CN106635426A - Maillard reaction device suitable for tobacco concentrate and use method - Google Patents
Maillard reaction device suitable for tobacco concentrate and use method Download PDFInfo
- Publication number
- CN106635426A CN106635426A CN201710103989.2A CN201710103989A CN106635426A CN 106635426 A CN106635426 A CN 106635426A CN 201710103989 A CN201710103989 A CN 201710103989A CN 106635426 A CN106635426 A CN 106635426A
- Authority
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- China
- Prior art keywords
- tank body
- reacting tank
- heat exchanger
- tobacco concentrate
- steam
- 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
- 241000208125 Nicotiana Species 0.000 title claims abstract description 76
- 235000002637 Nicotiana tabacum Nutrition 0.000 title claims abstract description 76
- 239000012141 concentrate Substances 0.000 title claims abstract description 68
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 40
- 239000000463 material Substances 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 238000001704 evaporation Methods 0.000 claims abstract description 11
- 239000003507 refrigerant Substances 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims abstract 4
- 238000009833 condensation Methods 0.000 claims description 10
- 230000005494 condensation Effects 0.000 claims description 10
- 238000013461 design Methods 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 10
- 230000008020 evaporation Effects 0.000 claims description 10
- 230000008569 process Effects 0.000 claims description 9
- 238000009413 insulation Methods 0.000 claims description 4
- 238000001514 detection method Methods 0.000 claims description 2
- 238000001727 in vivo Methods 0.000 claims description 2
- 239000003205 fragrance Substances 0.000 abstract description 2
- 239000000796 flavoring agent Substances 0.000 description 5
- 235000019634 flavors Nutrition 0.000 description 5
- 235000019504 cigarettes Nutrition 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000002262 irrigation Effects 0.000 description 2
- 238000003973 irrigation Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 235000013599 spices Nutrition 0.000 description 2
- 241000287828 Gallus gallus Species 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000006757 chemical reactions by type Methods 0.000 description 1
- 235000019506 cigar Nutrition 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/022—Refining
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B3/00—Preparing tobacco in the factory
- A24B3/12—Steaming, curing, or flavouring tobacco
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/008—Feed or outlet control devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
- B01J2204/007—Aspects relating to the heat-exchange of the feed or outlet devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Seasonings (AREA)
Abstract
The invention gives a Maillard reaction device suitable for a tobacco concentrate. A steam heating jacket is mounted outside a reaction tank body; a stirring impeller of a stirring component extends into the reaction tank body; a heat exchanger of a condensing component is communicated with the reaction tank body through a steam inlet pipe and a water outlet pipe; a cold source passes through a refrigerant channel of the heat exchanger. The condensing component is utilized for changing steam evaporated by the tobacco concentrate into a liquid state through the heat exchanger again. The invention further gives a use method of the device, which comprises the following steps: adding the tobacco concentrate into the reaction tank body and starting the stirring component when a liquid level reaches 30 percent; adding a material and heating the material and the tobacco concentrate through the steam heating jacket when the liquid level reaches 60 percent, and the temperature is lower than a set value; stopping adding the tobacco concentrate when the liquid level reaches 70-80 percent; evaporating the tobacco concentrate, enabling the evaporated tobacco concentrate to enter the heat exchanger, and changing into a liquid state again to flow into the reaction tank body; completing the reaction. Under the situation of sufficient reaction, fragrance components in the tobacco concentrate are reserved.
Description
Technical field
The present invention relates to a kind of Maillard reaction device suitable for tobacco concentrate.
The invention further relates to a kind of using method of the Maillard reaction device suitable for tobacco concentrate.
Background technology
Maillard reaction is one of the main path to form tobacco characteristic chicken flavor, and tobacco is in modulation, ageing, processing and fires
During suction, all along with different degrees of non enzymatic browning reacton, many flavor components are produced.At present, many cigar mills exist
While allocating cigarette composition meticulously, the research of additional fumet is more devoted to, to make up the caused cigarette fragrance of tar reduction institute not
The defect of foot, and application multiple favor of the Maillard reaction in terms of cigarette flavouring.Maillard reaction is assert by internal authority mechanism
Prepared essence base is " natural ", and is widely adopted in new flavouring essence for tobacco.Reaction class spices (i.e. Mei Lade
Reactant), always there is the spices of using value particularly important on tobacco and food and pole.
Affecting the factor of tobacco concentrate Maillard reaction has temperature, temperature retention time and tobacco concentrate concentration etc., so
Need aborning for these influence factors are controlled；But existing Maillard reaction device is during the course of the reaction, heating
Temperature is too high or heating is violent, causes the flood irrigation easy to foaming of tobacco concentrate, causes tobacco concentrate and the essence thing for wherein adding
Matter loss, waste, while during the course of the reaction tobacco concentrate is heated to need the insulation long period to carry out instead after design temperature
Should, and high temperature can cause tobacco concentrate to evaporate, the flavor component volatilization loss in tobacco concentrate, reduce tobacco concentrate matter
Amount.
The content of the invention
The technical problem to be solved is to provide a kind of concentrating suitable for tobacco for reduction tobacco concentrate evaporation
The Maillard reaction device of liquid.
The technical problem to be solved is also to provide a kind of Maillard reaction device suitable for tobacco concentrate
Using method.
To solve above-mentioned technical problem, the invention provides a kind of Maillard reaction device suitable for tobacco concentrate,
Including reacting tank body, steam heating jacket, mixing component, reacting tank body is provided with charging aperture, dog-house, discharging opening, and steam adds
Thermal jacket is wrapped in reacting tank body outside, and steam heating jacket is provided with steam inlet, steam condensate (SC) outlet, mixing component bag
Motor and agitator arm are included, agitator arm is stretched in reacting tank body；
Also include condensation, condensation includes thering is heat exchanger channels in heat exchanger, steam inlet pipe and outlet pipe, heat exchanger
And refrigerant passage, steam inlet pipe one end connects the upper end of the heat exchanger channels top of heat exchanger, the steam inlet pipe other end and reacting tank body
Communicate, outlet pipe one end connects the heat exchanger channels end of heat exchanger, and the other end of outlet pipe is communicated with reacting tank body, outside
Low-temperature receiver flows in and out heat exchanger through the refrigerant passage of heat exchanger.
After using such structure, the steam that tobacco concentrate evaporates is input into heat by steam inlet pipe using condensation
In the heat exchanger channels of exchanger, and there is heat exchange with the coolant of refrigerant passage, liquid is changed into again, eventually through water outlet
Pipe is returned in reacting tank body.
During Maillard reaction, tobacco concentrate steam is changed into liquid and returns again tobacco concentrate by condensation
Stream reacting tank body, it is ensured that tobacco concentrate concentration, stable tobacco concentrate quality reduces tobacco concentrate in pyroreaction mistake
Flavor component volatilization in journey, loss, stable tobacco concentrate quality.
For the clearer technology contents for understanding the present invention, below this is applied to into the Maillard reaction of tobacco concentrate
Device is referred to as this Maillard reaction device.
The reacting tank body upper end of this Maillard reaction device is provided with safety valve, and pressure is higher than preset value in reacting tank body
When, safety valve opens row pressure；After using such structure, it is ensured that pressure is excessive in reacting tank body, it is to avoid in reacting tank body
Pressure is excessive.
Magnetic valve is provided with the steam inlet of the steam heating jacket of this Maillard reaction device；Using such structure
Afterwards, the purpose of control opening and closing steam inlet can be reached by controlling magnetic valve.
To solve above-mentioned technical problem, present invention also offers a kind of above-mentioned Mei Lade suitable for tobacco concentrate is anti-
The using method of device is answered, is comprised the following steps：
A) discharging opening of reacting tank body is closed, from the charging aperture of reacting tank body the tobacco concentrate of Jing meterings is added, work as retort
When in vivo liquid level reaches 30%, start the motor of mixing component, drive agitator arm to rotate；
B) material required for Maillard reaction, charging is added to close dog-house after finishing from the dog-house of reacting tank body；
c）When material liquid level reaches 60%, temperature sensor is arrived according to the temperature of retort vivo detection, temperature sensor senses
If temperature be less than setting value, the steam inlet of steam heating jacket is opened, and outside steam is entered into by steam inlet
In steam heating jacket, material in reacting tank body and tobacco concentrate are heated, the condensation formed in steam heating jacket
Water is discharged by steam condensate (SC) outlet；
d）When material addition is to setting value, when now liquid level reaches 75～80% in reacting tank body, the charging of reacting tank body is closed
Mouthful, stop adding tobacco concentrate into reacting tank body, meet the tobacco concentrate per 1.5m and add 80～120kg of material；
E) when in reacting tank body material be heated to design temperature, the steam inlet of steam heating jacket is closed, and insulation starts, and is reacted
Tobacco concentrate evaporation in tank body, the tobacco concentrate Jing steam inlet pipes of evaporation enter the heat exchanger channels of heat exchanger, and with process
There is heat exchange in the external source of the refrigerant passage of heat exchanger, the tobacco concentrate of evaporation is changed into liquid by outlet pipe again
Flow in reacting tank body；
F) in insulating process, tobacco concentration liquid temp drops as follows in reacting tank body, after design temperature, steam heating jacket
Steam inlet is opened, and continues to proceed material in reacting tank body and tobacco concentrate heating, after design temperature to be achieved, is steamed
The steam inlet of vapour heating jacket is closed；
G) after the completion of reacting, discharging opening is opened, tobacco concentrate pump in retort is delivered to into next process, complete whole reaction
Process.
After using such method, achievable heating, heating process are controllable, and tobacco concentrate is sufficient in Maillard reaction
In the case of, the flavor component in tobacco concentrate is retained to greatest extent.
It is to prevent feed liquid in tank from foam is produced in heating process, causing that liquid level reaches 75～80% in reacting tank body
Flood irrigation.
Description of the drawings
Fig. 1 is the structural representation of this Maillard reaction device embodiment.
Specific embodiment
As shown in Figure 1
This Maillard reaction device includes reacting tank body 1, steam heating jacket 2, mixing component and condensation.
Reacting tank body 1 is provided with charging aperture 11, dog-house 13, top and takes off lid, observation visor 15, discharging opening 14, reacting tank body 1
Upper end is provided with safety valve 12, and when pressure is higher than preset value in reacting tank body 1, safety valve 12 opens row pressure, charging aperture 11 and throwing
Material mouth 13 is located at the upper end of reacting tank body 1, and discharging opening 14 is located in the bottom of reacting tank body 1, reacting tank body 1 and is additionally provided with temperature biography
Sensor and liquid level sensor.
Steam heating jacket 2 is wrapped in the outside of reacting tank body 1, and it is cold that steam heating jacket 2 is provided with steam inlet 21, steam
Solidifying water out 22, at the steam inlet 21 of steam heating jacket 2 magnetic valve 23 is provided with.
Mixing component includes motor 32 and agitator arm 31, and agitator arm 31 is stretched in reacting tank body 1.
Condensation includes heat exchanger 41, steam inlet pipe 42 and outlet pipe 43, the one end of steam inlet pipe 42 connection heat exchanger 41
Heat exchanger channels 41a tops, the other end of steam inlet pipe 42 communicates with the upper end of reacting tank body 1, the connection heat exchange of the one end of outlet pipe 43
The heat exchanger channels 41a ends of device 41, the other end of outlet pipe 43 is communicated with reacting tank body 1, and outside low-temperature receiver is through heat exchanger
41 refrigerant passage 41b flows in and out heat exchanger 41.
It is concrete to introduce using the using method of this Maillard reaction device with reference to above-mentioned Maillard reaction apparatus structure
（The Maillard reaction method of tobacco concentrate is carried out using this Maillard reaction device）；Comprise the following steps：
A) reacting tank body 1 closes the discharging opening 14 of reacting tank body 1, from reacting tank body using the material in front emptying reacting tank body 1
1 charging aperture 11 adds the tobacco concentrate of Jing meterings, when liquid level reaches 30% in reacting tank body 1, starts the electricity of mixing component
Machine 32, drives agitator arm 31 to rotate；
B) material required for Maillard reaction, charging is added to close dog-house 13 after finishing from the dog-house 13 of reacting tank body 1,
Meet the tobacco concentrate per 1.5m and add material 80kg（The tobacco concentrate for being not limited to every 1.5m herein adds material
80kg, can be according to actual Maillard reaction needs, and the tobacco concentrate per 1.5m adds material 90kg or 120kg all for just
Often scope, is all up due reaction effect）；
c）When material liquid level reaches 60%, temperature sensor is according to the temperature detected in reacting tank body 1, temperature sensor senses
If the temperature for arriving is less than setting value, the steam inlet 21 of steam heating jacket 2 is opened, and outside steam passes through steam inlet 21
In entering into steam heating jacket 2, the material of reacting tank body 1 and tobacco concentrate are heated, formed in steam heating jacket 2
Condensed water by steam condensate (SC) outlet 22 discharge；
d）When material addition is to setting value, when now liquid level reaches 75% in reacting tank body, the charging aperture of reacting tank body 1 is closed
11, stop adding tobacco concentrate into reacting tank body 1；
E) when in reacting tank body 1 material be heated to design temperature, the steam inlet 21 of steam heating jacket 2 is closed, and insulation starts,
Tobacco concentrate evaporation in reacting tank body 1, the tobacco concentrate Jing steam inlet pipes 42 of evaporation enter the heat exchanger channels of heat exchanger 41
41a, and there is heat exchange with the external source of the refrigerant passage 41b through heat exchanger 41, the tobacco concentrate of evaporation is again
It is changed into liquid to flow in reacting tank body 1 by outlet pipe 43；
F) in insulating process, tobacco concentration liquid temp drops as follows in reacting tank body 1, after design temperature, steam heating jacket 2
Steam inlet 21 open, continue to material in reacting tank body 1 and tobacco concentrate proceed heating, design temperature to be achieved
Afterwards, the steam inlet 21 of steam heating jacket 2 is closed；
G) after the completion of reacting, discharging opening 14 is opened, tobacco concentrate pump in retort is delivered to into next process, complete whole anti-
Answer process.
During the course of the reaction, material state in tank can be checked by observing visor 15 in, and when in retort
When pressure is more than 1bar, safety valve 12 automatically turns on row pressure, and safety valve 12 is automatically switched off after row pressure.
This Maillard reaction device can make whole reaction realize automatic business processing by DCS system control.
Above-described is only one embodiment of the present invention, it is noted that for one of ordinary skill in the art
For, under the premise without departing from the principles of the invention, some modifications and improvement can also be made, these also should be regarded as belonging to this
Bright protection domain, such as：Material liquid level is not only limited to 75%, needs liquid level to reach 78% or 80% according to reaction and all can be
's.
Claims (4)
1. a kind of Maillard reaction device suitable for tobacco concentrate, including reacting tank body, steam heating jacket, stirring group
Part, reacting tank body is provided with charging aperture, dog-house, discharging opening, and steam heating jacket is wrapped in reacting tank body outside, steam heating
Chuck is provided with steam inlet, steam condensate (SC) outlet, and mixing component includes motor and agitator arm, and agitator arm stretches into reaction
In tank body；
It is characterized by：
Also include condensation, condensation includes thering is heat exchanger channels in heat exchanger, steam inlet pipe and outlet pipe, heat exchanger
And refrigerant passage, steam inlet pipe one end connects the upper end of the heat exchanger channels top of heat exchanger, the steam inlet pipe other end and reacting tank body
Communicate, outlet pipe one end connects the heat exchanger channels end of heat exchanger, and the other end of outlet pipe is communicated with reacting tank body, outside
Low-temperature receiver flows in and out heat exchanger through the refrigerant passage of heat exchanger.
2. the Maillard reaction device suitable for tobacco concentrate according to claim 1, is characterized in that：
Described reacting tank body upper end is provided with safety valve, and when pressure is higher than preset value in reacting tank body, safety valve opens row pressure.
3. the Maillard reaction device suitable for tobacco concentrate according to claim 1, is characterized in that：
Magnetic valve is provided with the steam inlet of described steam heating jacket.
4. a kind of use of the Maillard reaction device for being applied to tobacco concentrate as claimed any one in claims 1 to 3
Method, comprises the following steps：
A) discharging opening of reacting tank body is closed, from the charging aperture of reacting tank body the tobacco concentrate of Jing meterings is added, work as retort
When in vivo liquid level reaches 30%, start the motor of mixing component, drive agitator arm to rotate；
B) material required for Maillard reaction, charging is added to close dog-house after finishing from the dog-house of reacting tank body；
c）When material liquid level reaches 60%, temperature sensor is arrived according to the temperature of retort vivo detection, temperature sensor senses
If temperature be less than setting value, the steam inlet of steam heating jacket is opened, and outside steam is entered into by steam inlet
In steam heating jacket, material in reacting tank body and tobacco concentrate are heated, the condensation formed in steam heating jacket
Water is discharged by steam condensate (SC) outlet；
d）When material addition is to setting value, when now liquid level reaches 75～80% in reacting tank body, the charging of reacting tank body is closed
Mouthful, stop adding tobacco concentrate into reacting tank body, meet the tobacco concentrate per 1.5m and add 80～120kg of material；
E) when in reacting tank body material be heated to design temperature, the steam inlet of steam heating jacket is closed, and insulation starts, and is reacted
Tobacco concentrate evaporation in tank body, the tobacco concentrate Jing steam inlet pipes of evaporation enter the heat exchanger channels of heat exchanger, and with process
There is heat exchange in the external source of the refrigerant passage of heat exchanger, the tobacco concentrate of evaporation is changed into liquid by outlet pipe again
Flow in reacting tank body；
F) in insulating process, tobacco concentration liquid temp drops as follows in reacting tank body, after design temperature, steam heating jacket
Steam inlet is opened, and continues to proceed material in reacting tank body and tobacco concentrate heating, after design temperature to be achieved, is steamed
The steam inlet of vapour heating jacket is closed；
G) after the completion of reacting, discharging opening is opened, tobacco concentrate pump in retort is delivered to into next process, complete whole reaction
Process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710103989.2A CN106635426A (en) | 2017-02-24 | 2017-02-24 | Maillard reaction device suitable for tobacco concentrate and use method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710103989.2A CN106635426A (en) | 2017-02-24 | 2017-02-24 | Maillard reaction device suitable for tobacco concentrate and use method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106635426A true CN106635426A (en) | 2017-05-10 |
Family
ID=58847534
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710103989.2A Pending CN106635426A (en) | 2017-02-24 | 2017-02-24 | Maillard reaction device suitable for tobacco concentrate and use method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106635426A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110973563A (en) * | 2019-11-14 | 2020-04-10 | 浙江味央科技有限公司 | Seasoning production method and seasoning |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202212197U (en) * | 2011-07-29 | 2012-05-09 | 黄鹤楼香精香料有限公司 | Novel Maillard reaction kettle |
| CN104474997A (en) * | 2014-11-24 | 2015-04-01 | 湖北中烟工业有限责任公司 | Maillard reaction cooling device and rapid cooling method thereof |
| CN206502794U (en) * | 2017-02-24 | 2017-09-19 | 安徽中烟再造烟叶科技有限责任公司 | Suitable for the Maillard reaction device of tobacco concentrate |
-
2017
- 2017-02-24 CN CN201710103989.2A patent/CN106635426A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202212197U (en) * | 2011-07-29 | 2012-05-09 | 黄鹤楼香精香料有限公司 | Novel Maillard reaction kettle |
| CN104474997A (en) * | 2014-11-24 | 2015-04-01 | 湖北中烟工业有限责任公司 | Maillard reaction cooling device and rapid cooling method thereof |
| CN206502794U (en) * | 2017-02-24 | 2017-09-19 | 安徽中烟再造烟叶科技有限责任公司 | Suitable for the Maillard reaction device of tobacco concentrate |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110973563A (en) * | 2019-11-14 | 2020-04-10 | 浙江味央科技有限公司 | Seasoning production method and seasoning |
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Application publication date: 20170510 |
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