CN202594776U - Distilling device for bromine production - Google Patents
Distilling device for bromine production Download PDFInfo
- Publication number
- CN202594776U CN202594776U CN 201220286891 CN201220286891U CN202594776U CN 202594776 U CN202594776 U CN 202594776U CN 201220286891 CN201220286891 CN 201220286891 CN 201220286891 U CN201220286891 U CN 201220286891U CN 202594776 U CN202594776 U CN 202594776U
- Authority
- CN
- China
- Prior art keywords
- tower
- bromine
- distillation
- utility
- model
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a distilling device for bromine production, which comprises a distilling tower, wherein the distilling tower comprises a steel tower body; a teflon layer is arranged on the inner wall of tower body; and a condenser is connected with the top part of the tower body, and includes a shell and tube condenser. The distilling device simplifies the structure, is convenient to operate, reduces the labor intensity and the misoperation of workers, saves the steam, and improves the quality of finished product bromine.
Description
Technical field
The utility model relates to the bromine production technical field, is specifically related to the water distilling apparatus that uses in a kind of bromine production process.
Background technology
Bromine is a kind of weight of material of chemical industry; Main being used as produced bromide, and is used as general analysis reagent, oxygenant, ethene and the absorption agent of heavy hydrocarbon polymer and the bromizating agent of organic synthesis in departments such as medicine, agricultural chemicals, dyestuff, spices, photographic material, fire-fighting medium, ore dressing, metallurgy, tanning, water purification.
In the bromine production process, distillation is the process step of a key, and the distillatory effect directly affects the quality product of bromine.At present, the distillation plant of bromine adopts the glass distillation tower, and this has just determined that distillation tower itself can not the too high distillation amount of burden.Therefore, generally be equipped with four groups of glass distillation towers and distill bromine, 4 meters of tower heights, 230 millimeters of diameters, each assembly is equipped with 2 spiral condensers, complex structure, not easy to operate, labour intensity is big, and the bromine quality is unstable, has potential safety hazard.
The utility model content
The utility model technical problem to be solved provides a kind of bromine production and uses water distilling apparatus, and its distillation efficiency is high, the bromine constant product quality of production, thus eliminate defective in the above-mentioned background technology.
For solving the problems of the technologies described above, the technical scheme of the utility model is:
Water distilling apparatus is used in a kind of bromine production, comprises distillation tower, it is characterized in that, said distillation tower comprises steel-made tower, and said tower body inwall is provided with polytetrafluoroethylene floor, and the top of said tower body is connected with condensing surface.
As a kind of improvement, said condensing surface comprises shell-and tube condenser.
In actual production, the steel-made tower height is 8.5m, diameter 0.6m, and its distillation work amount is enough to replace 4 meters of four groups of tower heights, the glass distillation tower that diameter is 230 millimeters; Under the prerequisite that does not influence distillation efficiency, simplify the structure, effectively avoided workman's mishandle, stablized the quality of bromine product.
Owing to adopted technique scheme, the beneficial effect of the utility model is:
The water distilling apparatus that the utility model provides is applicable to the distil process that bromine is produced, and adopts steel-made tower; The inner liner polytetrafluoroethylene layer can be born bigger distillation amount, than the conventional glass distillation tower; Structure is able to simplify, and is convenient to operation, has reduced labour intensity; Reduced workman's mishandle, saved steam, finished product bromine steady quality.
Water distilling apparatus is used in the bromine production that the utility model provides, and condensing surface comprises shell-and tube condenser, and the shell-and tube condenser evaporation efficiency is high, and can adapt to the distillation rate of this water distilling apparatus.
Description of drawings
Accompanying drawing is the utility model structural representation;
Among the figure: 1. tower body, 2. polytetrafluoroethylene floor, 3. condensing surface.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach purpose and be easy to understand understanding with effect, below in conjunction with concrete diagram, further set forth the utility model.
Shown in accompanying drawing, water distilling apparatus is used in a kind of bromine production, comprises distillation tower; It is characterized in that said distillation tower comprises steel-made tower 1, said tower body 1 inwall is provided with polytetrafluoroethylene floor 2; The top of said tower body 1 is connected with condensing surface 3, and said condensing surface 3 adopts shell-and tube condenser.
Present embodiment adopts steel-made tower 1, and inner liner polytetrafluoroethylene layer 2 can be born bigger distillation amount, than the conventional glass distillation tower; Structure is able to simplify, and is convenient to operation, has reduced labour intensity; Reduced workman's mishandle, saved steam, finished product bromine steady quality; Simultaneously, condensing surface 3 adopts shell-and tube condenser, and the shell-and tube condenser evaporation efficiency is high, and can adapt to the distillation rate of this water distilling apparatus.
The utility model is not limited to above-mentioned embodiment, and all are based on the technical conceive of the utility model, and the structural improvement of having done all falls among the protection domain of the utility model.
Claims (2)
1. water distilling apparatus is used in a bromine production, comprises distillation tower, and it is characterized in that: said distillation tower comprises steel-made tower, and said tower body inwall is provided with polytetrafluoroethylene floor, and the top of said tower body is connected with condensing surface.
2. water distilling apparatus is used in a kind of bromine production as claimed in claim 1, and it is characterized in that: said condensing surface comprises shell-and tube condenser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220286891 CN202594776U (en) | 2012-06-18 | 2012-06-18 | Distilling device for bromine production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220286891 CN202594776U (en) | 2012-06-18 | 2012-06-18 | Distilling device for bromine production |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202594776U true CN202594776U (en) | 2012-12-12 |
Family
ID=47312334
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201220286891 Expired - Fee Related CN202594776U (en) | 2012-06-18 | 2012-06-18 | Distilling device for bromine production |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202594776U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108100997A (en) * | 2017-12-28 | 2018-06-01 | 天津长芦汉沽盐场有限责任公司 | Bromine produces special destilling tower |
-
2012
- 2012-06-18 CN CN 201220286891 patent/CN202594776U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108100997A (en) * | 2017-12-28 | 2018-06-01 | 天津长芦汉沽盐场有限责任公司 | Bromine produces special destilling tower |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104595877B (en) | Multi-step pressure reduction reclaims the device and its recovery method of hot waste water waste heat | |
CN204932911U (en) | A kind of continuous rectification apparatus for maleic anhydride production | |
CN203355329U (en) | Coarse vinyl chloride distillation system | |
CN202594776U (en) | Distilling device for bromine production | |
CN201701787U (en) | Demister | |
CN103007673A (en) | Comprehensive recovery treater and method for pharmaceutical benzoic acid process tail gas | |
CN107759440A (en) | A kind of method that fluorine by Fluorine containing olefine double bond is replaced as hydrogen | |
CN201775971U (en) | Rectification system of thionyl chloride | |
CN202968431U (en) | Composite tower for separating intermediate products dimethyl oxalate and methanol in industrial production of ethylene glycol | |
CN108083978A (en) | The preparation process and device of cyclohexanedimethanol | |
CN204307504U (en) | Sulfolane distillation tail gas treatment device | |
CN103772084A (en) | Ester-exchange reaction device | |
CN203440262U (en) | Device for producing trans-1, 2-dichloroethylene with acetylene by adopting catalytic chlorination method | |
CN106380403B (en) | The method for efficiently separating dimethyl oxalate and dimethyl carbonate | |
CN203803141U (en) | Liquid collection and redistribution device applied to crylic acid refining process | |
CN102863322A (en) | Method for synthesizing p-methoxylbenzaldehyde | |
CN102849770A (en) | Method for synthesizing anhydrous aluminum chloride by recycling aluminum chloride hexahydrate | |
CN205759789U (en) | The novel bromine rectifying column that a kind of filler and column plate are combined | |
CN106146264B (en) | The synthetic method of allyl glyceroether | |
CN106278830A (en) | The synthetic method of diallyl glycerin ether | |
CN214551287U (en) | Tube plate structure of reboiler of reduced pressure refining tower | |
CN103013815A (en) | Modified glutamic acid fermentation tank | |
CN103408413A (en) | Method for preparing deuterated chloroform by using hexachloroacetone as intermediate | |
CN202989119U (en) | Energy-saving consumption-reducing glutamic acid fermentation tank | |
CN204485872U (en) | A kind of distillation reactor |
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: 20121212 Termination date: 20190618 |