CN205731204U - Maillard reaction still - Google Patents

Maillard reaction still Download PDF

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Publication number
CN205731204U
CN205731204U CN201620668188.1U CN201620668188U CN205731204U CN 205731204 U CN205731204 U CN 205731204U CN 201620668188 U CN201620668188 U CN 201620668188U CN 205731204 U CN205731204 U CN 205731204U
Authority
CN
China
Prior art keywords
kettle
maillard reaction
reaction still
sleeve
circulating pump
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
CN201620668188.1U
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Chinese (zh)
Inventor
谢义芹
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.)
Tianjin Kang Hongsheng Generation Industrial Co Ltd
Original Assignee
Tianjin Kang Hongsheng Generation Industrial 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 Tianjin Kang Hongsheng Generation Industrial Co Ltd filed Critical Tianjin Kang Hongsheng Generation Industrial Co Ltd
Priority to CN201620668188.1U priority Critical patent/CN205731204U/en
Application granted granted Critical
Publication of CN205731204U publication Critical patent/CN205731204U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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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, steam inlet and steam (vapor) outlet it is communicated with on heater, kettle is outside equipped with circulating pump, the separation sleeve of bottom opening it is connected with in kettle, it is provided with suction tube between circulating pump and separation set, suction tube one end is stretched in separation sleeve from separating sleeve top, the other end connects with circulating pump, separate to be formed between sleeve and heater and add temperature gap, heating gap location is provided with spraying pack unit, spraying pack unit connects with circulating pump, reach circulation more sufficiently purpose.

Description

Maillard reaction still
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.The equipment of conventional process Maillard reaction is the oil bath reacting by heating still of band stirring, is Mei Lade with this reactor During reaction, oil bath heats up relatively slow, and it is uneven to be heated in whipping process, and Maillard reaction can not be carried out completely.And existing U.S.A draws Moral reactor refers to the Chinese patent of Application No. 201120274229.6, and it includes reactor, and reactor top is equipped with cold Condenser, reactor is externally provided with insulation jacket, and the top of reactor is provided with charging aperture, and reactor is built with spiral triangular heat Device, heater is connected with steam inlet and steam (vapor) outlet, and the outlet at bottom of reactor is connected by pipeline circulating pump, circulating pump It is connected one cyclic feeding system of composition by pipeline with the material shower nozzle being contained in reactor, circulates the pipe that delivery side of pump connects Equipped with outlet valve and detector on road.The PH value of detector energy the real time measure material, temperature and color change.Its quick heating, Reaction is heated evenly, and can monitor the change of the PH value of Maillard reaction material, temperature and color in real time, U.S. of gained Maillard reaction product quality is high.
Common heater is positioned on the inwall of kettle, and the material at middle part can not thermally equivalent, logical in prior art Cross circulating pump to be circulated.But simply by the top that is recycled to of bottom, circulate the most insufficient.
Utility model content
The purpose of this utility model is to provide a kind of circulation more sufficiently 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, heater is communicated with steam and enters Mouth and steam (vapor) outlet, kettle is outside equipped with circulating pump, is connected with the separation sleeve of bottom opening in kettle, and circulating pump overlaps with separating Between be provided with suction tube, suction tube one end from separate sleeve top stretch into separation sleeve in, the other end connects with circulating pump, divide Being formed between spacer cylinder and heater and add temperature gap, heating gap location is provided with spraying pack unit, and spraying pack unit connects with circulating pump.
By using technique scheme, material is heated by heater, separates sleeve and material inside and outside is separated, material Can enter from the bottom separating sleeve, the material sucking-off separated in sleeve is sprayed into through circulating pump and adds temperature gap by suction tube Interior (namely separating sleeve outer), being constituted a circulation with this, the material on such side and the material of bottom are the most more filled Point flowing, heating more uniform.
It is also preferred that the left spraying pack unit is multiple and is circularly and evenly distributed.
By using technique scheme, during sprinkling, material is more uniform, and circulating-heating is more convenient fast.
It is also preferred that the left separate sleeve inner hollow to form heating chamber, heating chamber connects with heater.
By using technique scheme, separate set and also function to heat effect, it is higher that the efficiency of heating surface is so set, Heating the most more abundant.
It is also preferred that the left the top separating sleeve is tapered, suction tube is fixed in the middle part separating sleeve top.
By using technique scheme, material is not easy to remain in when entering from charging aperture or spraying pack unit enters point The top of spacer, material can slide along inclined-plane, it is to avoid material remained at top and goes bad for a long time.
It is also preferred that the left the distance separated between sleeve 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 connected by pipeline between spraying pack unit with circulating pump, pipeline body between the two be provided with detection mouth and Detector.
By using technique scheme, in cyclic process, can be sentenced by the material of detector detection detection mouth Whether disconnected material meets the requirements, thus controls relevant parameter, it is ensured that the quality of product.
It is also preferred that the left the cross section of heater is triangular in shape, heater is distributed twist.
By using technique scheme so that heater contacts more abundant with material, heating Quick uniform more.
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 Maillard reaction still structural representation in embodiment 1;
Fig. 2 is Maillard reaction still structural representation in embodiment 2.
In figure, 1, kettle;11, charging aperture;2, condenser;3, circulating pump;31, spraying pack unit;32, detection mouth;33, discharging Mouthful;34, suction tube;4, detector;5, insulation jacket;6, sleeve is separated;61, temperature gap is added;62, support;63, connecting tube; 7、 Observation window;8, heater;81, steam inlet;82, steam (vapor) outlet.
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 2 simultaneously, is connected with observation window 7, is coated with outside kettle 1 on the sidewall of kettle 1 Insulation jacket 5, the bottom of kettle 1 is provided with discharging opening 33.
It is connected with heater 8 on the inwall of kettle 1, heater 8 is provided with steam inlet 81 and steam (vapor) outlet 82, heating The cross section of device 8 can be triangular in shape, heater 8 in a tubular form and entirety twist.Being internally provided with of kettle 1 separates sleeve 6, Separate sleeve 6 and carry out affixed by support 62 with kettle 1.The distance separated between sleeve 6 and kettle 1 diapire is 5cm to 10cm Between.
The top separating sleeve 6 is connected with suction tube 34, and suction tube 34 is positioned at the middle part separating sleeve 6, and suction tube 34 insert in separation sleeve 6, and the degree of depth of insertion can separate 1/3rd of sleeve 6 height.
And the outside of kettle 1 is provided with circulating pump 3, suction tube 34 connects with circulating pump 3.Within separating sleeve 6 and kettle 1 Being formed between wall and add temperature gap 61, add temperature gap 61 is provided above spraying pack unit 31, and spraying pack unit 31 can be shower nozzle, and shower nozzle leads to Piping is connected with circulating pump 3.It is communicated with detection mouth 32 on pipeline between shower nozzle and circulating pump 3, arranges at detection mouth 32 There is detector 4.
Shower nozzle can be one, two even more than, meet and discuss in the case of multiple shower nozzles and can divide the most uniformly Cloth.
And the tapered setting in top separating sleeve 6, there is certain gradient, can be along under inclined-plane when material enters Sliding.
When producing, pouring in reactor by required material by charging aperture 11, start circulating pump 3, material is from separating set Sucking-off in cylinder 6, material arrives detector 4 through circulating pump 3 can show PH value, temperature and the refractive power of material, then arrives shower nozzle, Material returns to add temperature gap 61, and concrete flow direction of material refers in figure shown in arrow.Acid number needed for regulation technique, reaches After requirement, open steam inlet 81, steam (vapor) outlet 82 and condenser 2, by heater 8 and circulating pump 3, material is heated to 90-120 DEG C, heating-up temperature can be controlled by detector 4, from newly after in material, volatile component is condensed by condenser 2 Return in reactor.The product quality quality of Maillard reaction gained can be judged by the refractive power of detector 4, and refractive power reaches work Skill i.e. may know that Maillard reaction completes after requiring.
Embodiment 2: as in figure 2 it is shown, separate sleeve 6 inner hollow to form heating chamber, be provided with between heating chamber and heater 8 Connecting tube 63, both are connected by connecting tube 63 so that the steam in heater 8 can flow through heating chamber, separate sleeve 6 and also can Play certain heat effect.
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 (10)

1. a Maillard reaction still, including kettle (1), kettle (1) top is provided with charging aperture (11), on the inwall of kettle (1) It is provided with heater (8), heater (8) is communicated with steam inlet (81) and steam (vapor) outlet (82), it is characterised in that: kettle (1) it is outside equipped with circulating pump (3), in kettle (1), is connected with the separation sleeve (6) of bottom opening, circulating pump (3) and separation set Between be provided with suction tube (34), suction tube (34) one end is stretched in separation sleeve (6) from separating sleeve (6) top, the other end and Circulating pump (3) connects, and is formed and adds temperature gap (61) between separation sleeve (6) and heater (8), adds temperature gap (61) place and arranges Spraying pack unit (31), spraying pack unit (31) is had to connect with circulating pump (3).
Maillard reaction still the most according to claim 1, it is characterised in that: spraying pack unit (31) is multiple and the most uniform Distribution.
Maillard reaction still the most according to claim 1, it is characterised in that: separate sleeve (6) inner hollow and form heating Chamber, heating chamber connects with heater (8).
Maillard reaction still the most according to claim 1, it is characterised in that: the top separating sleeve (6) is tapered, suction Pipe (34) is fixed in the middle part separating sleeve (6) top.
Maillard reaction still the most according to claim 1, it is characterised in that: separate between sleeve (6) and kettle (1) diapire Distance be between 5cm to 10cm.
Maillard reaction still the most according to claim 1, it is characterised in that: logical between spraying pack unit (31) and circulating pump (3) Piping connects, and pipeline body between the two is provided with detection mouth (32) and detector (4).
Maillard reaction still the most according to claim 1, it is characterised in that: the cross section of heater (8) is triangular in shape, heating Device (8) is distributed twist.
Maillard reaction still the most according to claim 1, it is characterised in that: kettle (1) is outside is connected with insulation jacket (5)。
Maillard reaction still the most according to claim 1, it is characterised in that: the top of kettle (1) is communicated with condenser (2)。
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) (7)。
CN201620668188.1U 2016-06-28 2016-06-28 Maillard reaction still Expired - Fee Related CN205731204U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620668188.1U CN205731204U (en) 2016-06-28 2016-06-28 Maillard reaction still

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620668188.1U CN205731204U (en) 2016-06-28 2016-06-28 Maillard reaction still

Publications (1)

Publication Number Publication Date
CN205731204U true CN205731204U (en) 2016-11-30

Family

ID=57382716

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620668188.1U Expired - Fee Related CN205731204U (en) 2016-06-28 2016-06-28 Maillard reaction still

Country Status (1)

Country Link
CN (1) CN205731204U (en)

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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