CN205586968U - Warm -pressing control is chemical reaction tower with higher speed - Google Patents
Warm -pressing control is chemical reaction tower with higher speed Download PDFInfo
- Publication number
- CN205586968U CN205586968U CN201620358355.2U CN201620358355U CN205586968U CN 205586968 U CN205586968 U CN 205586968U CN 201620358355 U CN201620358355 U CN 201620358355U CN 205586968 U CN205586968 U CN 205586968U
- Authority
- CN
- China
- Prior art keywords
- tower
- tower body
- catalyst
- temperature
- reaction
- 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
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Abstract
The utility model discloses a warm -pressing control is chemical reaction tower with higher speed, including the tower body, at the bottom of ta gai and tower are installed respectively to the top of tower body and bottom, and all is connected with the tower body through the press joining pipe at the bottom of tagai and the tower, the side of tower body still fixed mounting have double -layered set, the tower external heat exchanger is still installed to tower body one side, the temperature control pipe is all installed to top and bottom at the tower external heat exchanger, there is the catalyser -accelerator tower at the internally mounted of tower body, and the catalyser -accelerator tower is connected at the tower body inner wall through distribution baffle and baffle, one side fixed mounting has the liquid atomization ware at the catalyser -accelerator tower, there is the catalyst entry at catalyser -accelerator tower opposite side fixed mounting, the bottom is equipped with the drain hole at the bottom of the tower, through the control to temperature and pressure, guarantee the required condition of reaction, add catalyst assurance reaction rate, reach the reaction requirement on the whole, the reaction rate in the design has also been reached, and artificial intervention convenient and fast.
Description
Technical field
This utility model relates to technical field of chemical, is specially a kind of temperature and pressure control and accelerates chemical anti-
Answer tower.
Background technology
The mankind are very close with the relation of chemical industry, spread to the every aspect of life.In the modern life,
The most all it be unable to do without chemical products, from material lifes such as clothing, food, shelter, row to culture skill
The cultural life such as art, amusement, is required for chemical products and services for it, and some chemical products is sent out the mankind
In exhibition history, play epoch-making important function, their production and application, even represent the mankind
Certain historical stage of civilization, the normal operation of chemical products production process, product quality and yield
Controlling and ensure, be unableing to do without adaptation and the normal operation of various chemical industry equipments, the apolegamy of chemical industry equipment must
Need to be fitted by calculating in detail, design, process, manufacture and matching whole chemical process
Answer required for Chemical Manufacture.
In particular with the progress of technology, temperature, pressure and the participation reacting substance to chemical industry equipment
State suffer from strict requirements, and while temperature and pressure when the most accurately controlling reaction
Missing the flank speed of reaction, therefore in chemical reaction, the application of catalyst is requisite,
But traditional reaction tower, controls in temperature and there is also many problems, such as temperature in the use of catalyst
Can not accurately control between degree and catalyst, manual intervention is inconvenient.
Utility model content
For problem above, this utility model provides a kind of temperature and pressure and controls to accelerate chemical reaction tower, logical
Cross the control to temperature and pressure, it is ensured that the condition needed for reaction, ensure reaction speed plus catalyst
Rate, has the most i.e. reached reaction requirement, has also reached the response speed in design, and manually
Intervene convenient and swift, can effectively solve the problem in background technology.
For achieving the above object, this utility model provides following technical scheme: a kind of temperature and pressure control to accelerate
Chemical reaction tower, including tower body, the top of described tower body and bottom are separately installed with at the bottom of Ta Gai and tower,
And be all connected with tower body by pressure connection tube at the bottom of Ta Gai and tower, also it is installed with in the side of tower body
Chuck, described tower body side is also equipped with tower external heat exchanger, equal at the top of tower external heat exchanger and bottom
Being provided with temperature control zone, internally installed at tower body has catalyst to accelerate tower, and catalyst accelerates tower
It is connected to tower body inwall by distribution separator and baffle plate, accelerates tower side at catalyst and be installed with liquid
Body nebulizer, accelerates tower opposite side at catalyst and is installed with catalyst inlet, set bottom at the bottom of tower
There is drain hole.
As a kind of preferably technical scheme of this utility model, described catalyst accelerates the bottom of tower and is provided with
Gas distributor.
As a kind of preferably technical scheme of this utility model, described tower body side is provided with several liquid
Body inlet port.
As a kind of preferably technical scheme of this utility model, the quantity of described chuck is four, and four
Individual chuck is respectively and fixedly installed to tower body outer surface both sides.
Compared with prior art, the beneficial effects of the utility model are: by the control to temperature and pressure
System, it is ensured that the condition needed for reaction, is ensureing reaction rate plus catalyst, is the most i.e. reaching
Reaction requirement, has also reached the response speed in design, and manual intervention is convenient and swift.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation；
Fig. 2 is this utility model pressure connection tube structural representation.
In figure: 1-tower body；2-tower lid；At the bottom of 3-tower；4-chuck；5-tower external heat exchanger；6-catalyst
Accelerate tower；7-liquid trap；8-distribution separator；9-baffle plate；10-gas distributor；11-liquid
Nebulizer；12-catalyst inlet；13-liquid inlet；14-temperature control zone；15-drain hole；
16-pressure connection tube.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, to the skill in this utility model embodiment
Art scheme is clearly and completely described, it is clear that described embodiment is only this utility model
A part of embodiment rather than whole embodiments.Based on the embodiment in this utility model, ability
The every other embodiment that territory those of ordinary skill is obtained under not making creative work premise,
Broadly fall into the scope of this utility model protection.
Embodiment:
Referring to Fig. 1 and Fig. 2, this utility model provides a kind of technical scheme: a kind of temperature and pressure control to accelerate
Chemical reaction tower, including tower body 1, is provided with several liquid inlets 13 in tower body 1 side, logical
Cross these inlets and realize the entrance of reaction material requested and catalyst etc., the top of tower body 1 and bottom
It is separately installed with at the bottom of tower lid 2 and tower 3, and 3 all by pressure connection tube 16 and tower at the bottom of tower lid 2 and tower
Body 1 connects, and closes tower body by pressure effect, particularly exceedes design load when pressure is excessive,
Will automatically split, the gases at high pressure within air defense, it is ensured that reaction safety, in the side of tower body 1 also
Being installed with chuck 4, the quantity of chuck 4 is four, and four chucks 4 are respectively and fixedly installed to tower
Body 1 outer surface both sides, the effect of chuck 4 is fixative body inlet port 13 and the reinforcing to tower body,
Tower body 1 side is also equipped with tower external heat exchanger 5, by its heat exchange action, controls tower body 1 internal
Thermal change, be mounted on temperature control zone 14 at the top of tower external heat exchanger 5 and bottom, pass through
The control action of temperature control zone 14 realizes accurately the carrying out, in the inside of tower body 1 of the outer heat exchange of tower
Being provided with catalyst and accelerate tower 6, accelerate the response speed in tower, catalyst accelerates the bottom of tower 6 and is provided with
Gas distributor 10, carries out State Transferring by required reactant, and catalyst accelerates tower 6 by distribution
Dividing plate 8 and baffle plate 9 are connected to tower body 1 inwall, distribution separator 8 and baffle plate 9 and carry out gradient control respectively
System and barrier effect, accelerate tower 6 side at catalyst and be installed with liquid atomiser 11, carries out anti-
Answer the State Transferring of thing, accelerate tower 6 opposite side at catalyst and be installed with catalyst inlet 12, side
Just catalyst change is with supplementary, is provided with drain hole 15 bottom at the bottom of tower 3, collects finished product；By to temperature
Degree and the control of pressure, it is ensured that the condition needed for reaction, ensureing reaction rate plus catalyst,
The most i.e. reach reaction requirement, also reach the response speed in design, and manual intervention side
The most quick.
The foregoing is only preferred embodiment of the present utility model, not new in order to limit this practicality
Type, all any amendment, equivalent and improvement made within spirit of the present utility model and principle
Deng, within should be included in protection domain of the present utility model.
Claims (4)
1. temperature and pressure control to accelerate a chemical reaction tower, including tower body (1), described tower body (1)
Top and bottom are separately installed with tower lid (2) He Tadi (3), and tower lid (2) He Tadi (3) is equal
It is connected with tower body (1) by pressure connection tube (16), also fixedly mounts in the side of tower body (1)
There is chuck (4), it is characterised in that: described tower body (1) side is also equipped with tower external heat exchanger (5),
It is mounted on temperature control zone (14), in tower body (1) at the top of tower external heat exchanger (5) and bottom
Internally installed have catalyst to accelerate tower (6), and catalyst accelerates tower (6) by distribution separator (8)
It is connected to tower body (1) inwall with baffle plate (9), accelerates tower (6) side at catalyst and be installed with
Liquid atomiser (11), accelerates tower (6) opposite side at catalyst and is installed with catalyst inlet (12),
It is provided with drain hole (15) in (3) bottom at the bottom of tower.
A kind of temperature and pressure the most according to claim 1 control to accelerate chemical reaction tower, it is characterised in that:
Described catalyst accelerates the bottom of tower (6) and is provided with gas distributor (10).
A kind of temperature and pressure the most according to claim 1 control to accelerate chemical reaction tower, it is characterised in that:
Described tower body (1) side is provided with several liquid inlets (13).
A kind of temperature and pressure the most according to claim 1 control to accelerate chemical reaction tower, it is characterised in that:
The quantity of described chuck (4) is four, and four chucks (4) are respectively and fixedly installed to tower body (1)
Outer surface both sides.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620358355.2U CN205586968U (en) | 2016-04-26 | 2016-04-26 | Warm -pressing control is chemical reaction tower with higher speed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620358355.2U CN205586968U (en) | 2016-04-26 | 2016-04-26 | Warm -pressing control is chemical reaction tower with higher speed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205586968U true CN205586968U (en) | 2016-09-21 |
Family
ID=56935860
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620358355.2U Expired - Fee Related CN205586968U (en) | 2016-04-26 | 2016-04-26 | Warm -pressing control is chemical reaction tower with higher speed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205586968U (en) |
-
2016
- 2016-04-26 CN CN201620358355.2U patent/CN205586968U/en not_active Expired - Fee Related
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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: 20160921 Termination date: 20170426 |