CN202212197U - Novel Maillard reaction kettle - Google Patents

Novel Maillard reaction kettle Download PDF

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Publication number
CN202212197U
CN202212197U CN2011202742296U CN201120274229U CN202212197U CN 202212197 U CN202212197 U CN 202212197U CN 2011202742296 U CN2011202742296 U CN 2011202742296U CN 201120274229 U CN201120274229 U CN 201120274229U CN 202212197 U CN202212197 U CN 202212197U
Authority
CN
China
Prior art keywords
reaction kettle
agitated reactor
circulating pump
maillard reaction
outlet
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.)
Expired - Fee Related
Application number
CN2011202742296U
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Chinese (zh)
Inventor
张辉
黄龙
喻世涛
张寅�
陈金强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
YELLOW CRANE TOWER FLAVORS PERFUME CO Ltd
Original Assignee
YELLOW CRANE TOWER FLAVORS PERFUME CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by YELLOW CRANE TOWER FLAVORS PERFUME CO Ltd filed Critical YELLOW CRANE TOWER FLAVORS PERFUME CO Ltd
Priority to CN2011202742296U priority Critical patent/CN202212197U/en
Application granted granted Critical
Publication of CN202212197U publication Critical patent/CN202212197U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a reaction kettle, in particular to a novel Maillard reaction kettle, which comprises a reaction kettle. A condenser is installed at the top part of the reaction kettle; a heat insulation jacket is arranged outside the reaction kettle; and a feed port is arranged at the top part of the reaction kettle. The novel Maillard reaction kettle is characterized in that a threaded triangular heater is installed in the reaction kettle and is connected with a steam inlet and a steam outlet; an outlet at the bottom part of the reaction kettle is connected with a circulating pump through a pipeline; the circulating pump is connected with a material spray head installed in the reaction kettle to form a cyclic feeding system; and a discharge valve and a detector are installed on a pipeline connected with an outlet of the circulating pump. The detector can determine the PH value, the temperature and the color change of materials on a real-time basis. The utility model has the beneficial effects that the temperature rising speed is quick; the reaction and the heating are uniform; and the PH value, the temperature and the color change of the Maillard reaction materials can be monitored on a real-time basis, so that an obtained Maillard reaction product has high quality.

Description

A kind of novel Maillard reaction still
Technical field
The utility model relates to a kind of agitated reactor, specifically a kind of novel Maillard reaction still.
Background technology
Maillard reaction is the reaction between carbonyls (reduced sugar) and amino-compound (amino acid and protein).Maillard reaction can produce a large amount of extremely fragrant compositions, has been widely used in preparing various meats and essence spice for cigarette, fumet.The equipment of conventional process Maillard reaction is the oil bath reacting by heating still that band stirs, when doing Maillard reaction with this agitated reactor the oil bath intensification slower, and it is inhomogeneous to be heated in the whipping process, Maillard reaction can not carry out fully.Therefore inventing a kind of novel Maillard reaction still is highly profitable.
Summary of the invention
The purpose of the utility model is exactly the above-mentioned deficiency to prior art, and a kind of novel Maillard reaction still is provided.Its quick heating, reaction are heated evenly, can monitor in real time pH value, temperature and the change color of Maillard reaction material, and the Maillard reaction product quality of gained is high.
The technical scheme of the utility model is achieved in that it comprises agitated reactor; Condenser is equipped with at the agitated reactor top; Agitated reactor is provided with insulation jacket outward, and the top of agitated reactor is provided with charging aperture, it is characterized in that: spiral triangle heater is housed in the agitated reactor; Heater is connected with steam (vapor) outlet with steam inlet; The outlet at bottom of agitated reactor is connected with circulating pump through pipeline, and circulating pump connects to form a feeding cycle system through pipeline and the material shower nozzle that is contained in the agitated reactor, on the pipeline that outlet of circulating pump connects bleeder valve and detector is housed.PH value, temperature and the change color of detector ability The real time measure material.
The utility model Maillard reaction efficient is high, energy consumption is low, simple in structure, easy operating, occupied ground are few; Can reach the needed temperature of Maillard reaction within a short period of time during the heater heating; Because reative cell is provided with the heat tracing chuck, this temperature can keep constant in a long time again.Set circulating pump can play the effect of stirring with the top of material from the transportation of reative cell bottom, can well material be heated evenly again.The effumability composition condensation that produces when set condenser can will react is got back in the reative cell, keeps the original characteristic of Maillard reaction product.Set detection means all links to each other with monitoring system, can control according to different Maillard reaction requirement and technology, makes the automation control and the production efficiency of a whole set of agitated reactor improve greatly.Set cleaning device is convenient in every batch materials reaction finishing back equipment cleaned, and has guaranteed to meet the GMP hygienic requirements.The agitated reactor of the utility model is to adopt the operation of sealing procedural style, the stable and reliable product quality of producing, and energy consumption is low, and can not damage and contaminated environment.
Description of drawings
Fig. 1 is the structural representation of the utility model
The specific embodiment
Below in conjunction with accompanying drawing the utility model is further described:
As shown in Figure 1, the utility model comprises agitated reactor 7, and condenser 9 is equipped with at agitated reactor 7 tops; Be provided with insulation jacket 12 outside the agitated reactor 7, the top of agitated reactor 7 is provided with charging aperture 1, and visor 8 is housed on the agitated reactor 7; Spiral triangle heater 5 is housed in the agitated reactor; Heater 5 is connected with steam (vapor) outlet 11 with steam inlet 10, and the outlet at bottom of agitated reactor is connected with circulating pump 4 through pipeline, and circulating pump 4 connects to form a feeding cycle system through pipeline and the material shower nozzle 6 that is contained in the agitated reactor 7; The pipeline that is connected between circulating pump 4 and the shower nozzle 6 is provided with bleeder valve 3 and detector 2, pH value, temperature and change color that detector 2 can the The real time measure materials.
The course of work is following: required material is poured in the agitated reactor 7 through charging aperture 1, started circulating pump 4, material arrives pH value, temperature and the refractive power that detector 2 can show material through circulating pump 4, arrives shower nozzle 6 again, and material turns back to reative cell.Regulate the required acid number of technology; After reaching requirement; Open steam inlet 10, outlet 11 and condenser 9; Through heater 5 and circulating pump 4 material is heated to 90-120 ℃, heating-up temperature can be controlled through detector 2, in the material volatile component through condenser 9 condensations after from newly getting back in the agitated reactor 7.The product quality quality of Maillard reaction gained can judge that refractive power is promptly known the Maillard reaction completion after reaching technological requirement through the refractive power of detector 2.

Claims (1)

1. novel Maillard reaction still; It comprises agitated reactor, and condenser is equipped with at the agitated reactor top, and agitated reactor is provided with insulation jacket outward; The top of agitated reactor is provided with charging aperture; It is characterized in that: spiral triangle heater is housed in the agitated reactor, and heater is connected with steam (vapor) outlet with steam inlet, and the outlet at bottom of agitated reactor is connected with circulating pump through pipeline; Circulating pump connects to form a feeding cycle system through pipeline and the material shower nozzle that is contained in the agitated reactor, and circulating pump is provided with bleeder valve and detector with the pipeline that is connected between the shower nozzle.
CN2011202742296U 2011-07-29 2011-07-29 Novel Maillard reaction kettle Expired - Fee Related CN202212197U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011202742296U CN202212197U (en) 2011-07-29 2011-07-29 Novel Maillard reaction kettle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011202742296U CN202212197U (en) 2011-07-29 2011-07-29 Novel Maillard reaction kettle

Publications (1)

Publication Number Publication Date
CN202212197U true CN202212197U (en) 2012-05-09

Family

ID=46011469

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011202742296U Expired - Fee Related CN202212197U (en) 2011-07-29 2011-07-29 Novel Maillard reaction kettle

Country Status (1)

Country Link
CN (1) CN202212197U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN106635426A (en) * 2017-02-24 2017-05-10 安徽中烟再造烟叶科技有限责任公司 Maillard reaction device suitable for tobacco concentrate and use method
CN107261887A (en) * 2017-07-28 2017-10-20 朱明� A kind of lubricating oil blending tank
CN107261888A (en) * 2017-07-28 2017-10-20 朱明� One kind is without spindle oil mixing arrangement
CN108176325A (en) * 2018-02-27 2018-06-19 上海市杨浦区中心医院(同济大学附属杨浦医院) Barium meal mixing and heating device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN106635426A (en) * 2017-02-24 2017-05-10 安徽中烟再造烟叶科技有限责任公司 Maillard reaction device suitable for tobacco concentrate and use method
CN107261887A (en) * 2017-07-28 2017-10-20 朱明� A kind of lubricating oil blending tank
CN107261888A (en) * 2017-07-28 2017-10-20 朱明� One kind is without spindle oil mixing arrangement
CN108176325A (en) * 2018-02-27 2018-06-19 上海市杨浦区中心医院(同济大学附属杨浦医院) Barium meal mixing and heating device

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120509

Termination date: 20140729

EXPY Termination of patent right or utility model