CN207371538U - A kind of catalyst reaction bed - Google Patents
A kind of catalyst reaction bed Download PDFInfo
- Publication number
- CN207371538U CN207371538U CN201720984079.5U CN201720984079U CN207371538U CN 207371538 U CN207371538 U CN 207371538U CN 201720984079 U CN201720984079 U CN 201720984079U CN 207371538 U CN207371538 U CN 207371538U
- Authority
- CN
- China
- Prior art keywords
- downside
- catalyst reaction
- reaction bed
- petroleum pipeline
- main body
- 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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- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Thermotherapy And Cooling Therapy Devices (AREA)
Abstract
The utility model discloses a kind of catalyst reaction beds,Including heating box main body,Thermistor is provided on the inside of the heating box main body,The thermistor is connected by conducting wire with battery,The battery is connected by conducting wire with adding thermal resistance,Petroleum pipeline is provided on the downside of the adding thermal resistance,Cooling cylinder is provided on the right side of the petroleum pipeline,Heater box is provided on the right side of the cooling cylinder,The petroleum pipeline is connected by stent with carrying board,Vertical supports are provided on the downside of the carrying board,Horizontal gird is provided on the right side of the vertical supports,Heating tube is provided on the inside of the heater box,Connecting plate is symmetrically arranged at left and right sides of constant temperature resistance,The catalyst reaction bed,It is designed using frame-type,It is provided with heating box main body,Convenient for being heated to the liquid flowed through,It is additionally provided with compensation adding thermal resistance,The temperature difference of generation is compensated,Using very convenient,Meet the requirement on chemical industry.
Description
Technical field
The utility model is related to chemical technology fields, are specially a kind of catalyst reaction bed.
Background technology
So-called catalyst reaction bed is exactly a kind of device for aiding in the charging of Chemical Manufacture constant temperature, is carrying out Chemical Manufacture mistake
Cheng Zhong, the sometimes production of catalyst need certain temperature that can carry out, are needed during entire material production constantly
Holding constant temperature, during material production, material transportation distance it is longer, temperature is easily reduced so that Chemical Manufacture without
Method is normally carried out, and the major way used now is exactly to carry out external insulation to transmission pipeline, but this kind of method is only to subtract
Lack thermal loss, but the reduction that the temperature of material still can be different degrees of so that user uses unusual inconvenience.
So how to design a kind of catalyst reaction bed, becoming us will currently solve the problems, such as.
Utility model content
The purpose of this utility model is to provide a kind of catalyst reaction bed, to solve mentioned above in the background art ask
Topic.
To achieve the above object, the utility model provides following technical solution：A kind of catalyst reaction bed, including heater box
Main body, the heating box main body inside are provided with thermistor, and the thermistor is connected by conducting wire with battery, the battery
It is connected by conducting wire with adding thermal resistance, petroleum pipeline is provided on the downside of the adding thermal resistance, is provided on the right side of the petroleum pipeline
Cylinder is cooled down, is provided with heater box on the right side of the cooling cylinder, the petroleum pipeline is connected by stent with carrying board, the carrying board
Downside be provided with vertical supports, horizontal gird is provided on the right side of the vertical supports, is provided on the inside of the heater box
Heating tube is symmetrically arranged with connecting plate at left and right sides of constant temperature resistance, metal cap, the metal is provided on the upside of the battery
Carbon-point is provided on the downside of cap, alkaline material is provided on the upside of the carbon-point, the downside of the alkalescence material is provided with electrolyte, institute
It states and clay is provided on the downside of electrolyte.
Further, the cylinder whole installation that cools down is into olive shape.
Further, the carrying board carries out vertical welding with vertical supports.
Further, the horizontal gird is arranged in parallel with horizontal direction.
Further, it is provided with constant temperature resistance on the downside of the heating tube.
Further, it is provided with stent on the downside of the petroleum pipeline.
Further, it is provided with discharge port on the right side of the heater box.
Further, the heating box main body is integrally made of stainless steel material.
Compared with prior art, the beneficial effects of the utility model are：The catalyst reaction bed, is designed using frame-type,
Heating box main body is provided with, convenient for being heated to the liquid flowed through, compensation adding thermal resistance is additionally provided with, to the temperature difference of generation
It compensates, use is very convenient, meets the requirement on chemical industry.
Description of the drawings
Fig. 1 is the overall structure diagram of the utility model；
Fig. 2 is the structural map of the utility model heater box；
Fig. 3 is the battery schematic diagram of the utility model；
In figure：1- heats box main body；2- thermistors；3- conducting wires；4- batteries；5- adding thermal resistances；6- petroleum pipelines；7- is cooled down
Cylinder；8- heater boxes；9- discharge ports；10- stents；11- carrying boards；12- vertical supports；13- horizontal girds；14- heating tubes；15-
Constant temperature resistance；16- connecting plates；17- metal caps；18- carbon-points；19- alkalescence material；20- electrolyte；21- clays.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
It please refers to Fig.1, Fig. 2, Fig. 3, the utility model provides a kind of technical solution：A kind of catalyst reaction bed, including adding
Hot tank main body 1,1 inside of heating box main body are provided with thermistor 2, and the thermistor 2 is connected by conducting wire 3 and battery 4
It connects, the battery 4 is connected by conducting wire 3 with adding thermal resistance 5, and the downside of the adding thermal resistance 5 is provided with petroleum pipeline 6, described defeated
The right side of oil pipe 6 is provided with cooling cylinder 7, and the right side of the cooling cylinder 7 is provided with heater box 8, and the petroleum pipeline 6 passes through stent 10
It is connected with carrying board 11, the downside of the carrying board 11 is provided with vertical supports 12, and the right side of the vertical supports 12 is provided with
Horizontal gird 13, the inside of the heater box 8 are provided with heating tube 14, and the left and right sides of constant temperature resistance 15 is symmetrically arranged with connection
Plate 16, the upside of the battery 4 are provided with metal cap 17, and the downside of the metal cap 17 is provided with carbon-point 18, the carbon-point 18
Upside be provided with alkalescence material 19, the downside of the alkalescence material 19 is provided with electrolyte 20, and the downside of the electrolyte 20 is set
There is clay 21.
Further, cooling 7 whole installation of cylinder can be effectively increased the heating surface (area) (HS of pipeline part into olive shape.
Further, the carrying board 11 carries out vertical welding with vertical supports 12, can cause element of installation connection more
It is firm to add.
Further, the horizontal gird 13 is arranged in parallel with horizontal direction, can be effectively increased element of installation
Harmony.
Further, the downside of the heating tube 14 is provided with constant temperature resistance 15, can control inside entire production flow line
Liquid keeps constant temperature.
Further, the downside of the petroleum pipeline 6 is provided with stent 10, pipeline can be supported in order to equipment.
Further, the right side of the heater box 8 is provided with discharge port 9, can discharge in order to equipment.
Further, the heating box main body 1 is whole is made of stainless steel material, can effectively improve element of installation
Durability.
Operation principle：When the device is in use, clear water, object to be produced are filled into the inside of heating box main body 1 first
Expect from the left end of petroleum pipeline 6 to enter and flow into cooling cylinder 7, at this time thermistor 2 can to heat the temperature in box main body 1 into
Row sensing, when temperature is too low, the resistance value of thermistor 2 can substantially reduce, and entire circuit forms close access, then heating electricity
Resistance 5 is started to work, and the water body in heating box main body 1 is heated, after the completion of to be heated, the substance flowed through in petroleum pipeline 6 exists
It cools down and water proof heating is carried out in cylinder 7, during the heated case 8 of material flow after heating, constant temperature resistance 15 carries out temperature-compensating to it again
Heating, last material are flowed out from discharge port 9, and whole equipment is terminated using process.
While there has been shown and described that the embodiment of the utility model, for the ordinary skill in the art,
It is appreciated that in the case where not departing from the principle of the utility model and spirit can these embodiments be carried out with a variety of variations, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (8)
1. a kind of catalyst reaction bed, including heating box main body (1), it is characterised in that：It is set on the inside of the heating box main body (1)
There is thermistor (2), the thermistor (2) is connected by conducting wire (3) with battery (4), and the battery (4) passes through conducting wire (3)
It is connected with adding thermal resistance (5), petroleum pipeline (6) is provided on the downside of the adding thermal resistance (5), is set on the right side of the petroleum pipeline (6)
Be equipped with cooling cylinder (7), be provided with heater box (8) on the right side of cooling cylinder (7), the petroleum pipeline (6) by stent (10) with
Carrying board (11) connects, and vertical supports (12), the right side of the vertical supports (12) are provided on the downside of the carrying board (11)
Horizontal gird (13) is provided with, heating tube (14), the left and right sides of constant temperature resistance (15) are provided on the inside of the heater box (8)
Connecting plate (16) is symmetrically arranged with, metal cap (17) is provided on the upside of the battery (4), is set on the downside of the metal cap (17)
Carbon-point (18) is equipped with, alkalescence material (19) is provided on the upside of the carbon-point (18), electricity is provided on the downside of the alkalescence material (19)
Matter (20) is solved, clay (21) is provided on the downside of the electrolyte (20).
2. a kind of catalyst reaction bed according to claim 1, it is characterised in that：It is described cooling cylinder (7) whole installation into
Olive shape.
3. a kind of catalyst reaction bed according to claim 1, it is characterised in that：The carrying board (11) and vertical supports
(12) vertical welding is carried out.
4. a kind of catalyst reaction bed according to claim 1, it is characterised in that：The horizontal gird (13) and level side
To being arranged in parallel.
5. a kind of catalyst reaction bed according to claim 1, it is characterised in that：The downside of the heating tube (14) is set
There is constant temperature resistance (15).
6. a kind of catalyst reaction bed according to claim 1, it is characterised in that：The downside of the petroleum pipeline (6) is set
There is stent (10).
7. a kind of catalyst reaction bed according to claim 1, it is characterised in that：The right side of the heater box (8) is set
There is discharge port (9).
8. a kind of catalyst reaction bed according to claim 1, it is characterised in that：The heating box main body (1) is integrally adopted
It is made of stainless steel material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720984079.5U CN207371538U (en) | 2017-08-08 | 2017-08-08 | A kind of catalyst reaction bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720984079.5U CN207371538U (en) | 2017-08-08 | 2017-08-08 | A kind of catalyst reaction bed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207371538U true CN207371538U (en) | 2018-05-18 |
Family
ID=62342346
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720984079.5U Expired - Fee Related CN207371538U (en) | 2017-08-08 | 2017-08-08 | A kind of catalyst reaction bed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207371538U (en) |
-
2017
- 2017-08-08 CN CN201720984079.5U patent/CN207371538U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180518 Termination date: 20190808 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |