CN206454631U - A kind of reactor for producing polydextrose - Google Patents
A kind of reactor for producing polydextrose Download PDFInfo
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- CN206454631U CN206454631U CN201720128746.XU CN201720128746U CN206454631U CN 206454631 U CN206454631 U CN 206454631U CN 201720128746 U CN201720128746 U CN 201720128746U CN 206454631 U CN206454631 U CN 206454631U
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- heat exchanger
- exchanger tube
- polydextrose
- reactor
- housing
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Abstract
The utility model is related to a kind of reactor for producing polydextrose, belongs to technical field of chemical, for solve the usual means reaction time it is long and can not continue carry out the problem of design.The utility model is made up of housing, heat exchanger tube, deflection plate and railing；Described housing is cylindrical body, and the housing has four interfaces, has an interface respectively in longitudinal two ends disc center, is material inlet and polydextrose outlet, has an interface respectively in the side close to two ends, be heat conductive oil inlet and conduction oil outlet；Described heat exchanger tube is longitudinally regularly arranged in enclosure interior along body to carry out the critical piece of heat transfer；Described deflection plate be and the orthogonal baffle plate of heat exchanger tube；Described railing is the body of rod of fixed deflection plate.The utility model is simple in construction, the reaction time is short, course of reaction is lasting, and can effectively improve production efficiency.
Description
Technical field
The utility model belongs to technical field of chemical, and in particular to a kind of glucose response device, more particularly to a kind of
Produce the reactor of polydextrose.
Background technology
At present, the reactor of known production polydextrose, carries out generally in reactor, by kettle, transmission device, stirs
Mix device, heater, cooling device, sealing device composition.Internal heat device is simple, and inefficiency belongs to intermittent life
Production process, the reaction time generally requires 2 to 6 hours, and production process can not continue, and cost is high, and energy waste is serious.
Accordingly, it would be desirable to which a kind of reactor for producing polydextrose of utility model, to shorten the reaction time, effectively improves production
Efficiency.
The content of the invention
The purpose of this utility model is to provide a kind of reactor for producing polydextrose, and the reactor can effectively solve to gather
The technical barrier that dextrose production process can not continue, and simple in construction, easy to operate, Technological Economy is feasible.
Technical solution adopted in the utility model is：A kind of reactor for producing polydextrose, it is by housing, heat exchange
Pipe, deflection plate and railing composition；Described housing is cylindrical body, and the housing has four interfaces, in longitudinal two ends disc
There is an interface centre respectively, is material inlet and polydextrose outlet, has an interface respectively in the side close to two ends, to lead
Hot oil inlet and conduction oil outlet；Described heat exchanger tube is longitudinally regularly arranged along body to carry out the critical piece of heat transfer
In enclosure interior；Described deflection plate be and the orthogonal baffle plate of heat exchanger tube；Described railing is the body of rod of fixed deflection plate.
Further specifically optimize：The housing is cylindrical shape, and it is respectively material inlet and poly- Portugal longitudinally to have two interfaces
The outlet of grape sugar, has one in the opposite direction in two end side surfaces and axis accordant interface is that heat conductive oil inlet and conduction oil go out respectively
Mouthful.
Further specifically optimize：The heat exchanger tube is starlike arrangement mode and heat conductive oil inlet and conduction oil outlet phase
Even, every three heat exchanger tube axial connecting lines are equilateral triangle, and the length of side is 15.88mm.
Further specifically optimize：The deflection plate be and the orthogonal baffle plate of heat exchanger tube.
The beneficial effects of the utility model are：A kind of structure of reactor for producing polydextrose is simple and is using process
In it is easy to operate, reached improve production efficiency purpose, have good economic benefits.
Additional aspect and advantage of the present utility model will be set forth in part in the description, partly by from following description
In become obvious, or by it is of the present utility model practice recognize.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the accompanying drawing used required in description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, is not paying the premise of creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is a kind of reactor overlooking the structure diagram for producing polydextrose of the utility model.
Fig. 2 is a kind of reactor heat exchanger tube arrangement mode schematic diagram for producing polydextrose of the utility model.
Fig. 3 is a kind of reactor baffle arrangement schematic diagram for producing polydextrose of the utility model.
Fig. 4 is a kind of reactor use state schematic diagram for producing polydextrose of the utility model.
Fig. 5 is a kind of reactor heat exchanger tube internal structure schematic diagram for producing polydextrose of the utility model.
Marginal data：1- housings；2- heat exchanger tubes；3- deflection plates；4- railings；5- material inlets；6- polydextroses are exported；7-
Heat conductive oil inlet；8- conduction oil outlets.
Embodiment
The exemplary embodiment of the disclosure is more fully described below with reference to accompanying drawings.Although showing the disclosure in accompanying drawing
Exemplary embodiment, it being understood, however, that may be realized in various forms the disclosure without should be by embodiments set forth here
Limited.On the contrary, these embodiments are provided to facilitate a more thoroughly understanding of the present invention, and can be by the scope of the present disclosure
Complete conveys to those skilled in the art.
In description of the present utility model, it is to be understood that term " longitudinal direction ", " transverse direction ", " on ", " under ", " preceding ",
The orientation or position relationship of the instruction such as " rear ", "left", "right", " vertical ", " level ", " top ", " bottom ", " interior ", " outer " be based on
Orientation shown in the drawings or position relationship, are for only for ease of description the utility model, rather than indicate or imply signified dress
Put or element there must be specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to the utility model
Limitation.
The utility model is described further below in conjunction with the accompanying drawings.
As shown in Figure 1, the utility model one kind production polydextrose, mainly by housing 1, heat exchanger tube 2, the and of deflection plate 3
Railing 4 is constituted；Described housing 1 is cylindrical body, and the housing has four interfaces, has one respectively in longitudinal two ends disc center
Individual interface, is material inlet 5 and polydextrose outlet 6, has an interface respectively in the side close to two ends, be heat conductive oil inlet
7 and conduction oil outlet 8；Described heat exchanger tube 2 is longitudinally regularly arranged in housing along body to carry out the critical piece of heat transfer
Inside 1；Described deflection plate 3 be and the orthogonal baffle plate of heat exchanger tube 2；Described railing 4 is the body of rod of fixed deflection plate 3.
As shown in figure 4, in use, first checking for reactor shell 1 ensures normal operation, next takes 20% lemon in proportion
Acid solution, 96% glucose and sorbitol fluid, by 20% citric acid solution, 96% glucose and sorbitol fluid pass through
Inside the injection housing 1 of material inlet 5,2bar165 DEG C of conduction oil is then injected to inside heat exchanger tube 2 by heat conductive oil inlet 7, treated
Reaction, which is finished, takes out polydextrose from polydextrose outlet 6, and conduction oil takes out from conduction oil outlet 8.
Application method of the present utility model is：It is a kind of to produce the reactor of polydextrose, in use, first checking for reactor
Housing ensures normal operation, secondly 20% citric acid solution, 96% glucose and sorbitol fluid is taken in proportion, by 20% lemon
Lemon acid solution, 96% glucose and sorbitol fluid inject enclosure interior by material inlet, then pass through heat conductive oil inlet
2bar165 DEG C of conduction oil is injected to inside heat exchanger tube, and question response is finished to export polydextrose from polydextrose and taken out, conduction oil
Taken out from conduction oil outlet.
Operation principle of the present utility model is：A kind of reactor for producing polydextrose, the first inside reactor are used
The mode of the starlike arrangement of heat exchanger tube, drastically increases heat exchange efficiency；Then continue to ensure that by the way of heat supply using heat exchanger tube
The lasting purpose of course of reaction.
While there has been shown and described that embodiment of the present utility model, it will be understood by those skilled in the art that：
These embodiments can be carried out with a variety of changes, modification in the case where not departing from principle of the present utility model and objective, replaced
And modification, scope of the present utility model limits by claim and its equivalent.
Claims (4)
1. a kind of reactor for producing polydextrose, it is characterised in that it is made up of housing, heat exchanger tube, deflection plate and railing；Institute
The housing stated is cylindrical body, and the housing has four interfaces, has an interface respectively in longitudinal two ends disc center, is raw material
, there is an interface import and polydextrose outlet in the side close to two ends, is heat conductive oil inlet and conduction oil outlet respectively；Institute
The heat exchanger tube stated is longitudinally regularly arranged in enclosure interior along body；Described deflection plate be and the orthogonal baffle plate of heat exchanger tube；
Described railing is the body of rod of fixed deflection plate；The inside of the heat exchanger tube is provided with the water conservancy diversion line in threading helical；It is described to lead
The flight pitch of flow liner is 20-40mm, and the bar number of the water conservancy diversion line is 1-3 bars.
2. a kind of reactor for producing polydextrose according to claim 1, it is characterised in that：The housing is cylinder
Shape, it is respectively material inlet and polydextrose outlet longitudinally to have two interfaces, two end side surfaces have respectively one it is in opposite direction and
Axis accordant interface is heat conductive oil inlet and conduction oil outlet.
3. a kind of reactor for producing polydextrose according to claim 1, it is characterised in that：The heat exchanger tube is starlike
Arrangement mode is connected with heat conductive oil inlet and conduction oil outlet, and every three heat exchanger tube axial connecting lines are equilateral triangle, and the length of side is
15.88mm。
4. a kind of reactor for producing polydextrose according to claim 1, it is characterised in that：The deflection plate is with changing
The orthogonal baffle plate of heat pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720128746.XU CN206454631U (en) | 2017-02-13 | 2017-02-13 | A kind of reactor for producing polydextrose |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720128746.XU CN206454631U (en) | 2017-02-13 | 2017-02-13 | A kind of reactor for producing polydextrose |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206454631U true CN206454631U (en) | 2017-09-01 |
Family
ID=59693858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720128746.XU Active CN206454631U (en) | 2017-02-13 | 2017-02-13 | A kind of reactor for producing polydextrose |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206454631U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108084294A (en) * | 2017-12-27 | 2018-05-29 | 人良生物科技（上海）有限公司 | A kind of production technology of high-purity polydextrose |
-
2017
- 2017-02-13 CN CN201720128746.XU patent/CN206454631U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108084294A (en) * | 2017-12-27 | 2018-05-29 | 人良生物科技（上海）有限公司 | A kind of production technology of high-purity polydextrose |
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