CN112646658A - Beef tallow deslagging and drying system and production process - Google Patents
Beef tallow deslagging and drying system and production process Download PDFInfo
- Publication number
- CN112646658A CN112646658A CN202011535864.5A CN202011535864A CN112646658A CN 112646658 A CN112646658 A CN 112646658A CN 202011535864 A CN202011535864 A CN 202011535864A CN 112646658 A CN112646658 A CN 112646658A
- Authority
- CN
- China
- Prior art keywords
- beef tallow
- drying system
- pump
- butter
- cyclone
- 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
Links
- 235000015278 beef Nutrition 0.000 title claims abstract description 24
- 239000003760 tallow Substances 0.000 title claims abstract description 24
- 238000001035 drying Methods 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 241001503485 Mammuthus Species 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 238000004332 deodorization Methods 0.000 claims abstract description 11
- 238000001914 filtration Methods 0.000 claims abstract description 10
- 239000012535 impurity Substances 0.000 claims abstract description 7
- 230000001877 deodorizing effect Effects 0.000 claims abstract description 5
- 235000014121 butter Nutrition 0.000 claims description 14
- 239000000796 flavoring agent Substances 0.000 claims description 12
- 235000019634 flavors Nutrition 0.000 claims description 12
- 238000005086 pumping Methods 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 150000002978 peroxides Chemical class 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 12
- 239000003921 oil Substances 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 4
- 230000002411 adverse Effects 0.000 abstract description 2
- 239000006227 byproduct Substances 0.000 abstract description 2
- 239000004519 grease Substances 0.000 description 6
- 239000000194 fatty acid Substances 0.000 description 5
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- 235000021588 free fatty acids Nutrition 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 206010067484 Adverse reaction Diseases 0.000 description 1
- 235000019737 Animal fat Nutrition 0.000 description 1
- 230000006838 adverse reaction Effects 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 235000021281 monounsaturated fatty acids Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000001256 steam distillation Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Images
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
- C11B3/00—Refining fats or fatty oils
Landscapes
- 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)
- Meat, Egg Or Seafood Products (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
Abstract
The invention discloses a beef tallow residue-removing and drying system, which comprises a de-odorizing tank connected with vacuum equipment, wherein the de-odorizing tank is connected with subsequent fine filtering equipment, the vacuum equipment comprises a cyclone and a high water level jet pump, a steam inlet at the bottom of the de-odorizing tank is connected with a mammoth pump with an improved nozzle, the mammoth pump is connected with a guide pipe with an enlarged pipe diameter, and the top of the guide pipe is provided with a hair-scattering cap. The invention also provides a production process for removing the residue and drying the beef tallow. The method has the advantages that impurities and water are thoroughly removed, the yield per unit time is high, the deodorization time is only 30min, the efficiency is improved, and the energy is saved; the deodorizing, impurity removing and drying effects are good, the finished oil gas has pure taste and no peculiar smell, and the generation of adverse side products is prevented; the operation flow is simple and easy to understand, no special requirements are required for operators, the equipment runs stably, and the method is an important guarantee for obtaining high-quality deodorized finished beef tallow.
Description
Technical Field
The invention belongs to the technical field of animal fat food processing, and particularly relates to a beef tallow deslagging and drying system and a production process thereof.
Background
The principle of the butter fat deslagging and drying is a technological process of removing moisture, light components, free fatty acid, mutton smell and the like by means of a steam distillation principle under the condition of high temperature and high vacuum by utilizing the characteristic that the volatility of the components to be removed is greatly different from that of butter, and the technological process is an important part in a butter fat refining process. In the traditional equipment and process, because the utilization rate of steam introduction is not high, in order to reach the standard of removing free fatty acid, the high-temperature retention time of the oil is long, and adverse reactions such as oxidation of the oil and decomposition of some effective components are accompanied, for example, trans-fatty acid (TFA) is greatly increased, so that the quality of the oil is influenced. Meanwhile, besides basic raw materials, the consumption of water, electricity, steam and the like is also an important component for deslagging and drying, wherein the consumption proportion of water vapor is the largest, the workload of a system is large, so that the energy consumption is high, the influence factors of the whole production process are many, and the control is difficult. The system which is convenient to operate, stable to operate and reliable in quality becomes an important guarantee for obtaining high-quality finished beef tallow.
Disclosure of Invention
The invention mainly aims to design a butter deslagging and drying system aiming at the requirements on butter deslagging and drying equipment and process, and provides a butter deslagging and drying production process, which has the advantages of high equipment and process yield, good deodorization effect, pure taste and flavor of finished oil gas, no peculiar smell, high quality, simple and understandable operation flow and no special requirements on operators.
In order to achieve the purpose of the invention, the technical scheme adopted by the invention is as follows:
the utility model provides a butter takes off sediment drying system, includes the jar of taking off the flavor of being connected with vacuum apparatus, takes off the follow-up fine filtration equipment of flavor jar reconnection, vacuum apparatus is cyclone and high water level jet pump, and the cyclone is connected and is taken off flavor jar air outlet, and the cyclone export is connected to high water level jet pump, take off the steam inlet of flavor jar bottom and connect the mammoth pump, the honeycomb duct is connected to the mammoth pump, and the honeycomb duct top is provided with the shot-cap.
Preferably, the pumping amount of the high-level jet pump is 300L/min.
The deodorizing tank adopts a high-level water jet pump as a vacuum source, the pumping amount of the vacuum source is 300L/min, the stability is strong, the operation is simple, and the failure rate is low.
Preferably, the pipe diameter of the flow guide pipe of the deodorization tank is 375 mm.
The pipe diameter of the traditional flow guide pipe is about 220mm, generally 219 mm. After the diameter of the flow guide pipe is enlarged, the contact time of steam and the grease is increased and fully saturated, and the foreign flavor in the grease is extracted under the vacuum condition.
Preferably, the mammoth pump nozzle is a straight hole, and the nozzle opening is enlarged by 20-60 degrees.
Specifically, the mammoth pump nozzle is a 6mm straight hole, the nozzle opening is enlarged by 20-45 degrees, and the diameter of the nozzle opening is 11 mm.
By adopting the mammoth pump, more effective steam can be introduced into the oil in a shorter time, and the oil and the steam are vigorously mixed, so that the effects of effective contact and increase of the specific surface area of oil diffusion are achieved. The traditional mammoth pump nozzle is a 4mm straight hole, and steam jet is not enough to be dispersed. The improved counterbore alpha angle is 20-45 deg..
The design that honeycomb duct pipe diameter in the middle of having adopted the increase in the design of the jar of taking off the flavor improves and has made neotype mammoth's pump, makes the grease under the thrust of steam and vacuum condition, and the stirring of unit interval is more abundant with rolling, and the cap of loosing above the honeycomb duct is cooperated, lets moisture in the grease, light component, free fatty acid, mutton smell etc. give off fast, is taken away in the vacuum. Simple operation and strong stability.
A production process for removing residue and drying beef tallow comprises the following steps:
1) conveying the semi-finished beef tallow into a deodorization tank, starting steam, and simultaneously starting a cyclone and a high water level jet pump to form a high-vacuum high-temperature environment with the temperature of 120-;
2) high-temperature steam is sprayed into the flow guide pipe through a mammoth pump, impurities of the semi-finished beef tallow are quickly evaporated and pumped away under the thrust and vacuum conditions of the steam, and the deodorization tank continuously operates for 30 min;
3) conveying the deslagged and dried beef tallow into subsequent fine filtering equipment for filtering to finally obtain the finished beef tallow with the acid value less than or equal to 0.06(KOH) mg/g, the peroxide value less than or equal to 0.2g/100g and the water content less than or equal to 0.5g/100 g.
In the process of removing impurities, the retention time is too long, so that the Trans Fatty Acid (TFA) is greatly increased, wherein most of the trans fatty acid is generated by polyunsaturated fatty acid and part of the trans fatty acid is generated by monounsaturated fatty acid, and the generation amount of the trans fatty acid has an exponential relation with the temperature and has a linear relation with the time.
Compared with the prior art, the invention has the beneficial effects that:
the butter deslagging and drying equipment and the process provided by the invention have the following advantages:
according to the device, the improvement of the mammoth pump enables the injected steam to be more uniform and sufficient, the contact time of the steam and the grease is increased and fully saturated after the diameter of the flow guide pipe is enlarged, and the foreign flavor in the grease is extracted under the vacuum condition; impurities and water are thoroughly removed, the yield per unit time is high, the deodorization time is only 30min, the efficiency is improved, and the energy is saved; the deodorizing effect is good, the taste of the finished oil gas is pure, no peculiar smell exists, and the generation of adverse side products is prevented; the operation flow is simple and easy to understand, no special requirements are required for operators, the equipment runs stably, and the method is an important guarantee for obtaining high-quality deodorized finished beef tallow.
Drawings
FIG. 1 is a schematic diagram of a butter deslag drying system of the invention.
Fig. 2 is a schematic view of a nozzle structure of a conventional mammoth pump.
Fig. 3 is a schematic structural diagram of the nozzle of the mammoth pump of the present invention.
Wherein, 1, a deodorizing tank; 2. a cyclone; 3. a high water level jet pump; 4. a hair-dispersing cap; 5. a flow guide pipe; 6. a mammoth pump.
Detailed Description
The foregoing summary of the invention is described in further detail below with reference to specific embodiments.
It should not be understood that the scope of the above-described subject matter of the present invention is limited to the following examples. Various substitutions and alterations can be made without departing from the technical idea of the invention as described above, according to the common technical knowledge and conventional means in the field, and the scope of the invention is covered.
Example 1
As shown in figure 1, a beef tallow dregs-removing and drying system comprises a smell-removing tank 1 connected with a vacuum device, wherein the smell-removing tank 1 is connected with a subsequent fine filtering device, the vacuum device comprises a cyclone 2 and a high water level jet pump 3, the cyclone 2 is connected with an air outlet of the smell-removing tank 1, the high water level jet pump 3 is connected with an outlet of the cyclone 2, and a draft tube 5 of the smell-removing tank 1 is provided with a dispersing cap 4.
The pumping amount of the high water level jet pump 3 is 300L/min.
The pipe diameter of the flow guide pipe 5 of the deodorization tank 1 is 375 mm.
As shown in figure 2, the nozzle of the mammoth pump 6 is a 6mm straight hole, the nozzle opening is enlarged by 20-45 degrees, and the diameter of the nozzle opening is 11 mm.
Example 2
1) Conveying the semi-finished beef tallow into a deodorization tank 1, starting steam, and simultaneously starting a cyclone 2 and a high water level injection pump 3 to form a high-vacuum high-temperature environment with the temperature of 120-;
2) high-temperature steam is sprayed into the flow guide pipe 5 through the mammoth pump 6, impurities of the semi-finished beef tallow are quickly evaporated and pumped away under the thrust and vacuum conditions of the steam, and the deodorization tank 1 continuously operates for 30 min;
3) conveying the deslagged and dried beef tallow into subsequent fine filtering equipment for filtering to finally obtain the finished beef tallow with the acid value less than or equal to 0.06(KOH) mg/g, the peroxide value less than or equal to 0.2g/100g and the water content less than or equal to 0.5g/100 g.
In conclusion, the invention provides the beef tallow residue-removing drying system and the production process, which have the advantages of high yield, good smell-removing effect, pure taste of finished oil gas, no peculiar smell, high quality, simple and understandable operation process and no special requirements on operators.
Claims (6)
1. The utility model provides a butter deslag drying system, includes the jar of taking off flavor (1) of being connected with vacuum apparatus, takes off flavor jar (1) and reconnects follow-up smart filtration equipment, its characterized in that: vacuum apparatus is cyclone (2) and high water level jet pump (3), and cyclone (2) are connected and are taken off flavor jar (1) air outlet, and cyclone (2) export is connected in high water level jet pump (3), take off the steam inlet of flavor jar (1) bottom and connect mammoth pump (6), and mammoth pump (6) are connected honeycomb duct (5), and honeycomb duct (5) top is provided with sporadic cap (4).
2. The butter deslag drying system of claim 1, wherein: the pumping amount of the high water level jet pump (3) is 300L/min.
3. The butter deslag drying system of claim 1, wherein: the pipe diameter of the flow guide pipe (5) of the deodorization tank (1) is 375 mm.
4. The butter deslag drying system of claim 1, wherein: the nozzle of the mammoth pump (6) is a straight hole, and the nozzle opening is enlarged by 20-60 degrees.
5. The butter deslag drying system of claim 4, wherein: the nozzle of the mammoth pump (6) is a 6mm straight hole, the nozzle opening is enlarged by 20-45 degrees, and the diameter of the nozzle opening is 11 mm.
6. The production process for removing residue and drying beef tallow is characterized by comprising the following steps:
1) conveying the semi-finished beef tallow into a deodorization tank (1), starting steam, and simultaneously starting a cyclone (2) and a high water level jet pump (3) to form a high-vacuum high-temperature environment with the temperature of 120-;
2) high-temperature steam is sprayed into the guide pipe (5) through the mammoth pump (6), impurities of the semi-finished beef tallow are quickly evaporated and pumped away under the thrust of the steam and the vacuum condition, and the deodorizing tank (1) continuously operates for 30 min;
3) conveying the deslagged and dried beef tallow into subsequent fine filtering equipment for filtering to finally obtain the finished beef tallow with the acid value less than or equal to 0.06(KOH) mg/g, the peroxide value less than or equal to 0.2g/100g and the water content less than or equal to 0.5g/100 g.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011535864.5A CN112646658A (en) | 2020-12-23 | 2020-12-23 | Beef tallow deslagging and drying system and production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011535864.5A CN112646658A (en) | 2020-12-23 | 2020-12-23 | Beef tallow deslagging and drying system and production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112646658A true CN112646658A (en) | 2021-04-13 |
Family
ID=75359343
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011535864.5A Pending CN112646658A (en) | 2020-12-23 | 2020-12-23 | Beef tallow deslagging and drying system and production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112646658A (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101195788A (en) * | 2007-12-31 | 2008-06-11 | 李家福 | Flavour removing technique and device for vegetable oil without moisture removed |
| CN101659902A (en) * | 2009-08-19 | 2010-03-03 | 嘉吉烯王生物工程(湖北)有限公司 | Oil deodorization method and equipment |
| CN102311872A (en) * | 2011-08-16 | 2012-01-11 | 山东渤海实业股份有限公司 | Method and equipment for low-temperature short-time deodorization of plant oil |
| CN103060087A (en) * | 2013-01-23 | 2013-04-24 | 上海焦尔工程技术有限公司 | Oil deodorization device, deodorization method thereof and packing stripping pump mechanism |
| CN103409236A (en) * | 2013-09-03 | 2013-11-27 | 河南粮工科技有限公司 | Combined type deacidification and deodorization tower suitable for deodorizing edible oil in oil industry |
| CN205603553U (en) * | 2016-05-09 | 2016-09-28 | 江西恩泉油脂有限公司 | Crude oil deodorization device |
| CN106281642A (en) * | 2016-08-31 | 2017-01-04 | 广汉市航佳食品有限公司 | A kind of production technology of animal oil |
| CN111676095A (en) * | 2020-06-24 | 2020-09-18 | 广汉市迈德乐食品有限公司 | Fully-automatic integrated production line for beef tallow |
| CN112755550A (en) * | 2020-12-23 | 2021-05-07 | 四川航佳生物科技有限公司 | Strong-flavor beef tallow rapid drying system and production process |
-
2020
- 2020-12-23 CN CN202011535864.5A patent/CN112646658A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101195788A (en) * | 2007-12-31 | 2008-06-11 | 李家福 | Flavour removing technique and device for vegetable oil without moisture removed |
| CN101659902A (en) * | 2009-08-19 | 2010-03-03 | 嘉吉烯王生物工程(湖北)有限公司 | Oil deodorization method and equipment |
| CN102311872A (en) * | 2011-08-16 | 2012-01-11 | 山东渤海实业股份有限公司 | Method and equipment for low-temperature short-time deodorization of plant oil |
| CN103060087A (en) * | 2013-01-23 | 2013-04-24 | 上海焦尔工程技术有限公司 | Oil deodorization device, deodorization method thereof and packing stripping pump mechanism |
| CN103409236A (en) * | 2013-09-03 | 2013-11-27 | 河南粮工科技有限公司 | Combined type deacidification and deodorization tower suitable for deodorizing edible oil in oil industry |
| CN205603553U (en) * | 2016-05-09 | 2016-09-28 | 江西恩泉油脂有限公司 | Crude oil deodorization device |
| CN106281642A (en) * | 2016-08-31 | 2017-01-04 | 广汉市航佳食品有限公司 | A kind of production technology of animal oil |
| CN111676095A (en) * | 2020-06-24 | 2020-09-18 | 广汉市迈德乐食品有限公司 | Fully-automatic integrated production line for beef tallow |
| CN112755550A (en) * | 2020-12-23 | 2021-05-07 | 四川航佳生物科技有限公司 | Strong-flavor beef tallow rapid drying system and production process |
Non-Patent Citations (1)
| Title |
|---|
| 殷永玲等: "炼制条件对牛油中塑化剂及风味物质的影响研究", 《中国油脂》 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101659902B (en) | Method and equipment for grease deodorization | |
| CN101649250A (en) | Technology for deodorizing vegetable oil with high content of unsaturated acid | |
| JP2005350632A (en) | Method for producing biodiesel fuel | |
| CN112646658A (en) | Beef tallow deslagging and drying system and production process | |
| CN113755240A (en) | Method for removing trichloropropanol ester and glycidyl ester in palm oil | |
| CN107216253A (en) | A kind of utilization enzyme-chemically United Technologies extract the production method of VE, sterol from soybean oil deodorizer distillate | |
| CN112755550A (en) | Strong-flavor beef tallow rapid drying system and production process | |
| CN218710256U (en) | Device for preparing fatty acid from waste oil | |
| CN102796620B (en) | Fixed bed-based continuous catalytic esterification production method | |
| CN201459093U (en) | Oil deodorization device | |
| CN212610501U (en) | Rapid deacidification and low-sulfur high-yield production system for producing fuel oil by using waste animal and vegetable oil | |
| CN104263509A (en) | DHA micro-algal oil degumming method | |
| JP2011068738A (en) | Method for extracting oil-and-fat from scenedesmus, and application of oil-and-fat and degreased residue | |
| CN111876264A (en) | Rapid deacidification and low-sulfur high-yield production system for producing fuel oil by using waste animal and vegetable oil | |
| CN201567322U (en) | Vegetable oil and fat desolventizing tower | |
| CN211339420U (en) | Deodorizing device for wheat germ oil | |
| CN217921978U (en) | Filtering equipment for low-temperature deodorization of corn oil | |
| CN201883085U (en) | Oil deodorizing tower with controllable temperature | |
| CN217459358U (en) | High-purity fatty acid preparation facilities | |
| CN214571779U (en) | Vegetable oil refining vacuum deodorization system | |
| CN221971523U (en) | Desolventizing device for rice bran wax refining | |
| CN115650943B (en) | Method for enriching polyunsaturated fatty acid ester, squalene, natural vitamin E and phytosterol from plant deodorization distillate | |
| CN210583734U (en) | Environment-friendly energy-saving tail gas treatment device for crude fat oil refining processing | |
| CN109169969B (en) | Preparation method of high-smoke-point mixed edible oil containing polyunsaturated fatty acid | |
| CN219342093U (en) | Edible oil stripping deacidification device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20210413 |
|
| RJ01 | Rejection of invention patent application after publication |