CN201333330Y - Fixed disc type cooling crystallizer - Google Patents
Fixed disc type cooling crystallizer Download PDFInfo
- Publication number
- CN201333330Y CN201333330Y CNU2008202220148U CN200820222014U CN201333330Y CN 201333330 Y CN201333330 Y CN 201333330Y CN U2008202220148 U CNU2008202220148 U CN U2008202220148U CN 200820222014 U CN200820222014 U CN 200820222014U CN 201333330 Y CN201333330 Y CN 201333330Y
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- cooling
- fixed disc
- scraper
- disc type
- housing
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Abstract
The utility model relates to the field of cooling crystallization of various materials in biochemical industry, particularly to a fixed disc type cooling crystallizer. In the prior disc type cooling crystallizer described in patent No. 200520078685.8, cooling discs are connected with a large shaft, the rotation of the large shaft drives the rotation of the cooling discs, connecting pipelines between the discs are centralized inside the shaft, however, due to the limited diameter of the shaft, the installation of multiple connecting pipelines and the variable multistage cooling region control can not be realized. The fixed disc type cooling crystallizer has a vertical cylindrical container as a casing, and multiple cooling discs are sequentially arranged inside the casing from the top to the bottom and are fixed with the casing; and the cooling discs are connected with cooling medium pipes outside the casing respectively. The fixed disc type cooling crystallizer can realize continuous crystallization production, so as to improve production efficiency and retain stable product quality. Due to the reasonable cooling crystallization structure of the fixed disc type cooling crystallizer, the control and adjustment of crystallization process parameters are convenient, and the variable multistage temperature control can be realized. The fixed disc type cooling crystallizer can be provided with a computer to realize automatic control so as to save consumption.
Description
Technical field
The utility model relates to the crystallisation by cooling field that is used for biochemical industry industry various materials, is specifically related to fixed disc formula cooler crystallizer.
Technical background
At present, domestic equipment of crystallisation by cooling single jar of Batch Process of little volume crystallizer that adopt more, volume of equipment is little, adds intermittent operation, and the charging discharging is lost time, energy consumption height, production instability.Its occupation area of equipment is big, and production can't realize automatic control, waste resource and labour.The device structure design is unreasonable, and the cooling temperature control method is single, and can form the dead angle in crystallization process influences crystal proterties and quality.
In the existing document, the patent No. is: 200520078685.8 disc type cooler crystallizer, its cooling disk links to each other with macro-axis, the rotation of macro-axis drives the cooling disk and rotates, connecting line between disk concentrates in the axle, but because the diameter of axle is limited, can't realize the installation of many connecting lines, can't realize becoming between multistage cooling zone and control.
The utility model content
The purpose of this utility model is to provide a kind of continuous crystallisation production that realizes, enhances productivity, and keeps the fixed disc formula cooler crystallizer of stable product quality.
For achieving the above object the technical solution adopted in the utility model:
Fixed disc formula cooler crystallizer comprises, its special character is: described fixed disc formula cooler crystallizer comprises the cooling disk, axle, connecting line, dish scraper, wall scraper, end scraper, loam cake, housing, awl end socket; Described housing is the vertical barrel type container, sets gradually a plurality of cooling disks in the housing from the top down, and fixes with housing; Described cooling disk is a cavity type shell disc structure, its respectively with outer being connected of housing with the cooling medium pipe.
On in the above-mentioned housing dish scraper is set, the wall scraper, end scraper is connected with axle; Described dish scraper is parallel with the cooling disk and at a distance of certain clearance; Described wall scraper is parallel with housing and at a distance of certain clearance; Scraper of the described end is parallel with the inner surface of awl end socket and at a distance of certain clearance.
Between the above-mentioned cooling disk connecting line is set.
The utility model is with respect to prior art, and its advantage is as follows:
1, fixed disc formula cooler crystallizer of the present utility model adopts a plurality of cooling disks and the fixing frame mode of housing, can realize continuous crystallisation production, enhances productivity, and keeps stable product quality; Its rational crystallisation by cooling structure makes the convenient control of crystallization processes parameter and adjusts, and can realize becoming multistage temperature control, but equipment dispensing computer system realizes control automatically, saves to consume.
2, in the housing of the present utility model the dish scraper is set, the wall scraper, end scraper, its device interior blade design is reasonable, can thoroughly solve the influence of dead angle to the material crystallization.
Figure of description
Fig. 1 is the utility model structural representation.
Label declaration: 1-cools off disk, the 2-axle, and the 3-connecting line, 4-coils scraper, 5-wall scraper, scraper at the bottom of the 6-, the 7-loam cake, the 8-housing, 9-bores end socket.
The specific embodiment
Below in conjunction with the drawings and specific embodiments the utility model is elaborated.
Referring to Fig. 1, the structure of fixed disc formula cooler crystallizer of the present utility model comprises cooling disk 1, axle 2, connecting line 3, dish scraper 4, wall scraper 5, end scraper 6, loam cake 7, housing 8, awl end socket 9; Described housing 8 is the vertical barrel type container, sets gradually a plurality of cooling disks 1 in the housing 8 from the top down, and fixing with housing 8; Described cooling disk 1 is a cavity type shell disc structure, its respectively with outer being connected of housing 8 with cooling medium pipe 10.
The housing 8 of crystallizer is the vertical barrel type container.Housing 8 inside have a plurality of cooling disks 1 that have cavity from top to bottom, and the cavity disk diameter is to evenly being provided with a plurality of bar holes, and disk and housing 8 are fixing, and the connecting line 3 by the equipment barrel outside between disk and the disk is connected, keeps connection.The crystallizer center has runs through macro-axis up and down, and dish scraper 4, wall scraper 5 and end scraper 6 are housed on the axle of housing 8 inside.Between dish scraper 4 and cooling disk suitable processing and working clearance are arranged, with cooling disk 1 planar horizontal.Suitable processing and working clearance are arranged, with housing 8 vertical plane levels between wall scraper 5 and equipment barrel.Between the awl end socket of end scraper and device bottom suitable processing and working clearance are arranged, parallel with awl end socket inner surface.Be stamped reductor on the crystallizer outside and link to each other with axle, the reductor operation drives the rotation of axle, drive dish scraper, wall scraper and the rotation of end scraper in cylindrical shell simultaneously.
During work, be connected with cooling medium in the cooling disk 1, material is from equipment top access arrangement, after in the crystallizing range that cooling disk and cylindrical shell form, realizing heat exchange with cooling medium, under the promotion of dish scraper, enter down one deck crystallizing range from the opening part that cools off the certain angle on the disk, after crystallization is finished, enter in the awl end socket of device bottom, scrape by end scraper and shift the exit discharging onto.Wall scraper and end scraper can be prevented and treated material deposition caking on barrel or awl end socket.
This structure can make material crystallization parameters segmentation control afterwards by the crystallization processes of different material and the cooling disk of curve design varying number, also the cooling disk can be communicated with by the demand combination simultaneously, helps the crystallisation by cooling temperature controlling more.The enterprising place down of this equipment operation material can realize continued operation.
Claims (3)
1, fixed disc formula cooler crystallizer is characterized in that: described fixed disc formula cooler crystallizer comprises cooling disk (1), axle (2), connecting line (3), dish scraper (4), wall scraper (5), end scraper (6), loam cake (7), housing (8), awl end socket (9); Described housing (8) is the vertical barrel type container, sets gradually a plurality of cooling disks (1) in the housing (8) from the top down, and fixing with housing (8); Described cooling disk (1) is a cavity type shell disc structure, its respectively with outer being connected of housing (8) with cooling medium pipe (10).
2, fixed disc formula cooler crystallizer according to claim 1 is characterized in that: dish scraper (4) is set in the described housing (8), and wall scraper (5), end scraper (6) is connected with axle (2); Described dish scraper (4) is parallel with cooling disk (1) and at a distance of certain clearance; Described wall scraper (5) is parallel with housing (8) and at a distance of certain clearance; Scraper of the described end (6) is parallel with the inner surface of awl end socket (9) and at a distance of certain clearance.
3, fixed disc formula cooler crystallizer according to claim 1 and 2 is characterized in that: connecting line (3) is set between the described cooling disk (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202220148U CN201333330Y (en) | 2008-10-24 | 2008-10-24 | Fixed disc type cooling crystallizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202220148U CN201333330Y (en) | 2008-10-24 | 2008-10-24 | Fixed disc type cooling crystallizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201333330Y true CN201333330Y (en) | 2009-10-28 |
Family
ID=41284972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008202220148U Expired - Lifetime CN201333330Y (en) | 2008-10-24 | 2008-10-24 | Fixed disc type cooling crystallizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201333330Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107970639A (en) * | 2017-12-31 | 2018-05-01 | 山东北方中意新材料有限公司 | A kind of multistage subsection stacker module quasi-continuous crystallizer |
| CN110772829A (en) * | 2019-10-25 | 2020-02-11 | 安徽金轩科技有限公司 | Cooling crystallization equipment for purifying furanone |
-
2008
- 2008-10-24 CN CNU2008202220148U patent/CN201333330Y/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107970639A (en) * | 2017-12-31 | 2018-05-01 | 山东北方中意新材料有限公司 | A kind of multistage subsection stacker module quasi-continuous crystallizer |
| CN107970639B (en) * | 2017-12-31 | 2023-07-25 | 腾中新材料科技(苏州)有限公司 | Multistage sectional tower type simulation continuous crystallizer |
| CN110772829A (en) * | 2019-10-25 | 2020-02-11 | 安徽金轩科技有限公司 | Cooling crystallization equipment for purifying furanone |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20091028 |
|
| CX01 | Expiry of patent term |