CN207958290U - Chafing dish butter system for decocting - Google Patents
Chafing dish butter system for decocting Download PDFInfo
- Publication number
- CN207958290U CN207958290U CN201820228273.5U CN201820228273U CN207958290U CN 207958290 U CN207958290 U CN 207958290U CN 201820228273 U CN201820228273 U CN 201820228273U CN 207958290 U CN207958290 U CN 207958290U
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- CN
- China
- Prior art keywords
- conveyance conduit
- butter
- chafing dish
- dregs
- condenser
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- 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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- Edible Oils And Fats (AREA)
Abstract
The utility model discloses a kind of chafing dish butter system for decocting, pre-processing assembly includes sequentially connected conveyer, jelly block crusher and preheating can, and the preheating can is connected to by the first conveyance conduit with oleo kettle, and is configured with material-handling pump.Dregs of fat separation assembly includes sequentially connected outfeed belt conveyor, oil-residue separator and butter storage bin, and the outfeed belt conveyor is connected to by the second conveyance conduit with oleo kettle, and second conveyance conduit is equipped with discharge valve.Smell processing component includes the condenser being sequentially communicated, vacuum water tank and deodorization trap, and the condenser is connected to by third conveyance conduit with the oleo kettle.The utility model has the advantages that:It is compact-sized, oil can not only be detached with the dregs of fat, additionally it is possible to timely remove butter and boil the gas with foreign flavor generated in the process, be conducive to environmental protection.
Description
Technical field
The utility model is related to a kind of edible fat production lines, and in particular to a kind of chafing dish butter system for decocting.
Background technology
For chafing dish as one of most unique cuisines in Chongqing, production technology is very exquisite, present chafing dish shop Major Epidemic
Edible vegetable oil chafing dish and beef tallow hot pot, edible vegetable oil chafing dish are mainly made of rapeseed oil, and beef tallow hot pot is utilized made of butter, dish
Seed oil is typically that rapeseed is squeezed and can be obtained by oil press, squeezing process comparative maturity.Butter are then from ox
It boils to obtain through low-temperature negative-pressure in sebum.In food processing technology very advanced today, existing butter tanning production line still has
Some shortcomings, for example many peculiar smell are will produce during boiling butter, it can not remove in time, affect air quality, and
And the oil and the dregs of fat generated by tanning butter cannot detach well, cause the dregs of fat that cannot preferably utilize, waste of resource.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of chafing dish butter system for decocting, compact-sized, can not only
It is enough to detach oil with the dregs of fat, additionally it is possible to timely to remove butter and boil the gas with foreign flavor generated in the process, be conducive to environmental protection.
To achieve the above object, technical solutions of the utility model are as follows:
A kind of chafing dish butter system for decocting, including oleo kettle, are characterized by, further include:
Pre-processing assembly comprising sequentially connected conveyer, jelly block crusher and preheating can, the preheating can pass through
One conveyance conduit is connected to the oleo kettle, and is configured with material-handling pump;
Dregs of fat separation assembly comprising sequentially connected outfeed belt conveyor, oil-residue separator and butter storage bin, it is described go out
Material conveyer is connected to by the second conveyance conduit with the oleo kettle, and second conveyance conduit is equipped with discharge valve;
Smell processing component comprising condenser, vacuum water tank and the deodorization trap being sequentially communicated, the condenser are logical
Third conveyance conduit is crossed to be connected to the oleo kettle.
Using the above structure, pre-processing assembly will crush place in the butter feedstock transportation of frost to jelly block crusher
Reason, then preheat and melt in preheating can, then be transported in oleo kettle by the first conveyance conduit under the driving of material-handling pump
Tanning, discharge valve when tanning on the second conveyance conduit are closed, again by the slurry of tanning by going out after tanning is good
Material conveyer is delivered in oil-residue separator, and oil-residue separator detaches oil with the dregs of fat, and the butter separated are stored in butter
In storage bin, due to containing a large amount of albumen and fat in the dregs of fat, the dregs of fat can make the feed of other animals, to make raw material obtain
It is utilized to sufficient.The gas with foreign flavor generated in tanning is vapor, and vapor first passes through condenser by most of vapor
It carries out level-one and cools down taste removal, then adsorbed by vacuum water tank and carry out two level taste removal, three-level is finally being carried out by deodorization trap
Taste removal.
As preferred:The oil-residue separator is also associated with dregs of fat transfer tank, which is connected with three side by side
The lard press of setting, the lard press are connected to by the 4th conveyance conduit with the butter storage bin.Using above-mentioned
Structure, lard press can carry out the dregs of fat squeezing again, squeeze out the butter come and be back to ox through the 4th conveyance conduit
Oily storage bin, makes raw material be fully utilized, cost-effective.
As preferred:The allocation ratio of the oleo kettle and condenser is 2:1.Using the above structure, can to meet gas cold
But needs.
As preferred:The quantity of the oleo kettle is 6, and the quantity of condenser is 3.Using the above structure, it is ensured that
Mass production.
As preferred:The quantity of the vacuum water tank is two, and is sequentially connected in series.Using the above structure, peculiar smell can be made to fill
Divide removal.
As preferred:The quantity of the deodorization trap is two, and is sequentially connected in series.Using the above structure, peculiar smell can be made
Fully removal.
As preferred:First conveyance conduit is equipped with Material control valve.Using the above structure, it is convenient for control raw material
The amount of being put into.
Compared with prior art, the utility model has the beneficial effects that:
Using chafing dish butter system for decocting provided by the utility model, pre-processing assembly by the butter feedstock transportation of frost extremely
Freeze in block crusher and crush processing, then preheat and melt in preheating can, then passes through first under the driving of material-handling pump
Conveyance conduit is transported to tanning in oleo kettle, and discharge valve when tanning on the second conveyance conduit is closed, and is boiled
The slurry of tanning is delivered to by outfeed belt conveyor in oil-residue separator again afterwards, oil-residue separator detaches oil with the dregs of fat, point
It separates out the butter come to be stored in butter storage bin, due to containing a large amount of albumen and fat in the dregs of fat, the dregs of fat can be made other
The feed of animal, to make raw material be fully utilized.The gas with foreign flavor generated in tanning is vapor, and vapor first leads to
It crosses condenser and most of vapor is subjected to level-one cooling taste removal, then adsorbed by vacuum water tank and carry out two level taste removal, finally exist
Three-level taste removal is carried out by deodorization trap.
Description of the drawings
Fig. 1 is the floor map of the utility model.
Specific implementation mode
The utility model is described in further detail with attached drawing with reference to embodiments.
As shown in Figure 1, a kind of chafing dish butter system for decocting, compact-sized, oil can not only be detached with the dregs of fat, additionally it is possible to
Timely removal butter boil the gas with foreign flavor generated in the process, are conducive to environmental protection.Its structure includes:Oleo kettle 4, pre-processing assembly
A, dregs of fat separation assembly B and smell processing component C, wherein pre-processing assembly A include sequentially connected conveyer 1, it is broken to freeze block
Broken machine 2 and preheating can 3, preheating can 3 are connected to by the first conveyance conduit 5 with the oleo kettle 4, and are configured with material-handling pump 6,
The material-handling pump 6 is used to pump the raw material in preheating can 3 is defeated to oleo kettle 4.Being put into for convenience of control raw material simultaneously
Amount, the first conveyance conduit 5 are equipped with Material control valve 19.
Dregs of fat separation assembly B includes sequentially connected outfeed belt conveyor 7, oil-residue separator 8 and butter storage bin 9, wherein
Outfeed belt conveyor 7 is connected to by the second conveyance conduit 10 with the oleo kettle 4, and second conveyance conduit 10 is equipped with outlet valve
Door 11, when tanning, above-mentioned discharge valve 11 was closed, and was opened again after tanning is good, the slurry of tanning passes through outfeed belt conveyor
7 are delivered in oil-residue separator 8, and the butter separated are stored in butter storage bin 9, due to containing a large amount of egg in the dregs of fat
White and fat, the dregs of fat can make the feed of other animals, to make raw material be fully utilized.
Smell processing component C includes the condenser 12, vacuum water tank 13 and deodorization trap 14 being sequentially communicated, the condensation
Device 12 is connected to by third conveyance conduit 15 with the oleo kettle 4.The gas with foreign flavor generated in tanning is vapor, vapor
It first passes through condenser 12 and most of vapor is subjected to level-one cooling taste removal, then progress two level is adsorbed by vacuum water tank 13 and is removed
Taste is finally carrying out three-level taste removal by deodorization trap 14.
To make raw material be fully utilized, more butter are extracted, the oil-residue separator 8 is also associated in the dregs of fat
Turn tank 16, which is connected with three lard press 17 arranged side by side, which passes through the 4th
Conveyance conduit 18 is connected to the butter storage bin 9, and lard press 17 can carry out the dregs of fat squeezing again, squeeze out and
Butter be back to butter storage bin 9 through the 4th conveyance conduit 18.
To ensure the needs of gas taste removal, the allocation ratio for stating oleo kettle 4 and condenser 12 is 2:1, in the present embodiment
The quantity of oleo kettle 4 is 6, and the quantity of condenser 12 is 3.Certainly, according to different throughput requirements oleo kettles 4 and condenser
12 quantity can do other arrangements.The quantity of vacuum water tank 13 and deodorization trap 14 is two simultaneously, and is sequentially connected in series.
The technological process of the utility model is:
Raw material → conveyer 1 → freezing block 2 → preheating can of crusher 3 → material-handling pump 6 and the first conveyance conduit 5 → is wasted lamp oil by not sleeping at night
4 → the second conveyance conduit 10 → outfeed belt conveyor, 7 → oil-residue separator, 8 → butter storage bins 9 of pot.
The dregs of fat that oil-residue separator 8 generates carry out twice pressing extraction residue through 16 → lard press of dregs of fat transfer tank 17
Butter, and collected in butter storage bin 9 by the 4th conveyance conduit 18.
The peculiar smell vapor generated in oleo kettle 4 first passes through condenser 12 and carries out level-one cooling taste removal, then passes through vacuum water
The absorption of case 13 carries out two level taste removal, finally carries out three-level taste removal by deodorization trap 14 again.
Finally, it should be noted that foregoing description is only the preferred embodiment of the utility model, the common skill of this field
Art personnel are under the enlightenment of the utility model, under the premise of without prejudice to the utility model aims and claim, can make
Expression, such transformation are each fallen within the scope of protection of the utility model as multiple types.
Claims (7)
1. a kind of chafing dish butter system for decocting, including oleo kettle (4), which is characterized in that further include:
Pre-processing assembly (A) comprising sequentially connected conveyer (1) freezes block crusher (2) and preheating can (3), the preheating
Tank (3) is connected to by the first conveyance conduit (5) with the oleo kettle (4), and is configured with material-handling pump (6);
Dregs of fat separation assembly (B) comprising sequentially connected outfeed belt conveyor (7), oil-residue separator (8) and butter storage bin
(9), the outfeed belt conveyor (7) is connected to by the second conveyance conduit (10) with the oleo kettle (4), and second conveyance conduit
(10) it is equipped with discharge valve (11);
Smell processing component (C) comprising condenser (12), vacuum water tank (13) and the deodorization trap (14) being sequentially communicated,
The condenser (12) is connected to by third conveyance conduit (15) with the oleo kettle (4).
2. chafing dish butter system for decocting according to claim 1, it is characterised in that:The oil-residue separator (8) is also connected with
There is dregs of fat transfer tank (16), which is connected with three lard press (17) arranged side by side, the dregs of fat
Squeezer (17) is connected to by the 4th conveyance conduit (18) with the butter storage bin (9).
3. chafing dish butter system for decocting according to claim 1 or 2, it is characterised in that:The oleo kettle (4) and condenser
(12) allocation ratio is 2:1.
4. chafing dish butter system for decocting according to claim 3, it is characterised in that:The quantity of the oleo kettle (4) is 6
A, the quantity of condenser (12) is 3.
5. chafing dish butter system for decocting according to claim 4, it is characterised in that:The quantity of the vacuum water tank (13) is
Two, and be sequentially connected in series.
6. chafing dish butter system for decocting according to claim 5, it is characterised in that:The quantity of the deodorization trap (14)
It is two, and is sequentially connected in series.
7. chafing dish butter system for decocting according to claim 1, it is characterised in that:It is set on first conveyance conduit (5)
There is Material control valve (19).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820228273.5U CN207958290U (en) | 2018-02-08 | 2018-02-08 | Chafing dish butter system for decocting |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820228273.5U CN207958290U (en) | 2018-02-08 | 2018-02-08 | Chafing dish butter system for decocting |
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CN207958290U true CN207958290U (en) | 2018-10-12 |
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ID=63738416
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CN201820228273.5U Expired - Fee Related CN207958290U (en) | 2018-02-08 | 2018-02-08 | Chafing dish butter system for decocting |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110250551A (en) * | 2019-06-18 | 2019-09-20 | 重庆周君记火锅食品有限公司 | It is capable of the flavor pack production line and food seasoning packet of accurate Proportioning Oil and sauce ratio |
CN112277360A (en) * | 2020-10-13 | 2021-01-29 | 百珍堂生物科技(浙江)有限公司 | Column cap recovery and squeezing system |
CN112500924A (en) * | 2020-12-16 | 2021-03-16 | 河南领帆机械设备有限公司 | Surrounding type animal oil cooking equipment |
CN112931634A (en) * | 2019-12-11 | 2021-06-11 | 重庆市帅克食品有限公司 | Efficient beef tallow refining method |
CN113698982A (en) * | 2021-07-23 | 2021-11-26 | 四川航佳生物科技有限公司 | Hot pot butter processingequipment |
CN113980737A (en) * | 2021-11-25 | 2022-01-28 | 王勇 | Continuous production process of animal fat |
-
2018
- 2018-02-08 CN CN201820228273.5U patent/CN207958290U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110250551A (en) * | 2019-06-18 | 2019-09-20 | 重庆周君记火锅食品有限公司 | It is capable of the flavor pack production line and food seasoning packet of accurate Proportioning Oil and sauce ratio |
CN112931634A (en) * | 2019-12-11 | 2021-06-11 | 重庆市帅克食品有限公司 | Efficient beef tallow refining method |
CN112277360A (en) * | 2020-10-13 | 2021-01-29 | 百珍堂生物科技(浙江)有限公司 | Column cap recovery and squeezing system |
CN112500924A (en) * | 2020-12-16 | 2021-03-16 | 河南领帆机械设备有限公司 | Surrounding type animal oil cooking equipment |
CN113698982A (en) * | 2021-07-23 | 2021-11-26 | 四川航佳生物科技有限公司 | Hot pot butter processingequipment |
CN113980737A (en) * | 2021-11-25 | 2022-01-28 | 王勇 | Continuous production process of animal fat |
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GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181012 Termination date: 20210208 |