CN206940919U - One kind sugaring crystallizing tank - Google Patents
One kind sugaring crystallizing tank Download PDFInfo
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- CN206940919U CN206940919U CN201720564609.0U CN201720564609U CN206940919U CN 206940919 U CN206940919 U CN 206940919U CN 201720564609 U CN201720564609 U CN 201720564609U CN 206940919 U CN206940919 U CN 206940919U
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- tank body
- tank
- sugaring
- heating region
- screw mandrel
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Abstract
The utility model discloses one kind sugaring crystallizing tank, including tank body, steam pipe, agitating device, drive device and the control system for controlling drive device, it is connected at the top of the tank body by connecting seat with drive device, the tank base exports provided with massecuite, the tank body includes heating region and the evaporation region above heating region, the evaporation region is provided with vacuum orifice, syrup inlet, clean entrance and evacuation port, the heating region top is provided with seed entrance, heating region bottom is provided with vapour inlet, the screw mandrel for stretching into tank interior is connected with the drive device, feed screw nut is arranged with screw mandrel, the feed screw nut is provided with the stirring vane one for stirring syrup, the steam pipe is arranged at heating region inwall in the shape of a spiral, the screw mandrel and connecting seat, seal is provided between screw mandrel and tank body.The utility model have make the technique effect that syrup is sufficiently stirred, heater is simple in construction in tank body.
Description
Technical field
It the utility model is related to sugar mill field, and in particular to one kind sugaring crystallizing tank.
Background technology
It is the key link in sugar enterprise's production process to boil sugar, and its main task is syrup in boiling pan
Certain degree of supersaturation is concentrated to, satisfactory crystallization of sucrose body is separated out and brings crystal up, good massecuite is made, then
Mother liquor is excluded by crystallization in motion and with centrifuge again, obtains the second best in quality crystallized sugar.Current most of sugar refinery generally use
Sugar is boiled in automation, reduces labour, saves energy consumption, improves sugaring efficiency.
In sugar boiling process, in order to quickly separate out crystal, the efficiency for separating out crystal is improved, it is necessary to constantly be stirred syrup
Mix.A kind of cane sugar boiling and crystal tank is disclosed in the prior art, is provided with forced circulation blade in tank body, is passed through forced circulation blade
Rotary motion is stirred continuously to syrup, the upright beam tube of ring-type is provided with tank body, for being heated to syrup.It is but existing
In technology, forced circulation blade can only rotate in same position, easily cause the syrup of top and the bottom in tank body not
It can be sufficiently stirred, so as to reduce the efficiency of sugaring, and the upright bundle tube structure of ring-type for heating syrup is complicated.
Utility model content
The purpose of this utility model is:It can only be rotated for forced circulation blade in the prior art in same position
Motion, easily causes the syrup of top and the bottom in tank body can not be sufficiently stirred, the baroque technical problem of heater,
The utility model provides a kind of sugaring crystallizing tank, is sufficiently stirred syrup in tank body, and heater is simple in construction.
The technical solution adopted in the utility model is as follows:
One kind sugaring crystallizing tank, including tank body, steam pipe, agitating device, drive device and for controlling drive device
Control system, the tank body top are connected by connecting seat with drive device, and the tank base exports provided with massecuite, the tank
Body includes heating region and the evaporation region above heating region, the evaporation region be provided with vacuum orifice, syrup inlet,
Cleaning entrance and evacuation port, the heating region top are provided with seed entrance, and heating region bottom is provided with vapour inlet, the drive
The screw mandrel for stretching into tank interior is connected with dynamic device, feed screw nut is arranged with screw mandrel, the feed screw nut, which is provided with, to be used for
The stirring vane one of syrup is stirred, the steam pipe is arranged at heating region inwall, the screw mandrel and connecting seat, silk in the shape of a spiral
Seal is provided between bar and tank body.
Further, the stirring vane one is provided with several pod apertures one.
Further, the feed screw nut bottom is provided with stirring vane two, and the stirring vane two is located at stirring vane
One lower section.
Further, the stirring vane two is identical with tank inner chamber shape and size fit, the stirring vane two are set
It is equipped with several pod apertures two.
Further, the screw mandrel bottom is provided with limited block.
Further, cleaning sprayer is provided with the tank body, the cleaning sprayer connects with cleaning entrance.
Further, the vacuum orifice, syrup inlet, cleaning entrance, evacuation port, seed entrance and vapour inlet are all provided with
It is equipped with regulating valve.
Further, the vapour inlet is provided with air gauge, and the air gauge is arranged between regulating valve and tank body.
In summary, by adopting the above-described technical solution, the beneficial effects of the utility model are:
1. being connected with the screw mandrel for stretching into tank interior in the utility model drive device, feed screw nut is arranged with screw mandrel,
Feed screw nut is provided with the stirring vane one for stirring syrup, and stirring vane one makees fortune up and down under the cooperation of feed screw nut
It is dynamic, it is sufficiently stirred the syrup of top and the bottom in tank body;The utility model steam pipe is arranged at heating region in the shape of a spiral
Inwall, simple in construction, the syrup in heating region is heated evenly;The utility model stirring vane one is provided with several pod apertures
One, guiding syrup motion, make syrup stirring more abundant;The utility model is provided with the control system for being used for controlling drive device, control
Direction of rotation and the speed for the screw mandrel being connected with drive device are made, so as to control the direction of the up and down motion of stirring vane one and speed
Degree;
2. the utility model feed screw nut bottom is provided with stirring vane two, stirring efficiency is lifted;Stirring vane two and tank
Intracoelomic cavity shape is identical and size fit, stirring vane two are provided with several pod apertures two, is easy to inner tank wall attachment
Crystal or syrup scrape, and avoid crystal or syrup from being attached to inner tank wall, further lift stirring efficiency, and make manufactured syrup
It is homogeneous.
3. the utility model screw mandrel bottom is provided with limited block, feed screw nut is limited on screw mandrel and moved up and down;
4. being provided with cleaning sprayer in the utility model tank body, it is easy to clean tank interior;
5. the utility model vacuum orifice, syrup inlet, cleaning entrance, evacuation port, seed entrance and vapour inlet are all provided with
Regulating valve is equipped with, is easy to control the quantity of various materials in the working condition and tank body of tank body;The utility model vapour inlet is set
Air gauge is equipped with, is easy to be monitored the steam air pressure for inputting tank body.
Brief description of the drawings
Fig. 1 is the utility model overall structure diagram;
Fig. 2 is the structural representation of the utility model stirring vane two;
Marked in figure:1- tank bodies;11- evaporation regions;12- heating regions;13- vacuum orifices;14- syrup inlets;15- is clear
Wash mouth;16- evacuation ports;17- seed entrances;18- vapour inlets;19- massecuites export;2- steam pipes;3- agitating devices;31-
Screw mandrel;32- feed screw nut;33- stirring vanes one;34- pod apertures one;35- stirring vanes two;36- pod apertures two;4- driving dresses
Put;5- connecting seats;6- regulating valves;7- limited blocks;8- seals;9- cleaning sprayers.
Embodiment
All features disclosed in this specification, can be with any in addition to mutually exclusive feature and/or step
Mode combines.
The utility model is elaborated below in conjunction with the accompanying drawings.
Embodiment 1, with reference to Fig. 1, Fig. 2, one kind sugaring crystallizing tank, including tank body 1, steam pipe 2, agitating device 3, driving dress
Put 4 and for controlling the control system of drive device 4, the top of tank body 1 is connected by connecting seat 5 with drive device 4, described
The bottom of tank body 1 is provided with massecuite outlet 19, and the tank body 1 includes heating region 12 and the evaporation region above heating region 12
11, the evaporation region 11 is provided with vacuum orifice 13, syrup inlet 14, cleaning entrance 15 and evacuation port 16, the heating region
12 tops are provided with seed entrance 17, and the bottom of heating region 12 is provided with vapour inlet 18, the vacuum orifice 13, syrup inlet 14,
Cleaning entrance 15, evacuation port 16, seed entrance 17 and vapour inlet 18 are provided with regulating valve 6, are easy to control the work of tank body 1
The quantity of various materials in state and tank body 1, the vapour inlet 18 are provided with air gauge, and the air gauge is arranged at regulating valve
Between 6 and tank body 1, it is easy to be monitored the steam air pressure for inputting tank body 1;It is connected with the drive device 4 and stretches into tank body 1
Internal screw mandrel 31, feed screw nut 32 is arranged with screw mandrel 31, the bottom of screw mandrel 31 is provided with limited block 7, feed screw nut 32 is limited
Moved up and down on screw mandrel 31, the feed screw nut 32 is provided with the stirring vane 1 for stirring syrup, stirring vane
One 33 are provided with several pod apertures 1, and the bottom of feed screw nut 32 is additionally provided with stirring vane 2 35, the paddle
Piece 2 35 is located at the lower section of stirring vane 1, and stirring vane 2 35 is identical with the cavity shape of tank body 1 and size fit, the stirring
Blade 2 35 is provided with several pod apertures 2 36;The steam pipe 2 is arranged at the inwall of heating region 12, the silk in the shape of a spiral
Seal 8 is provided between bar 31 and connecting seat 5, screw mandrel 31 and tank body 1, cleaning sprayer 9 is provided with the tank body 1, it is described
Cleaning sprayer 9 connects with cleaning entrance 15, is easy to being cleaned inside tank body 1.
Utility model works principle:Syrup is sent into tank body 1 by syrup inlet 14, now passes through vapour inlet 18
Steam is inputted to the steam pipe 2 of heating region 12 to be heated, steam pipe 2 is arranged at the inwall of heating region 12 in the shape of a spiral, knot
Structure is simple, and the syrup in heating region 12 is heated evenly, and will be vacuumized by vacuum orifice 13 inside tank body 1 while heating,
When being heated, drive device 4 is opened, drives screw mandrel 31 to rotate by drive device 4, the He of stirring vane 1
Stirring vane 2 35 moves up and down under the drive of feed screw nut 32, the syrup of top and the bottom in tank body 1 is fully stirred
Mix, pod apertures 1 and the further guiding syrup motion of pod apertures 2 36, the crystal that stirring vane 2 35 adheres to the inwall of tank body 1
Or syrup scrapes, avoid crystal or syrup from being attached to the inwall of tank body 1, make syrup stirring more abundant;When syrup evaporative concn controls
After quasi-stationary state, add certain Icing Sugar from seed entrance 17 and then grown as seed, crystallization on Icing Sugar seed, started
Crystallization, continue to evaporate after starting crystallization, while syrup is continuously replenished to a certain amount of, crystallization process is finally completed after abundant growing the grain;
The gas in tank body 1 is discharged by evacuation port 16 after the completion of crystallization, afterwards from massecuite made of the output of massecuite outlet 19.This reality
Be used to control the control system of drive device 4 with new be provided with, control the screw mandrel 31 being connected with drive device 4 direction of rotation and
Speed, so as to control the direction of the up and down motion of stirring vane 1 and speed.
It is embodiment of the present utility model as described above.The utility model is not limited to above-mentioned embodiment, anyone
The structure change made under enlightenment of the present utility model should be learnt, it is every that there is same or like skill with the utility model
Art scheme, each falls within the scope of protection of the utility model.
Claims (8)
1. one kind sugaring crystallizing tank, it is characterised in that including tank body (1), steam pipe (2), agitating device (3), drive device (4)
With the control system for controlling drive device (4), tank body (1) top is connected by connecting seat (5) and drive device (4)
Connect, tank body (1) bottom is provided with massecuite outlet (19), and the tank body (1) includes heating region (12) and positioned at heating region
(12) evaporation region (11) above, the evaporation region (11) are provided with vacuum orifice (13), syrup inlet (14), cleaning entrance
(15) and evacuation port (16), heating region (12) top are provided with seed entrance (17), and heating region (12) bottom, which is provided with, steams
Gas entrance (18), is connected with the drive device (4) and stretches into the internal screw mandrel (31) of tank body (1), and screw mandrel is arranged with (31)
Feed screw nut (32), the feed screw nut (32) are provided with the stirring vane one (33) for stirring syrup, the steam pipe (2)
Heating region (12) inwall is arranged in the shape of a spiral, between the screw mandrel (31) and connecting seat (5), screw mandrel (31) and tank body (1)
It is provided with seal (8).
2. sugaring crystallizing tank as claimed in claim 1, it is characterised in that the stirring vane one (33) is provided with several and led
Discharge orifice one (34).
3. sugaring crystallizing tank as claimed in claim 1, it is characterised in that feed screw nut (32) bottom is provided with paddle
Piece two (35), the stirring vane two (35) are located at below stirring vane one (33).
4. sugaring crystallizing tank as claimed in claim 3, it is characterised in that the stirring vane two (35) and tank body (1) inner chamber
Shape is identical and size fit, the stirring vane two (35) are provided with several pod apertures two (36).
5. sugaring crystallizing tank as claimed in claim 1, it is characterised in that screw mandrel (31) bottom is provided with limited block (7).
6. sugaring crystallizing tank as claimed in claim 1, it is characterised in that cleaning sprayer (9) is provided with the tank body (1),
The cleaning sprayer (9) connects with cleaning entrance (15).
7. the sugaring crystallizing tank as described in any one in claim 1 to 6, it is characterised in that the vacuum orifice (13), sugar
Slurry entrance (14), cleaning entrance (15), evacuation port (16), seed entrance (17) and vapour inlet (18) are provided with regulating valve
(6)。
8. sugaring crystallizing tank as claimed in claim 7, it is characterised in that the vapour inlet (18) is provided with air gauge, institute
Air gauge is stated to be arranged between regulating valve (6) and tank body (1).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720564609.0U CN206940919U (en) | 2017-05-20 | 2017-05-20 | One kind sugaring crystallizing tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720564609.0U CN206940919U (en) | 2017-05-20 | 2017-05-20 | One kind sugaring crystallizing tank |
Publications (1)
Publication Number | Publication Date |
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CN206940919U true CN206940919U (en) | 2018-01-30 |
Family
ID=61361268
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CN201720564609.0U Active CN206940919U (en) | 2017-05-20 | 2017-05-20 | One kind sugaring crystallizing tank |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113151612A (en) * | 2021-03-25 | 2021-07-23 | 义乌市思味特食品有限公司 | Novel single crystal rock candy crystallization process and crystallization equipment |
-
2017
- 2017-05-20 CN CN201720564609.0U patent/CN206940919U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113151612A (en) * | 2021-03-25 | 2021-07-23 | 义乌市思味特食品有限公司 | Novel single crystal rock candy crystallization process and crystallization equipment |
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