CN205731255U - A kind of Maillard reaction still - Google Patents
A kind of Maillard reaction still Download PDFInfo
- Publication number
- CN205731255U CN205731255U CN201620668422.0U CN201620668422U CN205731255U CN 205731255 U CN205731255 U CN 205731255U CN 201620668422 U CN201620668422 U CN 201620668422U CN 205731255 U CN205731255 U CN 205731255U
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- China
- Prior art keywords
- kettle
- steam
- maillard reaction
- reaction still
- heat pipe
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Abstract
The utility model discloses a kind of Maillard reaction still, its drip irrigation device is to include kettle, kettle top is provided with charging aperture, it is provided with heater on the inwall of kettle, kettle be internally provided with agitator, the driver driving agitator to rotate it is connected with outside kettle, heater include at least two in bolt shape arrange add heat pipe, adding heat pipe one end is steam inlet, the other end is steam (vapor) outlet, add heat pipe to arrange along short transverse and steam inlet and steam (vapor) outlet are in staggered distribution up and down, wherein a steam inlet adding heat pipe is positioned at homonymy with an adjacent steam (vapor) outlet adding heat pipe, reach to ensure that material is heated more uniformly purpose.
Description
Technical field
This utility model relates to a kind of reactor, particularly to a kind of Maillard reaction still.
Background technology
Maillard reaction is between carbonyl compound (reducing sugar) and amino-compound (amino acid and protein)
Reaction.Maillard reaction can produce substantial amounts of to fragrant composition, have been widely used for preparing various meat and essence spice for cigarette,
Fumet.
And existing Maillard reaction still refers to the Chinese patent of Application No. 201320569408.1, it includes still
Body, material is contained in kettle, and the outside of kettle is provided with chuck, and jackets outer wall is provided with steam inlet, steam (vapor) outlet；In kettle
Portion is provided with agitator, Multifunction Sensor, and described agitator is connected with motor.Heated by steam, then by stirring
Mix device to stir.
Mode more than and makes steam be full of chuck simply by the diffusion of steam so that the temperature of regional has one
Fixed difference so that heat the most uneven.Agitator simply left and right stirring simultaneously, stirring is more uneven all so that material holds
Easily it is heated inequality.
Utility model content
The purpose of this utility model is to provide one and ensures that material is heated more uniform Maillard reaction still.
Above-mentioned technical purpose of the present utility model has the technical scheme that a kind of Maillard reaction
Still, including kettle, kettle top is provided with charging aperture, and the inwall of kettle is provided with heater, kettle be internally provided with stirring
Device, be connected with outside kettle drive agitator rotate driver, heater include at least two in bolt shape arrange add heat pipe,
Adding heat pipe one end is steam inlet, and the other end is steam (vapor) outlet, adds heat pipe and arranges along short transverse and steam inlet and steam go out
Mouth is in staggered distribution up and down, and wherein a steam inlet adding heat pipe is positioned at homonymy with an adjacent steam (vapor) outlet adding heat pipe.
By using technique scheme, steam passes in and out from steam inlet and steam (vapor) outlet respectively, has a fixing stream
Road, has fully ensured that the circulation of steam, and steam adds heat pipe from one and moves under upper simultaneously, transports from the bottom to top from another
Dynamic to heat the most uniform, it is to avoid when after entrance, steam flows to steam outlet, temperature decreases, and fully ensures that kettle
Upper and lower temperature contrast is little, thus ensure that material homogeneous heating.
It is also preferred that the left be connected with heating muff in kettle, heating muff connects with heater.
By using technique scheme, heating muff plays the effect of auxiliary heating, can enter material in the middle part of kettle
Row heating, it is ensured that homogeneous heating；Heated by the steam in heater simultaneously, more convenient.
It is also preferred that the left agitator stretches in heating muff, heating muff immerses in material, and agitator includes being connected with driver
Rotating shaft and rotating shaft on the affixed blade driving materials downward.
By using technique scheme, promote the materials downward in heating muff, be then subjected to extruding, material to
Move between heating muff and inner wall of kettle, return to heating muff from the top of heating muff afterwards, form circulation, it is ensured that
Heating more uniform.
It is also preferred that the left the distance between heating muff and kettle diapire is between 5cm to 10cm.
By using technique scheme, the flow that material enters in the case of distance is the least can be smaller, it is not easy to
Being circulated, the material of the relatively big then autoclave body bottom of distance is less likely to occur to follow bad；And distance is the setting between 5cm to 10cm
Can the most sufficiently ensure the circulation of material.
It is also preferred that the left be provided with mouth spray in kettle, mouth spray connects with heater, is provided with shower valve at mouth spray.
By using technique scheme, opening shower valve, steam also can humidify in being entered kettle by mouth spray.
Adopt material mouth it is also preferred that the left be communicated with on the sidewall of kettle, adopt material mouth and tilt to be connected with kettle.
By using technique scheme, the product produced can be carried out the amount of taking out inspection, after the assay was approved by adopting material mouth
Unification is discharged by discharging opening again, it is ensured that product quality.
It is also preferred that the left be connected with insulation jacket outside kettle.
By using technique scheme, kettle is played certain heat insulation effect, it is ensured that the temperature in kettle.
It is also preferred that the left the top of kettle is communicated with condenser.
By using technique scheme, after volatile component is condensed in material, return to reactor by condenser from newly
In.
It is also preferred that the left be connected with observation window on the sidewall of kettle.
By using technique scheme, the convenient material observed in kettle, it is ensured that the high-quality of material.
In sum, this utility model has the advantages that circulation is more abundant, heats the most uniform, it is ensured that
The quality of product.
Accompanying drawing explanation
Fig. 1 is the structural representation of Maillard reaction still in embodiment 1；
Fig. 2 is the structural representation of Maillard reaction still in embodiment 2；
Fig. 3 is the structural representation of agitator in embodiment 2.
In figure, 1, kettle；11, charging aperture；12, observation window；13, insulation jacket；2, agitator；21, motor；22, rotating shaft；
23, blade；3, detector；31, display；4, condenser；5, mouth spray；6, heater；61, first adds heat pipe；62, second
Root adds heat pipe；63, steam (vapor) outlet；64, steam inlet；7, discharging opening；8, heating muff；9, material mouth is adopted.
Detailed description of the invention
Below in conjunction with accompanying drawing, this utility model is described in further detail.The most identical parts are with identical accompanying drawing
Labelling represents.It should be noted that the word "front", "rear" used in describing below, "left", "right", "up" and "down" refer to
Being the direction in accompanying drawing, word " bottom surface " and " end face ", " interior " and " outward " refer respectively to towards or away from particular elements geometry
The direction at center.
Embodiment 1: as it is shown in figure 1, a kind of Maillard reaction still, including kettle 1, the top of kettle 1 is provided with charging aperture
11.The top of kettle 1 is also communicated with condenser 4 simultaneously, is connected with observation window 12 on the sidewall of kettle 1, and the bottom of kettle 1 sets
It is equipped with discharging opening 7.
Being connected with heater 6 on the inwall of kettle 1, heater 6 includes that at least two spiral add heat pipe, the most excellent
Elect even number root as.Every adds heat pipe and all has steam inlet 64 and steam (vapor) outlet 63, adds heat pipe and vertically arrange, adding
In the case of heat pipe is two, first adds the steam inlet 64 of heat pipe 61 up, then steam (vapor) outlet 63 is positioned at lower section, steam
From top to bottom；Second steam inlet 64 adding heat pipe 62 is positioned at lower section, and steam (vapor) outlet 63 is above, and steam is from bottom to top.
Can also connect on heater 6 and have mouth spray 5, mouth spray 5 to be positioned at kettle 1, mouth spray 5 is provided with spray
Valve.Can also arrange detector 3 in kettle 1, detector 3 connects display 31, thus reflects the situation of material, the most permissible
Related data is controlled.
Meanwhile, kettle 1 be internally provided with agitator 2, the top of kettle 1 is connected with motor 21, and motor 21 drives stirring
Device 2 rotates.
When producing, required material is poured in reactor by charging aperture 11, the acid number needed for regulation technique, reach to want
After asking, open steam inlet 64, steam (vapor) outlet 63 and condenser 4, by heater 6, material is heated to 90-120 DEG C, heating
Temperature can be controlled by detector 3, and in material, volatile component returns in reactor from newly after being condensed by condenser 4.
Embodiment 2: as in figure 2 it is shown, be connected with insulation jacket 13 outside kettle 1, be connected with heating muff 8 in kettle 1,
Having cavity in heating muff 8 and connect with heater 6, heating muff 8 can also play certain heats.
Heating muff 8 now immerses in material, and agitator 2 stretches in heating muff 8, rotates, stir in heating muff 8
Mix device 2 and include rotating shaft 22 and blade 23.Blade 23 is fixed in rotating shaft 22 and is inclined to set (referring to Fig. 3), motor 21
Drive shaft 22 rotates thus band moving vane 23 rotates, and the blade 23 of inclination pushes down on material so that materials downward.
Distance between heating muff 8 and kettle 1 diapire is between 5cm to 10cm.
Meanwhile, the sidewall of kettle 1 is communicated with and adopts material mouth 9, adopt material mouth 9 and may be located at the bottom of kettle 1, adopt material mouth 9 oblique
Set up.
When producing, required material is poured in reactor by charging aperture 11, the acid number needed for regulation technique, reach to want
After asking, open steam inlet 64, steam (vapor) outlet 63, condenser 4 and motor 21, by heater 6, material is heated to 90-120
DEG C, during blade 23 promote the materials downward in heating muff 8, be then subjected to extruding, material is to heating muff 8 and still
Move between body 1 inwall, the top from heating muff 8 returns to heating muff 8 afterwards, form circulation and (refer to the arrow in Fig. 2
Head direction).Heating-up temperature can be controlled by detector 3, returns from new after in material, volatile component is condensed by condenser 4
In reactor.
This specific embodiment is only that it is not to restriction of the present utility model, ability to explanation of the present utility model
The present embodiment can be made after reading this specification by field technique personnel as required does not has the amendment of creative contribution, but
As long as all being protected by Patent Law in right of the present utility model.
Claims (9)
1. a Maillard reaction still, including kettle (1), kettle (1) top is provided with charging aperture (11), on the inwall of kettle (1)
Be provided with heater (6), kettle (1) be internally provided with agitator (2), be connected with outside kettle (1) driving agitator (2) rotate
Driver, it is characterised in that: heater (6) include at least two in bolt shape arrange add heat pipe, add heat pipe one end for steam
Vapor inlet (64), the other end is steam (vapor) outlet (63), adds heat pipe and arranges and steam inlet (64) and steam (vapor) outlet along short transverse
(63) being in staggered distribution up and down, wherein one adds the steam inlet (64) of heat pipe and adds steam (vapor) outlet (63) position of heat pipe with adjacent one
In homonymy.
Maillard reaction still the most according to claim 1, it is characterised in that: it is connected with heating muff (8) in kettle (1),
Heating muff (8) connects with heater (6).
Maillard reaction still the most according to claim 2, it is characterised in that: agitator (2) stretches in heating muff (8),
Heating muff (8) immerses in material, and agitator (2) includes that the rotating shaft (22) being connected with driver and rotating shaft (22) are gone up the most affixed
Drive the blade (23) of materials downward.
Maillard reaction still the most according to claim 2, it is characterised in that: between heating muff (8) and kettle (1) diapire
Distance be between 5cm to 10cm.
Maillard reaction still the most according to claim 1, it is characterised in that: it is provided with mouth spray (5) in kettle (1), spray
Drenching mouth (5) to connect with heater (6), mouth spray (5) place is provided with shower valve.
Maillard reaction still the most according to claim 1, it is characterised in that: it is communicated with on the sidewall of kettle (1) and adopts material mouth
(9), adopt material mouth (9) to tilt to be connected with kettle (1).
Maillard reaction still the most according to claim 1, it is characterised in that: kettle (1) is outside is connected with insulation jacket
(13).
Maillard reaction still the most according to claim 1, it is characterised in that: the top of kettle (1) is communicated with condenser
(4).
Maillard reaction still the most according to claim 1, it is characterised in that: it is connected with observation window on the sidewall of kettle (1)
(12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620668422.0U CN205731255U (en) | 2016-06-28 | 2016-06-28 | A kind of Maillard reaction still |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620668422.0U CN205731255U (en) | 2016-06-28 | 2016-06-28 | A kind of Maillard reaction still |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205731255U true CN205731255U (en) | 2016-11-30 |
Family
ID=57382740
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620668422.0U Expired - Fee Related CN205731255U (en) | 2016-06-28 | 2016-06-28 | A kind of Maillard reaction still |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205731255U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107691640A (en) * | 2017-11-23 | 2018-02-16 | 湖北酷我乳业股份有限公司 | A kind of molten milk brown stain device |
| CN116268475A (en) * | 2023-03-07 | 2023-06-23 | 湖南省溢味佳生物科技有限公司 | Meat powder preparation device and method based on Maillard reaction |
-
2016
- 2016-06-28 CN CN201620668422.0U patent/CN205731255U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107691640A (en) * | 2017-11-23 | 2018-02-16 | 湖北酷我乳业股份有限公司 | A kind of molten milk brown stain device |
| CN116268475A (en) * | 2023-03-07 | 2023-06-23 | 湖南省溢味佳生物科技有限公司 | Meat powder preparation device and method based on Maillard reaction |
| CN116268475B (en) * | 2023-03-07 | 2024-01-23 | 湖南省溢味佳生物科技有限公司 | Meat powder preparation device and method based on Maillard reaction |
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Legal Events
| 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161130 Termination date: 20180628 |