulser and animal tallow particle is mixed, wherein should
Amount of grease enters mulser as heat source and dilution, and another part grease is cooled to finished product.
The mulser 1 includes stir chamber, and stirring cavity is divided into the first stir chamber 105 and the by baffle plate 104
Two stir chambers 106,105 upper surface of the first stir chamber are equipped with emulsification machine inlet 101, and the first stir chamber upper surface is additionally provided with emulsification
103 baffle plate 104 of machine oil inlet is equipped with overflow hole 1041, is additionally provided with first motor above 105 upper surface of the first stir chamber
107, the output end of first motor 107 protrudes into 105 inside of the first stir chamber and connects the first impeller 108, in the second stir chamber 106
It is additionally provided with the second motor 109 above end face, the output end of the second motor 109 protrudes into inside the second stir chamber 106 and connects the second leaf
Wheel 110, the second impeller 110 are also arranged third stir chamber 111 outside, and third stir chamber 111 is fixed in the second stir chamber 106, the
The lower section of three stir chambers 111 is additionally provided with third stirring chamber discharge port 1111, and the lower section of the second stir chamber 106 is additionally provided with mulser and goes out
Material mouth 102, the first stir chamber 105 are also connected to the 4th heat exchanger feed inlet 1121, and the first stir chamber 105 and the 4th heat exchanger are fed
Delivery pump 113 is equipped between mouth 1121, the 4th heat exchanger discharge port 1122 is connected to third stir chamber 111.
Mulser 1 in use, opens first motor 107 and the second motor 109, by animal tallow particle from charging
Mouth is conveyed into stirring in the first stir chamber 105, meanwhile, grease enters from mulser oil inlet 103, grease and animal tallow particle
It is stirred together for, opens delivery pump 113 and the slurries after stirring are pumped into the 4th heat exchanger 112, the 4th heat exchanger 112 adds slurries
Enter in third stir chamber 111 after heat, futher stir, then flows into the second stir chamber 106 from third stirring chamber discharge port 1111
It is interior, then flowed out from mulser discharge port 102.
The fat melting dehydrator 2 includes seal casinghousing 201, and in a tubular form, lower part is in cavity type, shell on shell 201 top
It is equipped with sealing plate above and below in 201 tops, the edge of the sealing plate is connect with the inner sidewall of shell 201, the sealing plate
It for upper sealing panel 202 and lower sealing plate 203, is connected, is arranged by tubulation 204 between upper sealing panel 202 and lower 203 plate face of sealing plate
The upper end opening of pipe 204 is located at upper sealing panel 202, and the lower ending opening of tubulation 204 is located at lower sealing plate 203, also sets on shell 201
There is fat melting dehydrator feed inlet 205 and the feed inlet is located at the top of upper sealing panel 202, fat melting dehydration is additionally provided on shell 201
The device steam inlet 206 and steam inlet is located between upper sealing panel 202 and lower sealing plate 203, is additionally provided with fat melting on shell 201
Dehydrator drain port 209, fat melting dehydrator drain port 209 is located on lower sealing plate 203 and, shell adjacent with lower sealing plate 203
Fat melting dehydrator steam (vapor) outlet 207 is additionally provided with above 201 lower part of body and the steam (vapor) outlet is located at the lower section of lower sealing plate 203, shell
201 bottom of body is equipped with fat melting dehydrator discharge port 208.
Fat melting dehydrator 2 in use, material from fat melting dehydrator 2 enter, fall into lower part of the housing using tubulation 204, steam
Vapour enters from fat melting dehydrator steam inlet 206 and heats to the material in tubulation 204, then after condensing it is hydrophobic from fat melting dehydrator
Mouth 209 flows out, and after material enters the cavity of 201 lower part of shell, steam comes out from fat melting dehydrator steam (vapor) outlet 207.
Claims (4)
1. a kind of continuous fat melting of animal oil, dewatering process, which is characterized in that comprise the steps of:
(1) by animal tallow Particle Breakage, then animal tallow is delivered in mulser and heats and stir into slurries, then according to
Melting is further heated in three fat melting dehydrators of secondary entrance, three fat melting dehydrators are respectively the first fat melting dehydrator, second
Fat melting dehydrator, third fat melting dehydrator, the steam of the second fat melting dehydrator are delivered to steam conduct in the first fat melting dehydrator
Heat source is heated into the first fat melting dehydrator, and third fat melting dehydrator steam is delivered to steam in the second fat melting dehydrator
As heat source to heating into the second fat melting dehydrator, by the slurries of third fat melting dehydrator carry out degreasing by grease with
Dregs of fat separation；
(2) a portion grease in step (1) is reentered in mulser and animal tallow particle is mixed, wherein should
Amount of grease enters mulser as heat source and dilution, and another part grease is cooled to finished product.
2. the continuous fat melting of animal oil according to claim 1, dewatering system, which is characterized in that the mulser includes
Stir chamber, stirring cavity are divided into the first stir chamber and the second stir chamber by baffle plate, and the first stir chamber upper surface is equipped with cream
Change machine inlet, the first stir chamber upper surface is additionally provided with mulser oil inlet, and baffle plate is equipped with overflow hole, in the first stir chamber
First motor is additionally provided with above end face, the output end of first motor protrudes into inside the first stir chamber and the first impeller of connection, and second
The second motor is additionally provided with above stir chamber upper surface, the output end of the second motor, which protrudes into, connects the second blade inside the second stir chamber
Wheel, the second impeller outer are also arranged third stir chamber, and third stir chamber is fixed in the second stir chamber, and the lower section of third stir chamber is also
Chamber discharge port is stirred equipped with third, is additionally provided with mulser discharge port below the second stir chamber, the first stir chamber is also connected to the 4th
Heat exchanger feed inlet is equipped with delivery pump, the connection of the 4th heat exchanger discharge port between the first stir chamber and the 4th heat exchanger feed inlet
Third stir chamber.
3. the continuous fat melting of animal oil according to claim 1, dewatering system, which is characterized in that the fat melting dehydrator 2
Including seal casinghousing, in a tubular form, lower part is in cavity type for upper part of the housing, in upper part of the housing above and below be equipped with sealing plate, divide
Not Wei upper sealing panel and lower sealing plate, the inner sidewall of the edge of the sealing plate and shell connects, upper sealing and lower sealing plate plate face
Between connected by tubulation, the upper end opening of tubulation is located at upper sealing panel, and the lower ending opening of tubulation is located at lower sealing plate, on shell
It is additionally provided with fat melting dehydrator feed inlet and the feed inlet is located at the top of upper sealing panel, fat melting dehydrator steam is additionally provided on shell
The import and steam inlet is located between upper sealing panel and lower sealing plate, is additionally provided with fat melting dehydrator drain port, fat melting on shell
Dehydrator drain port is located on lower sealing plate and adjacent with lower sealing plate, is additionally provided with fat melting dehydrator steam above lower part of the housing
Outlet and the steam (vapor) outlet are located at the lower section of lower sealing plate, and housing bottom is equipped with fat melting dehydrator discharge port.
4. the continuous fat melting of the animal oil according to claim, dewatering process, which is characterized in that the broken animal
The diameter of lipochondrion is 3-10mm3, the heating temperature in the mulser is 30-50 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910294325.8A CN110029020A (en) | 2019-04-12 | 2019-04-12 | A kind of continuous fat melting of animal oil, dewatering process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910294325.8A CN110029020A (en) | 2019-04-12 | 2019-04-12 | A kind of continuous fat melting of animal oil, dewatering process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110029020A true CN110029020A (en) | 2019-07-19 |
Family
ID=67238205
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910294325.8A Pending CN110029020A (en) | 2019-04-12 | 2019-04-12 | A kind of continuous fat melting of animal oil, dewatering process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110029020A (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202107688U (en) * | 2011-06-09 | 2012-01-11 | 寿光市圣润化工有限公司 | Grease dehydrating equipment |
| CN203768325U (en) * | 2014-01-10 | 2014-08-13 | 重庆市昌鑫植物油有限责任公司 | Grease production line |
| CN204848801U (en) * | 2015-07-08 | 2015-12-09 | 王敏 | Airtight vacuum melting production facility of animal oil |
| CN206721163U (en) * | 2017-04-21 | 2017-12-08 | 南通海珥玛科技股份有限公司 | A kind of vapor dehydration column for grease post processing |
| CN108018115A (en) * | 2017-12-07 | 2018-05-11 | 莱阳易农农牧设备有限公司 | Animal fat refining process |
| CN207567192U (en) * | 2017-12-07 | 2018-07-03 | 莱阳易农农牧设备有限公司 | Animal fat refining equipment |
| CN108499509A (en) * | 2018-06-12 | 2018-09-07 | 深圳市朗坤环境集团股份有限公司 | The dry method system of raising prepares the devices and methods therefor of meat meal tankage and oil quality |
| CN108559621A (en) * | 2018-06-26 | 2018-09-21 | 新乡市红阳油脂工程技术有限公司 | A kind of animal fat Environment-friendlyextraction extraction method |
| CN208632480U (en) * | 2018-07-10 | 2019-03-22 | 郑州宏旺机械设备有限公司 | Animal oil extraction system with environment-friendly function |
-
2019
- 2019-04-12 CN CN201910294325.8A patent/CN110029020A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202107688U (en) * | 2011-06-09 | 2012-01-11 | 寿光市圣润化工有限公司 | Grease dehydrating equipment |
| CN203768325U (en) * | 2014-01-10 | 2014-08-13 | 重庆市昌鑫植物油有限责任公司 | Grease production line |
| CN204848801U (en) * | 2015-07-08 | 2015-12-09 | 王敏 | Airtight vacuum melting production facility of animal oil |
| CN206721163U (en) * | 2017-04-21 | 2017-12-08 | 南通海珥玛科技股份有限公司 | A kind of vapor dehydration column for grease post processing |
| CN108018115A (en) * | 2017-12-07 | 2018-05-11 | 莱阳易农农牧设备有限公司 | Animal fat refining process |
| CN207567192U (en) * | 2017-12-07 | 2018-07-03 | 莱阳易农农牧设备有限公司 | Animal fat refining equipment |
| CN108499509A (en) * | 2018-06-12 | 2018-09-07 | 深圳市朗坤环境集团股份有限公司 | The dry method system of raising prepares the devices and methods therefor of meat meal tankage and oil quality |
| CN108559621A (en) * | 2018-06-26 | 2018-09-21 | 新乡市红阳油脂工程技术有限公司 | A kind of animal fat Environment-friendlyextraction extraction method |
| CN208632480U (en) * | 2018-07-10 | 2019-03-22 | 郑州宏旺机械设备有限公司 | Animal oil extraction system with environment-friendly function |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190719 |
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| RJ01 | Rejection of invention patent application after publication |