CN205528517U - High -purity triphenylchloromethane apparatus for producing - Google Patents
High -purity triphenylchloromethane apparatus for producing Download PDFInfo
- Publication number
- CN205528517U CN205528517U CN201620093467.XU CN201620093467U CN205528517U CN 205528517 U CN205528517 U CN 205528517U CN 201620093467 U CN201620093467 U CN 201620093467U CN 205528517 U CN205528517 U CN 205528517U
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- CN
- China
- Prior art keywords
- heat exchanger
- connects
- vortex tube
- tube refrigerator
- triphenylchloromethane
- 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.)
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses a high -purity triphenylchloromethane apparatus for producing, including raw materials import and sprayer, raw materials import links to each other with the sprayer, raw materials import is connected with heat exchanger II, heat exchanger II links to each other with the sprayer, heat exchanger II is connected with heat exchanger I, heat exchanger II is connected with vortex tube refrigerator II, vortex tube refrigerator II is connected with vortex tube refrigerator I, vortex tube refrigerator I is connected with the chemical reaction cauldron, the chemical reaction cauldron is connected in heat exchanger I and heat exchanger between II, heat exchanger I is connected with choke valve II, choke valve II is connected with heat exchanger III and heat exchanger IV respectively, heat exchanger III links to each other with heat exchanger IV, heat exchanger III is connected with the compressor, the compressor is connected with the export, heat exchanger IV is connected with choke valve I, choke valve I is connected with the separator, the utility model discloses a plurality of heat exchangers and vortex tube refrigerator act on repeatedly, and rethread compressor and separator can lift the production concentration of high energy triphenylchloromethane in very big chengdu.
Description
Technical field
The utility model relates to chemical production facilities field, is specifically related to a kind of high-purity triphenyl chloromethane
Alkane process units.
Background technology
The medicine intermediate that triphenylchloromethane is important.Triphenylchloromethane is normal in field of medicine and chemical technology
One of basic organic, during organic chemical industry with pharmaceutical synthesis, can serve as nucleosides,
In the compound such as monose or polysaccharide with primary hydroxyl selective protection base and Peptide systhesis in
Basic chemical reagent.
To produce highly purified triphenylchloromethane at present more complicated, and, cost is the most relatively
High, it is difficult to realize.
Utility model content
For problem above, the utility model provides a kind of high-purity triphenylchloromethane process units,
By some heat exchangers and vortex tube refrigerator repeated action, then by compressor and separator, can be
Improve the production concentration of energy triphenylchloromethane on the biggest Chengdu, effectively solve asking in technical background
Topic.
To achieve these goals, the technical solution adopted in the utility model is as follows: a kind of high-purity three
Phenylchloride methane production device, including material inlet and injector, described material inlet and injector phase
Even, described material inlet connects has heat exchanger II, described heat exchanger II to be connected with injector, described in change
Hot device II connects heat exchanger I, and described heat exchanger II connects vortex tube refrigerator II, described eddy current
Control cooler II is connected with injector, heat exchanger I, and described vortex tube refrigerator II connects vortex tube
Refrigerator I, described vortex tube refrigerator I connects chemical reaction kettle, and described chemical reaction kettle connects
Between heat exchanger I and heat exchanger II, described vortex tube refrigerator I is also attached in heat exchanger I,
Described heat exchanger I connects has choke valve II, described choke valve II to be connected to heat exchanger III and heat exchange
Device IV, described heat exchanger III is connected with heat exchanger IV, and described heat exchanger III connects compressor, described
Compressor connects outlet, and described heat exchanger IV connects choke valve I, and described choke valve I connects to be had
Separator.
Further, described injector is connected with outlet.
Further, described separator is connected with heat exchanger IV.
The beneficial effects of the utility model:
The utility model passes through some heat exchangers and vortex tube refrigerator repeated action, then passes through compressor
And separator, the production concentration of energy triphenylchloromethane can be improved on the biggest Chengdu.
Accompanying drawing explanation
Accompanying drawing is used for providing being further appreciated by of the present utility model, and constitutes a part for specification,
It is used for explaining the utility model together with embodiment of the present utility model, is not intended that the utility model
Restriction.
Fig. 1 is the utility model overall structure schematic diagram.
Figure is numbered: 1-material inlet；2-injector；3-heat exchanger II；4-heat exchanger I；5-
Vortex tube refrigerator II；6-vortex tube refrigerator I；7-chemical reaction kettle；8-choke valve II；9-changes
Hot device III；10-heat exchanger IV；11-compressor；12-exports；13-choke valve I；14-separator.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with
Drawings and Examples, are further elaborated to the utility model.Should be appreciated that this place is retouched
The specific embodiment stated, only in order to explain the utility model, is not used to limit the utility model.
Embodiment:
As it is shown in figure 1, a kind of high-purity triphenylchloromethane process units, including material inlet 1 He
Injector 2, described material inlet 1 is connected with injector 2, and described material inlet 1 connects heat exchanger
II 3, described heat exchanger II 3 is connected with injector 2, and described heat exchanger II 3 connects heat exchanger I 4,
Described heat exchanger II 3 connects a vortex tube refrigerator II 5, described vortex tube refrigerator II 5 and injector 2,
Heat exchanger I 4 is connected, and described vortex tube refrigerator II 5 connects vortex tube refrigerator I 6, described whirlpool
Flow tube refrigerator I 6 connects has chemical reaction kettle 7, described chemical reaction kettle 7 to be connected to heat exchanger I 4
With between heat exchanger II 3, described vortex tube refrigerator I 6 is also attached in heat exchanger I 4, described in change
Hot device I 4 connects has choke valve II 8, described choke valve II 8 to be connected to heat exchanger III 9 and heat exchanger
IV 10, described heat exchanger III 9 is connected with heat exchanger IV 10, and described heat exchanger III 9 connects compressor
11, described compressor 11 connects outlet 12, and described heat exchanger IV 10 connects choke valve I 13,
Described choke valve I 13 connects separator 14.
On above-described embodiment preferably, described injector 2 is connected with outlet 12.
On above-described embodiment preferably, described separator 14 is connected with heat exchanger IV 10
Based on above-mentioned, the utility model passes through some heat exchangers and vortex tube refrigerator repeated action, then
By compressor and separator, the production concentration of energy triphenylchloromethane can be improved on the biggest Chengdu.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, not
For limiting the utility model, although the utility model having been carried out specifically with reference to previous embodiment
Bright, for a person skilled in the art, it still can be to the skill described in foregoing embodiments
Art scheme is modified, or wherein portion of techniques feature is carried out equivalent.All new in this practicality
Within the spirit of type and principle, any modification, equivalent substitution and improvement etc. made, should be included in
Within protection domain of the present utility model.
Claims (3)
1. a high-purity triphenylchloromethane process units, it is characterised in that: include material inlet and
Injector, described material inlet is connected with injector, and described material inlet connects heat exchanger II, institute
Stating heat exchanger II to be connected with injector, described heat exchanger II connects heat exchanger I, described heat exchanger II
Connecting has vortex tube refrigerator II, described vortex tube refrigerator II to be connected with injector, heat exchanger I,
Described vortex tube refrigerator II connects vortex tube refrigerator I, and described vortex tube refrigerator I connects to be had
Chemical reaction kettle, described chemical reaction kettle is connected between heat exchanger I and heat exchanger II, described eddy current
Control cooler I is also attached in heat exchanger I, and described heat exchanger I connects choke valve II, described joint
Stream valve II is connected to heat exchanger III and heat exchanger IV, and described heat exchanger III is connected with heat exchanger IV,
Described heat exchanger III connects compressor, and described compressor connects has outlet, described heat exchanger IV to connect
Having choke valve I, described choke valve I connects separator.
A kind of high-purity triphenylchloromethane process units the most according to claim 1, its feature
It is: described injector is connected with outlet.
A kind of high-purity triphenylchloromethane process units the most according to claim 1, its feature
It is: described separator is connected with heat exchanger IV.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620093467.XU CN205528517U (en) | 2016-01-29 | 2016-01-29 | High -purity triphenylchloromethane apparatus for producing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620093467.XU CN205528517U (en) | 2016-01-29 | 2016-01-29 | High -purity triphenylchloromethane apparatus for producing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205528517U true CN205528517U (en) | 2016-08-31 |
Family
ID=56774679
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620093467.XU Expired - Fee Related CN205528517U (en) | 2016-01-29 | 2016-01-29 | High -purity triphenylchloromethane apparatus for producing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205528517U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115160105A (en) * | 2022-07-08 | 2022-10-11 | 苏州金宏气体股份有限公司 | Method and device for purifying hexafluoro-1,3-butadiene by using eddy current technology |
-
2016
- 2016-01-29 CN CN201620093467.XU patent/CN205528517U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115160105A (en) * | 2022-07-08 | 2022-10-11 | 苏州金宏气体股份有限公司 | Method and device for purifying hexafluoro-1,3-butadiene by using eddy current technology |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20190129 |