CN204767571U - Crystallizer is used in sugaring - Google Patents
Crystallizer is used in sugaring Download PDFInfo
- Publication number
- CN204767571U CN204767571U CN201520380668.3U CN201520380668U CN204767571U CN 204767571 U CN204767571 U CN 204767571U CN 201520380668 U CN201520380668 U CN 201520380668U CN 204767571 U CN204767571 U CN 204767571U
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- agitator
- crystallizer
- sugaring
- tank
- ball valve
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Abstract
The utility model relates to a crystallizer is used in sugaring, the upper cover in jar body upper end is installed including a jar body to the crystallizer, is provided with matter entrance, drug entry, manhole, sight glass lamp on the upper cover, and the lower part sets up temperature measuring device in jar body, and a jar internal portion is provided with agitator and agitator down, and the both sides of going up the agitator and the bottom of agitator down are equipped with the wing respectively, and a jar body bottom is provided with the discharge gate, and the discharge gate lower extreme has a fast -assembling ball valve through last clamp connection, and the pipe connection is expected through clamp down with arranging to the fast -assembling ball valve. Crystallizer is used in sugaring has adopted the fast -assembling ball valve as crystallizer tank bottoms valve, and easy dismounting makes the internal material of crystallizer jar because uncertain factor when causing the tank bottoms scale deposit to block up, and the crystal feed liquid is emitted in scale removal fast, and the assurance subsequent handling goes on smoothly, can the minimize scale deposit or time of extension scale deposit through setting up the wing, in addition through setting up cooling device, can make the crystallizer in the temperature accord with the crystallization requirement, guarantee product quality.
Description
Technical field
The utility model relates to crystallizer technical field, is specifically related to a kind of sugaring crystallizing tank.
Background technology
D-ribose is a kind of epochmaking aldopentose, is the important composition composition of inhereditary material nucleic acid in organism, is also the important intermediate metabolites of organism composite part amino acid, base etc., has important physiological function.D-ribose is as the natural components be present in all cells, substantial connection is had with the formation of adenylate and the regeneration of ATP, be one of the most basic energy source of vital metabolic, play a crucial role in heart and muscle metabolism, the recovery of local organization ischemic, anoxic can be promoted.Current D-ribose is mainly used to synthetic vitamin B2 and flavour nucleotide etc., and the investigation and application simultaneously as the bulk drug synthesizing antiviral, cancer therapy drug is also more and more extensive.In a word, D-ribose has boundless application prospect.
No matter industrial production D-ribose is use enzymatic hydrolysis yeast rna, or chemical synthesis, and the extraction and separation process of D-ribose determines the yield of final products, purity, quality, production cost and range of application in the future.Operate relative to other chemical separating, this separation method of crystallization has many excellent features: it is less etc. that it can isolate highly purified product, safer, the consuming little energy of operation, environmental pollution.In recent years, crystallization operation all achieves very much progress in theory or in commercial Application, obtains larger economic benefit.Therefore, generally adopt crystallization means to obtain polishing product in multiple industries such as medicine, food.But crystallization is a complicated operating process, be heterogeneous, multi-component heat and mass transfer process, complicated mechanism not yet reaches the level carrying out complete Theory calculating at present.
Crystallizing tank is as equipment vital in D-ribose Crystallizing process, and the design of its crystalline quality to D-ribose, crystallization rate and whole flow process all can have a huge impact.Therefore, reasonably improve crystallizing tank, ensure that in crystallization tank body, D-ribose solution can carry out crystallization, to improve crystalline rate under most suitable condition.D-ribose is in crystallization process, once various factors control is improper, solution degree of supersaturation will be caused too large so that at crystallization tank skin bear building-up dirt.After crystallization tank skin bear building-up dirt, crystal feed liquid just cannot discharge crystallizing tank, so that the operation of back cannot be carried out.And crystallizing tank generally uses exhibition baiting valve as bottom valve at present, upper exhibition baiting valve generally connects crystallization pot bottom by welding manner, and dismounting is very inconvenient.
Utility model content
The purpose of this utility model is to overcome defect of the prior art, designs a kind of bottom valve easy accessibility, the sugaring crystallizing tank that after crystallization tank skin bear building-up dirt, crystal feed liquid also can be released smoothly.
For achieving the above object, the technical scheme that the utility model adopts is:
A kind of sugaring crystallizing tank, it is characterized in that, described crystallizing tank comprises tank body, be arranged on the upper cover of tank body upper end, upper cover is provided with material inlet, spice entrance, manhole, visor lamp, tank body middle and lower part arranges temperature measuring equipment, tank interior is provided with agitator and lower agitator, the both sides of upper agitator and the bottom of lower agitator are respectively equipped with wing, tank base is provided with discharging opening, discharging opening lower end is connected with Packaged ball valve by front band, and Packaged ball valve is connected with drainage line by lower catch hoop.
Wherein preferred technical scheme is that, at described tank body arranged outside cooling jacket, cooling water inlet is established in the bottom of cooling jacket, and the top of cooling jacket is provided with coolant outlet.
Preferred technical scheme also has, and described wing is connected with the both sides of upper agitator and the bottom of lower agitator respectively by the hinge with torsion spring.
Preferred technical scheme also has, and described upper cover is also provided with steam vent, and steam vent is connected with vavuum pump by blast pipe.
Advantage of the present utility model and beneficial effect are: described sugaring crystallizing tank have employed Packaged ball valve as crystallizing tank bottom valve, easy accessibility, make the material in crystallizing tank tank body due to uncertain factor cause fouling and clogging at the bottom of tank time, can quick descaling, crystal feed liquid is released, ensures that subsequent handling is carried out smoothly; By arranging the time that wing can reduce fouling or extend fouling as far as possible, additionally by arranging cooling device, temperature in crystallizing tank can be made to meet crystallization requirement, ensureing product quality.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model sugaring crystallizing tank.
In figure: 1, tank body; 2, cooling jacket; 3, coolant outlet; 4, material inlet; 5, spice entrance; 6, upper cover; 7, visor lamp; 8, manhole; 9, upper agitator; 10, wing; 11, temperature measuring equipment; 12, lower agitator; 13, wing; 14, cooling water inlet; 15, Packaged ball valve; 16, lower catch hoop; 17, drainage line; 18, front band; 19, discharging opening.
Detailed description of the invention
Below in conjunction with drawings and Examples, detailed description of the invention of the present utility model is further described.Following examples only for clearly the technical solution of the utility model being described, and can not limit protection domain of the present utility model with this.
As shown in Figure 1: the utility model is a kind of sugaring crystallizing tank, described crystallizing tank comprises tank body 1, be arranged on the upper cover 6 of tank body 1 upper end, upper cover 6 is provided with material inlet 4, spice entrance 5, manhole 8, visor lamp 7, tank body 1 middle and lower part arranges temperature measuring equipment 11, tank body 1 inside is provided with agitator 9 and lower agitator 12, the both sides of upper agitator 9 and the bottom of lower agitator are respectively equipped with wing 10, 13, discharging opening 19 is provided with bottom tank body 1, discharging opening 19 lower end is connected with Packaged ball valve 15 by front band 18, Packaged ball valve 15 is connected with drainage line 17 by lower catch hoop 16.
The preferred embodiment of the utility model is, at described tank body 1 arranged outside cooling jacket 2, cooling water inlet 14 is established in the bottom of cooling jacket 2, and the top of cooling jacket 2 is provided with coolant outlet 3.
The preferred embodiment of the utility model also has, and described wing 9,12 is connected with the both sides of upper agitator 9 and the bottom of lower agitator 11 respectively by the hinge with torsion spring.
The preferred technical scheme of the utility model also has, and described upper cover 6 is also provided with steam vent, and steam vent is connected with vavuum pump by blast pipe.
The above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art; under the prerequisite not departing from the utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (4)
1. a sugaring crystallizing tank, it is characterized in that, described crystallizing tank comprises tank body, be arranged on the upper cover of tank body upper end, upper cover is provided with material inlet, spice entrance, manhole, visor lamp, tank body middle and lower part arranges temperature measuring equipment, tank interior is provided with agitator and lower agitator, the both sides of upper agitator and the bottom of lower agitator are respectively equipped with wing, tank base is provided with discharging opening, discharging opening lower end is connected with Packaged ball valve by front band, and Packaged ball valve is connected with drainage line by lower catch hoop.
2. sugaring crystallizing tank as claimed in claim 1, it is characterized in that, at described tank body arranged outside cooling jacket, cooling water inlet is established in the bottom of cooling jacket, and the top of cooling jacket is provided with coolant outlet.
3. sugaring crystallizing tank as claimed in claim 1, is characterized in that, described wing is connected with the both sides of upper agitator and the bottom of lower agitator respectively by the hinge with torsion spring.
4. sugaring crystallizing tank as claimed in claim 1, it is characterized in that, described upper cover (6) is also provided with steam vent, and steam vent is connected with vavuum pump by blast pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520380668.3U CN204767571U (en) | 2015-06-04 | 2015-06-04 | Crystallizer is used in sugaring |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520380668.3U CN204767571U (en) | 2015-06-04 | 2015-06-04 | Crystallizer is used in sugaring |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204767571U true CN204767571U (en) | 2015-11-18 |
Family
ID=54507703
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520380668.3U Expired - Fee Related CN204767571U (en) | 2015-06-04 | 2015-06-04 | Crystallizer is used in sugaring |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204767571U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105641966A (en) * | 2016-01-07 | 2016-06-08 | 南昌理工学院 | Crystallization tank for isepamicin sulfate |
| CN105696441A (en) * | 2016-02-01 | 2016-06-22 | 无锡华通沥青新技术发展有限公司 | Modified asphalt production stirrer |
| CN107758766A (en) * | 2017-11-22 | 2018-03-06 | 遵义汇恒环保科技有限公司 | Recycling can for bauxite sewage |
| CN115350498A (en) * | 2022-07-20 | 2022-11-18 | 徐姣姣 | Amino acid recycling system |
-
2015
- 2015-06-04 CN CN201520380668.3U patent/CN204767571U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105641966A (en) * | 2016-01-07 | 2016-06-08 | 南昌理工学院 | Crystallization tank for isepamicin sulfate |
| CN105641966B (en) * | 2016-01-07 | 2017-07-28 | 南昌理工学院 | A kind of Isepamicin sulfate crystallizing tank |
| CN105696441A (en) * | 2016-02-01 | 2016-06-22 | 无锡华通沥青新技术发展有限公司 | Modified asphalt production stirrer |
| CN107758766A (en) * | 2017-11-22 | 2018-03-06 | 遵义汇恒环保科技有限公司 | Recycling can for bauxite sewage |
| CN115350498A (en) * | 2022-07-20 | 2022-11-18 | 徐姣姣 | Amino acid recycling system |
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Legal Events
| 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 |
Granted publication date: 20151118 Termination date: 20160604 |