CN202342932U - Tower plate filler type rectifying tower - Google Patents
Tower plate filler type rectifying tower Download PDFInfo
- Publication number
- CN202342932U CN202342932U CN2011204837110U CN201120483711U CN202342932U CN 202342932 U CN202342932 U CN 202342932U CN 2011204837110 U CN2011204837110 U CN 2011204837110U CN 201120483711 U CN201120483711 U CN 201120483711U CN 202342932 U CN202342932 U CN 202342932U
- Authority
- CN
- China
- Prior art keywords
- tower
- rectifying
- plate
- column
- rectifying column
- 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
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model provides a tower plate filler type rectifying tower, which belongs to the technical field of chemical equipment. A support network tower plate is arranged in the rectifying tower; one side of the support network tower plate is provided with an overflow dam; the support network tower plate is provided with an active carbon filter layer; the active carbon filter layer is provided with a zeolite filler layer; the bottom of the rectifying tower is connected with a reaction kettle; a heating jacket is arranged outside the reaction kettle; the top of the rectifying tower is connected to a condenser through a guide pipe; the condenser is connected to a distillate collecting pipe; the distillate collecting pipe is communicated with a reflow pipe; and the reflow pipe is communicated to the tower top of the rectification tower. In the tower plate filler type rectifying tower, tower plate type filling is adopted, and the designs of a plate tower and a filler tower are integrated, so that the rectification coefficient can be increased in a certain degree, a gas-liquid mass transfer process is greatly enhanced, a continuous rectifying process can be realized, the product quality is improved, an operation management mode is improved, the production labor intensity is lowered, and the production safety is improved.
Description
Technical field
The utility model relates to technical field of chemical, specifically a kind of column plate material filling type rectifying column.
Background technology
Rectifying column is a kind of tower vapor-liquid contacting apparatus that carries out rectifying, and two kinds of main types of plate column and packed tower are arranged.Rectifying column work is that steam gets at the bottom of by tower, evaporates the gas phase and the decline liquid that and carries out counter current contacting, and two contact; Volatile (low boiling) component in the decline liquid constantly shifts in gas phase, and difficulty volatilization (higher boiling) component in the gas phase constantly shifts in decline liquid, and gas phase is more near cat head; Its volatile components concentration is higher; And decline liquid is healed near at the bottom of the tower, and its difficult volatile component is more enrichment then, thereby reaches the purpose that component is separated.Rectifying column structure type under the prior art is single, and mode is simple, is difficult to improve the rectifying coefficient again.
Summary of the invention
The technical assignment of the utility model is the deficiency that solves prior art, and a kind of column plate material filling type rectifying column is provided.
The technical scheme of the utility model realizes by following mode; This column plate material filling type rectifying column; Its structure is in rectifying column, to be provided with the supporting network column plate; One side of supporting network column plate is provided with downflow weir, and the supporting network column plate is provided with the active carbon filtering layer, and the active carbon filtering layer is provided with the zeolite filler layer.
The bottom of rectifying column is connected with agitated reactor, and agitated reactor is outside equipped with heating jacket.
The top of rectifying column is connected on the condenser through conduit, and condenser connects the distillate collecting pipe, is communicated with return duct on the distillate collecting pipe, and return duct is communicated to the rectifying column cat head.
The beneficial effect that the utility model is compared with prior art produced is:
This column plate material filling type rectifying column utilizes the filler of column plate type, and the design of set plate column and packed tower can improve the rectifying coefficient to a certain extent; Greatly strengthen mass-transfer progress; Can realize the continuous rectification process, improve the quality of products, the pattern of improving management and administration; Reduce productive labor intensity, increase the security of producing.
This column plate material filling type Rectification Tower Design is reasonable, simple in structure, safe and reliable, easy to use, be easy to safeguard, has good value for applications.
Description of drawings
Accompanying drawing 1 is the structural representation of the utility model.
Mark in the accompanying drawing is represented respectively:
1, rectifying column, 2, the supporting network column plate, 3, downflow weir, 4, the active carbon filtering layer, 5, the zeolite filler layer, 6, agitated reactor, 7, heating jacket, 8, conduit, 9, condenser, 10, the distillate collecting pipe, 11, return duct.
The specific embodiment
Below in conjunction with accompanying drawing the column plate material filling type rectifying column of the utility model is done following the detailed description.
Shown in accompanying drawing 1; The column plate material filling type rectifying column of the utility model, its structure are in rectifying column 1, to be provided with supporting network column plate 2, and a side of supporting network column plate 2 is provided with downflow weir 3; Supporting network column plate 2 is provided with active carbon filtering layer 4, and active carbon filtering layer 4 is provided with zeolite filler layer 5.The bottom of rectifying column 1 is connected with agitated reactor 6, and agitated reactor 6 is outside equipped with heating jacket 7.The top of rectifying column 1 is connected on the condenser 9 through conduit 8, and condenser 9 connects distillate collecting pipe 10, is communicated with return duct 11 on the distillate collecting pipe 10, and return duct 11 is communicated to rectifying column 1 cat head.
Claims (3)
1. column plate material filling type rectifying column is characterized in that in rectifying column, being provided with the supporting network column plate, and a side of supporting network column plate is provided with downflow weir, and the supporting network column plate is provided with the active carbon filtering layer, and the active carbon filtering layer is provided with the zeolite filler layer.
2. column plate material filling type rectifying column according to claim 1 is characterized in that the bottom of rectifying column is connected with agitated reactor, and agitated reactor is outside equipped with heating jacket.
3. column plate material filling type rectifying column according to claim 1 is characterized in that the top of rectifying column is connected on the condenser through conduit, and condenser connects the distillate collecting pipe, is communicated with return duct on the distillate collecting pipe, and return duct is communicated to the rectifying column cat head.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011204837110U CN202342932U (en) | 2011-11-29 | 2011-11-29 | Tower plate filler type rectifying tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011204837110U CN202342932U (en) | 2011-11-29 | 2011-11-29 | Tower plate filler type rectifying tower |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202342932U true CN202342932U (en) | 2012-07-25 |
Family
ID=46531959
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011204837110U Expired - Fee Related CN202342932U (en) | 2011-11-29 | 2011-11-29 | Tower plate filler type rectifying tower |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202342932U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103961895A (en) * | 2014-04-30 | 2014-08-06 | 江苏大恒环保电气科技股份有限公司 | Rectifying tower |
CN116328340A (en) * | 2023-05-29 | 2023-06-27 | 烟台国邦化工机械科技有限公司 | Multistage type liquid phase material rectifying equipment with high separation efficiency |
-
2011
- 2011-11-29 CN CN2011204837110U patent/CN202342932U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103961895A (en) * | 2014-04-30 | 2014-08-06 | 江苏大恒环保电气科技股份有限公司 | Rectifying tower |
CN116328340A (en) * | 2023-05-29 | 2023-06-27 | 烟台国邦化工机械科技有限公司 | Multistage type liquid phase material rectifying equipment with high separation efficiency |
CN116328340B (en) * | 2023-05-29 | 2023-07-28 | 烟台国邦化工机械科技有限公司 | Multistage type liquid phase material rectifying equipment with high separation efficiency |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202342932U (en) | Tower plate filler type rectifying tower | |
CN203513649U (en) | Diaphragm reaction kettle for producing biodiesel | |
CN103961895A (en) | Rectifying tower | |
CN204017411U (en) | Rectifying column | |
CN103566614A (en) | Dimethyl sulfate rectifying tower | |
CN202898052U (en) | Production device of <11>boron trifluoride electronic specific gas | |
CN105600762A (en) | Method and device for preparing high-purity yellow phosphorus industrially and continuously | |
CN202538405U (en) | Improved column plate filling-type rectifying column | |
CN203227315U (en) | Recovery tower | |
CN102617629A (en) | New separation process for organosilicon mixing monomer methylchlorosilane | |
CN203803141U (en) | Liquid collection and redistribution device applied to crylic acid refining process | |
CN203227314U (en) | Rectifying tower device of menthone | |
CN101913609A (en) | Method and device for removing impurities from trichlorosilane mixed gas | |
CN205275501U (en) | Epoxypropane apparatus for producing | |
CN201085940Y (en) | Rectifying tower for ethyl alcohol purification production | |
CN208814917U (en) | A kind of formaldehyde reacts the catalytic rectifying tower for producing dimethoxym ethane with methanol | |
CN204779421U (en) | Utilize device of novel catalysis rectification regular packing production methylal | |
CN203507575U (en) | Rectifying tower | |
CN104016833B (en) | The processing method of the integrated rectifying ethanol of three tower heat | |
CN203540100U (en) | Dimethyl sulfate rectifying tower | |
CN204824188U (en) | Silane rectifying column | |
CN109420355A (en) | Column plate type rectifying column | |
CN204051037U (en) | Furfural continuous rectification apparatus | |
CN101250082A (en) | Preparation method of alpha-methylnaphthalene | |
CN203244800U (en) | Beta- methyl naphthalene rectifying tower |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120725 Termination date: 20121129 |