CN207685175U - Epoxychloropropane saponification column - Google Patents
Epoxychloropropane saponification column Download PDFInfo
- Publication number
- CN207685175U CN207685175U CN201721825114.5U CN201721825114U CN207685175U CN 207685175 U CN207685175 U CN 207685175U CN 201721825114 U CN201721825114 U CN 201721825114U CN 207685175 U CN207685175 U CN 207685175U
- Authority
- CN
- China
- Prior art keywords
- saponification
- column plate
- column
- epoxychloropropane
- pipeline
- 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.)
- Active
Links
Landscapes
- Epoxy Compounds (AREA)
- Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
Abstract
The utility model belongs to chemical plant installations technical field, and in particular to a kind of epoxychloropropane saponification column.The epoxychloropropane saponification column, including the column plate inside saponification tower body and saponification column body, it further include saponification liquid horizontal feed pipeline, saponification liquid feeding vertical pipeline is connected after saponification liquid horizontal feed pipeline, upper layer column plate is not provided with inside saponification column body, column plate be followed successively by from top to bottom the second column plate, third column plate, the 4th column plate ..., bottom column plate, the second column plate is set below saponification liquid feeding vertical pipeline.The utility model shortens flowing time of the saponification liquid in pipeline, reduces fouled condition, while also improving the scale formation of column plate, reduces frequent pickling processes, extends the production cycle, greatly reduces production cost.
Description
Technical field
The invention belongs to chemical plant installations technical fields, and in particular to a kind of epoxychloropropane saponification column.
Background technology
At present in the production technology of epoxychloropropane, dichlorohydrin and milk of lime enter saponification column and carry out saponification,
The thick epoxychloropropane generated carries out condensation extraction by evaporator overhead condenser collection, and saponification waste-water squeezes into sudden strain of a muscle by saponification column bottoms pump
Steaming pot carries out recuperation of heat processing.Also there is side reaction during saponification, the milk of lime not reacted completely can absorb saponification
Carbon dioxide in liquid generates calcium carbonate.
Polylith column plate inside epoxychloropropane saponification column in the prior art, including saponification tower body and saponification column body, point
Not Wei upper layer column plate, the second column plate, third column plate, the 4th column plate ..., bottom column plate, further include saponification liquid level into
Expects pipe line, connects saponification liquid feeding vertical pipeline after saponification liquid horizontal feed pipeline, saponification liquid vertically into
Expects pipe line bottom nozzle connects saponification liquid horizontal flow pipeline.Since the direction of saponification liquid horizontal flow pipeline is horizontal
Direction, mobility is poor, and positioned at the top of upper layer column plate, closer from upper layer column plate, distance is less than 20cm, leads to calcium carbonate very
It is readily adsorbed on saponification liquid horizontal flow pipeline.In addition, calcium carbonate is also easier to be adsorbed on column plate.
With the passage of production time, the phenomenon that saponification liquid horizontal flow pipeline and column plate fouling, is increasingly severe,
It is excessive so as to cause saponification column pressure difference, affect the stable operation of saponification column.It needs to carry out pickling, Cai Nengbao to column plate, pipeline
Card production is smoothed out.And pickling will cause to stop, and not only delay production, and a large amount of manpower and materials is caused to be lost, and be produced into
This also rises therewith.
To sum up, it is badly in need of researching and developing a kind of reduction fouled condition, the epoxychloropropane saponification column to extend manufacture cycle at present.
Utility model content
The purpose of this utility model is to provide a kind of flowing time shortening saponification liquid in pipeline, reduces fouling shape
Condition, the epoxychloropropane saponification column to extend manufacture cycle.
Column plate inside epoxychloropropane saponification column described in the utility model, including saponification tower body and saponification column body, also
Including saponification liquid horizontal feed pipeline, saponification liquid vertical feed pipe is connected after saponification liquid horizontal feed pipeline
Line is not provided with upper layer column plate inside saponification column body, and column plate is followed successively by the second column plate, third column plate, the 4th tower from top to bottom
Plate ..., bottom column plate, the second column plate is set below saponification liquid feeding vertical pipeline.
Wherein:
The distance between the saponification liquid feeding vertical pipeline bottom nozzle and the second column plate are 30-60cm.
The saponification liquid horizontal feed pipeline connects static mixer.
The static mixer is connected with dichlorohydrin feeding line, milk of lime feeding line respectively.
The number of the column plate is 15-25 blocks.
The column plate outer surface sprays anticorrosive PTFE layer.It is preferred that after the column plate outer surface first connects sandblasting layer,
Anticorrosive PTFE layer is sprayed again.
Steam pipe line is set below the bottom column plate.
The beneficial effects of the utility model are as follows:
Saponification liquid horizontal flow pipeline in the prior art direction is horizontally oriented, and mobility is poor, increases soap
Change flowing time of the reaction solution in pipeline, leads to easy fouling.So the utility model is by saponification liquid horizontal flow pipeline
Remove, only retains saponification liquid horizontal feed pipeline and saponification liquid feeding vertical pipeline, avoid saponification liquid water
The phenomenon that flat bypass line easy fouling, reduces flowing time of the saponification liquid in pipeline, avoid in the short time, saponification
Milk of lime fouling in pipeline in reaction solution, the pipeline blockage caused by fouling also greatly reduce.
In addition, the second column plate is arranged in saponification liquid feeding vertical pipeline directly below, upper layer column plate is eliminated so that soap
The distribution for changing reaction solution is more uniform, while increasing activity space when operating personnel's maintenance.
Meanwhile the utility model also provides the column plate for preventing fouling.Because polytetrafluoroethylene (PTFE) friction coefficient is small, has and do not glue
Property, and polytetrafluoroethylene (PTFE) has the characteristic of acid-alkali-corrosive-resisting and scale inhibition, and anticorrosive PTFE layer is sprayed in column plate outer surface, greatly
Reduce scale formation greatly.And be fixedly connected with anticorrosive PTFE layer by sandblasting layer in column plate outer surface, make poly- four
Vinyl fluoride erosion resistant coating is combined more secured with column plate.In order to keep original production efficiency, after improvement the percent opening of column plate with change
Percent opening into preceding column plate is identical.Therefore, the fouled condition of column plate is substantially improved by spraying anticorrosive PTFE layer.
To sum up, the utility model shortens flowing time of the saponification liquid in pipeline, reduces fouled condition, simultaneously
The scale formation for also improving column plate reduces frequent pickling processes, extends the production cycle, greatly reduces and be produced into
This.
Description of the drawings
Fig. 1 is the utility model structure diagram;
Fig. 2 is that the utility model improves pre-structure schematic diagram;
Fig. 3 is the second tower plate structure schematic diagram;
In figure:1, static mixer;2, saponification liquid horizontal feed pipeline;3, saponification liquid feeding vertical pipeline;
4, the second column plate;5, saponification tower body;6, steam pipe line;7, bottom column plate;8, milk of lime feeding line;9, dichlorohydrin feed pipe
Line;10, saponification liquid horizontal flow pipeline;11, upper layer column plate;12, sandblasting layer;13, anticorrosive PTFE layer.
Specific implementation mode
The utility model is described further with reference to embodiments.
Embodiment 1
As shown in Figure 1, Figure 3, epoxychloropropane saponification column described in the utility model, including saponification tower body 5 and saponification column
20 blocks of column plates inside body 5 further include saponification liquid horizontal feed pipeline 2, connect after saponification liquid horizontal feed pipeline 2
Saponification liquid feeding vertical pipeline 3 is connect, upper layer column plate 11 is not provided with inside saponification tower body 5, column plate is followed successively by from top to bottom
Two column plates 4, third column plate, the 4th column plate, the 5th column plate, the 6th column plate, the 7th column plate, the 8th column plate, the 9th column plate, the tenth tower
Plate, the 11st column plate, the 12nd column plate, the 13rd column plate, the 14th column plate, the 15th column plate, the 16th column plate, the 17th tower
Plate, the 18th column plate, the 19th column plate, the 20th column plate, bottom column plate 7, the 3 lower section setting of saponification liquid feeding vertical pipeline
Second column plate 4.
The distance between 3 bottom nozzle of saponification liquid feeding vertical pipeline and the second column plate 4 are 40cm.Saponification liquid water
Flat feeding line 2 connects static mixer 1.Static mixer 1 also respectively with dichlorohydrin feeding line 9, milk of lime feed pipe
Line 8 is connected.
After column plate outer surface first connects sandblasting layer 12, then spray anticorrosive PTFE layer 13.By taking the second column plate 4 as an example,
The outer surface connection sandblasting layer 12 of second column plate 4, the outer surface of sandblasting layer 12 sprays anticorrosive PTFE layer 13 again.Bottom tower
Steam pipe line 6 is arranged in 7 lower section of plate.
When production, comes from the milk of lime of milk of lime feeding line 8 and come from the dichloro third of dichlorohydrin feeding line 9
Alcohol enters static mixer 1 and is mixed, and obtained saponification liquid is along saponification liquid horizontal feed pipeline 2, saponification
Liquid feeding vertical pipeline 3 enters inside saponification tower body 5, be further continued for along the second column plate 4, third column plate ..., bottom column plate 7 arrives
Up to 5 bottom of saponification tower body, saponification occurs in the process.The thick epoxychloropropane generated is carried out cold by condenser collection
Solidifying extraction, the saponification waste-water of generation squeeze into flash tank by the pump of 5 bottom of saponification tower body and carry out recuperation of heat processing.
As shown in Fig. 2, inside epoxychloropropane saponification column in the prior art, including saponification tower body 5 and saponification tower body 5
21 blocks of column plates, respectively upper layer column plate 11, the second column plate 4, third column plate, the 4th column plate ..., the 19th column plate, the 20th
Column plate, bottom column plate 7 further include saponification liquid horizontal feed pipeline 2, are connected after saponification liquid horizontal feed pipeline 2
Saponification liquid feeding vertical pipeline 3,3 bottom nozzle of saponification liquid feeding vertical pipeline connect saponification liquid horizontal flow pipe
Line 10.Upper layer column plate 11 is arranged in the lower section of saponification liquid horizontal flow pipeline 10.
Claims (8)
1. a kind of epoxychloropropane saponification column includes the column plate of saponification tower body (5) and saponification tower body (5) inside, further includes saponification
Reaction solution horizontal feed pipeline (2), it is characterised in that:Saponification liquid is connected after saponification liquid horizontal feed pipeline (2)
Feeding vertical pipeline (3), saponification tower body (5) is internal to be not provided with upper layer column plate (11), and column plate is followed successively by the second column plate from top to bottom
(4), third column plate, the 4th column plate ..., bottom column plate (7), setting second below saponification liquid feeding vertical pipeline (3)
Column plate (4).
2. epoxychloropropane saponification column according to claim 1, it is characterised in that:The saponification liquid vertical feed pipe
The distance between line (3) bottom nozzle and the second column plate (4) are 30-60cm.
3. epoxychloropropane saponification column according to claim 1, it is characterised in that:The saponification liquid horizontal feed pipe
Line (2) connects static mixer (1).
4. epoxychloropropane saponification column according to claim 3, it is characterised in that:The static mixer (1) respectively with
Dichlorohydrin feeding line (9), milk of lime feeding line (8) are connected.
5. epoxychloropropane saponification column according to claim 1, it is characterised in that:The number of the column plate is 15-25 blocks.
6. epoxychloropropane saponification column according to claim 1, it is characterised in that:The column plate outer surface sprays polytetrafluoro
Ethylene erosion resistant coating (13).
7. epoxychloropropane saponification column according to claim 6, it is characterised in that:The column plate outer surface first connects sandblasting
After layer (12), then spray anticorrosive PTFE layer (13).
8. epoxychloropropane saponification column according to claim 1, it is characterised in that:Setting below the bottom column plate (7)
Steam pipe line (6).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721825114.5U CN207685175U (en) | 2017-12-22 | 2017-12-22 | Epoxychloropropane saponification column |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721825114.5U CN207685175U (en) | 2017-12-22 | 2017-12-22 | Epoxychloropropane saponification column |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207685175U true CN207685175U (en) | 2018-08-03 |
Family
ID=62995429
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721825114.5U Active CN207685175U (en) | 2017-12-22 | 2017-12-22 | Epoxychloropropane saponification column |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207685175U (en) |
-
2017
- 2017-12-22 CN CN201721825114.5U patent/CN207685175U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110775986B (en) | Device for preparing ammonia by catalytic hydrolysis of urea and preparation method thereof | |
CN103613126B (en) | A kind of method and system removing vanadium impurity from titanic tetrachloride | |
CN204396420U (en) | For the rotary spraying device of cleaning reactor | |
CN203678369U (en) | Circulating cooling system of reaction kettle | |
CN207685175U (en) | Epoxychloropropane saponification column | |
CN207680627U (en) | Epoxychloropropane saponification system | |
CN110479043A (en) | A kind of purification work system | |
CN204275521U (en) | A kind of liquid ammonia gasification dry evaporator | |
CN207079005U (en) | A kind of wire rope factory abraum salt acid treatment device | |
CN205701243U (en) | A kind of plastic foil produces uses dyestuff circulating device | |
CN204625555U (en) | One once heats modified pitch production system | |
CN204147564U (en) | A kind of equipment utilizing solar energy concentrated vitriol zinc solution | |
CN211373282U (en) | Steam condensate gas recovery device | |
CN208553645U (en) | Emission-control equipment in copper sulphate production process | |
CN207085874U (en) | A kind of environment-friendly type neutralization reaction kettle | |
CN204159189U (en) | Absorption tower device in a kind of silver-colored method high-concentration formaldehyde device | |
CN208287511U (en) | A kind of N- acryloyl morpholine purifying plant | |
CN206351030U (en) | Acid solution blender and decoction system | |
CN112107969A (en) | Ammonia-containing tail gas absorption tower and matched energy recovery system | |
CN206843114U (en) | One kind energy-conservation water vaporization tower | |
CN206980496U (en) | A kind of dilute sulfuric acid production equipment | |
CN206343058U (en) | A kind of tail gas absorber in CBS production processes | |
CN206082505U (en) | Be used for 2 liquid caustic soda spraying feeding device of chloroacrylonitrile production | |
CN204981177U (en) | Production cyanuric acid by -product pyrolysis absorption system for ammonium sulfate | |
CN205219531U (en) | A cooling water circulation system for preparing damping fin |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address | ||
CP03 | Change of name, title or address |
Address after: No.227, Changguo East Road, chemical industry park, Zhangdian District, Zibo City, Shandong Province Patentee after: Shandong MINJI New Material Technology Co.,Ltd. Address before: 255000 Shandong city of Zibo province Zhangdian two road Hutian Road on the north side of cross East Chemical Industrial Zone Patentee before: SHANDONG MINJI CHEMICAL Co.,Ltd. |