CN207951402U - Convenient for the hydrogenation reactor of loading catalyst - Google Patents
Convenient for the hydrogenation reactor of loading catalyst Download PDFInfo
- Publication number
- CN207951402U CN207951402U CN201721825356.4U CN201721825356U CN207951402U CN 207951402 U CN207951402 U CN 207951402U CN 201721825356 U CN201721825356 U CN 201721825356U CN 207951402 U CN207951402 U CN 207951402U
- Authority
- CN
- China
- Prior art keywords
- catalyst
- layer
- cylindrical shell
- pivoting support
- inner ring
- 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
Landscapes
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The utility model discloses a kind of hydrogenation reactor convenient for loading catalyst, including cylindrical shell, catalyst support frame, steel wire and catalyst layer have been evenly arranged in cylindrical shell;Hydrogenation reactor further includes the catalyst input supervisor being set in cylindrical shell, inputs comb and the horizontal stand being arranged above each catalyst layer under the catalyst exhaust outlet for being responsible for connection, the vertical catalyst being fixed on catalyst support frame with catalyst, pivoting support is provided on horizontal stand, it is connected with cylinder on the inner ring of pivoting support, scraper plate is connected on the piston rod of cylinder.The utility model hydrogenation reactor, can will be on catalyst emission to corresponding catalyst layer steel wire by controlling the electronic cutting ball valve of No.1 and No. two electronic cutting ball valves in loading catalyst;And during filling, moreover it is possible to drive the inner ring of pivoting support to rotate by controlling motor, so that scraper plate is struck off catalyst layer, can guarantee that the thickness of catalyst layer is uniform.
Description
Technical field
The utility model is related to a kind of chemical industry equipment, more particularly to the hydrogenation reaction in a kind of high-purity propane production line
Device.
Background technology
The mainstream refrigerant of domestic market be containing fluorinated refrigerant, such as R22, R410A and R407, but they cause it is smelly
The environmental problems such as oxygen layer destruction, greenhouse effects.For the environmental protection refrigerant R290 for obtaining natural, high-purity propane production technology is ground
Study carefully the research and development focus as refrigeration industry.
At present using the low-purity propane from natural gas or crude oil as raw material, through pretreatment of raw material, saturated hydrogenation, separation essence
The process of ultra-pure propane is made in the technical process such as system, has preferable development prospect.Core equipment in the technique is
Hydrogenation reactor, low-purity propane is after the pretreatments such as desulfurization, dehydration, with hydrogen together as reactant, is admitted to plus hydrogen is anti-
Device is answered, under hydrogenation catalyst effect, so that the unsaturated component such as alkene in raw material is saturated, obtains adding hydrogen saturated products.
Existing hydrogenation reactor, loading catalyst are manually completed, and specially worker is introduced into reactor, then
Catalyst is hung in into reactor from reactor head entrance by crane, finally again by catalyst is manually transferred to catalyst support
On the net, the filling labor intensity of catalyst is big, and filling operating efficiency is low.
Utility model content
In view of this, the purpose of this utility model is to provide a kind of hydrogenation reactor convenient for loading catalyst, to solve
The technical problem that labor intensity is big existing for artificial loading catalyst in the prior art, packing efficiency is low.
The utility model is convenient for the hydrogenation reactor of loading catalyst, including cylindrical shell, in the cylindrical shell uniformly
If being disposed with dried layer catalyst support frame, the steel wire for placing catalyst, the steel wire are provided on the catalyst support frame
It is provided with catalyst layer on the net;
Further include the catalyst input supervisor being set in cylindrical shell, the feed end of the catalyst input supervisor is located at
Outside cylindrical shell, and hopper is provided on the feed end of catalyst input supervisor;
It further include the catalyst exhaust outlet that supervisor's connection is inputted with catalyst;In addition to basecoat catalyst layer, remaining
Each catalyst layer be corresponding with a catalyst exhaust outlet;It is additionally provided with several No.1s on the catalyst input supervisor
Electronic cutting ball valve, there are one the electronic cutting ball valves of No.1 for the top correspondence of each catalyst layer;Every catalyst exhaust outlet
On also set up there are one No. two electronic cutting ball valves;
Further include comb under the catalyst being fixed on vertically on catalyst support frame, correspondence is set on each catalyst support frame
It is equipped with comb under an at least catalyst, the input end of comb is located at the bottom of catalyst layer under catalyst, under every catalyst
There are one No. three electronic cutting ball valves for setting on comb;
Further include the horizontal stand being arranged above each catalyst layer, pivoting support be provided on the horizontal stand,
It is with teeth on the inner ring of the pivoting support, the motor for driving pivoting support inner ring to rotate, institute are additionally provided on horizontal stand
State the driving gear being connected on the armature spindle of motor with tooth engagement on pivoting support inner ring;On the inner ring of the pivoting support also
It is connected with cylinder, the piston rod of the cylinder stretches out straight down, and scraper plate is connected on the piston rod end of cylinder;
The bottom of the cylindrical shell is additionally provided with the drainage conduit of discharge catalyst.
The beneficial effects of the utility model:
1, the utility model is convenient for the hydrogenation reactor of loading catalyst, and by catalyst, input supervisor is defeated by catalyst
Enter into hydrogenation reactor, it, can be by controlling the electronic cutting ball valve of No.1 and No. two electronic cut-out balls in loading catalyst
Valve will be on catalyst emission to corresponding catalyst layer steel wire;And during filling, moreover it is possible to by controlling motor driving
The inner ring of pivoting support rotates, and so that scraper plate is struck off catalyst layer, can guarantee that the thickness of catalyst layer is uniform.This hydrogenation reactor energy
Realize that automatic Loading catalyst, filling operating efficiency are high.
2, the utility model is convenient for the hydrogenation reactor of loading catalyst, when needing replacing catalyst, is urged by opening
Each layer catalyst can be drained into the bottom of cylindrical shell, into cylindrical shell by No. three electronic stop valves under agent on comb
Bottom catalyst again from drainage conduit be discharged hydrogenation reactor, catalyst discharge be automatically performed, discharge is efficient;And in discharge mistake
Cheng Zhong, motor drive the inner ring rotation of pivoting support, and it is close with steel wire that cylinder drives scraper plate to drop to, what scraper plate can be more thoroughly
Catalyst on steel wire is scraped into comb under catalyst, discharge is clean.
Description of the drawings
Fig. 1 is the structural schematic diagram of the hydrogenation reactor convenient for loading catalyst in embodiment;
Fig. 2 is the close-up schematic view of the hydrogenation reactor convenient for loading catalyst in embodiment.
Specific implementation mode
The utility model is further described with reference to the accompanying drawings and examples.
As shown, being convenient for the hydrogenation reactor of loading catalyst, including cylindrical shell 1, the column in the present embodiment
If being evenly arranged dried layer catalyst support frame 2 in shell, the steel wire for placing catalyst is provided on the catalyst support frame
Net 3 is provided with catalyst layer 4 on the steel wire.
It is convenient for the hydrogenation reactor of loading catalyst in the present embodiment, further includes that the catalyst that is set in cylindrical shell is defeated
Enter supervisor 5, catalyst input supervisor is parallel with the axial direction of cylindrical shell, and catalyst input supervisor is close to along cylindrical shell
Side portion is arranged.The feed end of the catalyst input supervisor is located at outside cylindrical shell, and the feed end of catalyst input supervisor
On be provided with hopper 6.
It is convenient for the hydrogenation reactor of loading catalyst in the present embodiment, further includes the catalysis for inputting supervisor's connection with catalyst
Agent exhaust outlet 7;In addition to basecoat catalyst layer, remaining each catalyst layer is corresponding with a catalyst exhaust outlet;
It is additionally provided with the electronic cutting ball valve 8 of several No.1s on the catalyst input supervisor, is corresponding with above each catalyst layer
One electronic cutting ball valve of No.1;No. two electronic cutting ball valves 9 there are one being also set up on every catalyst exhaust outlet.
It is convenient for the hydrogenation reactor of loading catalyst in the present embodiment, further includes being fixed on vertically on catalyst support frame
Comb 10 under catalyst, are correspondingly arranged on comb under an at least catalyst on each catalyst support frame, comb under catalyst
Input end be located at the bottom of catalyst layer, there are one No. three electronic cutting ball valves 11 for setting on comb under every catalyst.
It is convenient for the hydrogenation reactor of loading catalyst in the present embodiment, further includes the water being arranged above each catalyst layer
Flat holder 12, is provided with pivoting support 13 on the horizontal stand, with teeth on the inner ring of the pivoting support, on horizontal stand also
It is provided with the motor 14 for driving pivoting support inner ring to rotate, is connected with and pivoting support inner ring on the armature spindle of the motor
The driving gear 15 of upper tooth engagement;Cylinder 16 is also associated on the inner ring of the pivoting support, the piston rod of the cylinder is vertical
It extends downwardly, and is connected with scraper plate 17 on the piston rod end of cylinder.Motor in the present embodiment is waterproof machine, and cylinder is anti-
Aqueous vapor cylinder, each electronic cutting ball valve are that waterproof establishes cutting ball valve.
The bottom of the cylindrical shell is additionally provided with the drainage conduit 18 of discharge catalyst.
It is convenient for the hydrogenation reactor of loading catalyst, catalyst support frame to be specifically provided with three layers in the present embodiment, dress
Sequence is filled out from top to bottom, i.e., first to load third layer, the second layer is recharged, finally loads first layer.In loading catalyst, first
The amount of each catalyst layer is calculated, is then added the hopper that catalyst is inputted from catalyst on supervisor's feed end by crane
Enter.
When loading third layer catalyst, the electronic cutting ball valve of each No.1 need to be closed, and open corresponding with third layer
No. two electronic cutting ball valves;After third layer is loaded, No. two electronic cutting ball valves corresponding with third layer are closed.
When loading second layer catalyst, the electronic cutting ball valve of No.1 above third layer is opened, and opens and second
The corresponding No. two electronic cutting ball valve of floor;The second layer load after, will and No. two electronic cutting ball valves corresponding with the second layer
It closes.
When loading third layer catalyst, each No. two electronic cutting ball valves are turned off, and each electronic cutting ball valve of No.1 is opened
It opens.
And during filling, hydrogenation reactor can also drive the inner ring of pivoting support by controlling motor in the present embodiment
Rotation, makes scraper plate strike off catalyst layer, can guarantee that the thickness of catalyst layer is uniform.This hydrogenation reactor can realize that automatic Loading is urged
Agent, filling operating efficiency are high.
And when needing replacing catalyst, hydrogenation reactor can also be by opening under catalyst on comb in the present embodiment
No. three electronic stop valves, each layer catalyst is drained into the bottom of cylindrical shell, into cylindrical shell bottom catalyst again
Hydrogenation reactor is discharged from drainage conduit, catalyst discharge is automatically performed, and discharge is efficient;And in discharging process, motor driving
The inner ring of pivoting support rotates, and it is close with steel wire that cylinder drives scraper plate to drop to, and what scraper plate can be more thoroughly will be on steel wire
Catalyst scrapes comb under catalyst, and discharge is clean.
Finally illustrate, above example is merely intended for describing the technical solutions of the present application, but not for limiting the present application, although ginseng
The utility model is described in detail according to preferred embodiment, it will be understood by those of ordinary skill in the art that, it can be to this
The technical solution of utility model is modified or replaced equivalently, without departing from the objective and model of technical solutions of the utility model
It encloses, should all cover in the right of the utility model.
Claims (1)
1. a kind of hydrogenation reactor convenient for loading catalyst, including cylindrical shell, if being evenly arranged in the cylindrical shell
Dried layer catalyst support frame is provided with the steel wire for placing catalyst on the catalyst support frame, is arranged on the steel wire
There is catalyst layer;It is characterized in that:
Further include the catalyst input supervisor being set in cylindrical shell, the feed end of the catalyst input supervisor is located at column
Outside shell, and hopper is provided on the feed end of catalyst input supervisor;
It further include the catalyst exhaust outlet that supervisor's connection is inputted with catalyst;In addition to basecoat catalyst layer, remaining is every
One catalyst layer is corresponding with a catalyst exhaust outlet;It is electronic it to be additionally provided with several No.1s on the catalyst input supervisor
Cutting ball valve, there are one the electronic cutting ball valves of No.1 for the top correspondence of each catalyst layer;On every catalyst exhaust outlet also
There are one No. two electronic cutting ball valves for setting;
Further include comb under the catalyst being fixed on vertically on catalyst support frame, is correspondingly arranged on each catalyst support frame
Comb under an at least catalyst, the input end of comb is located at the bottom of catalyst layer under catalyst, comb under every catalyst
There are one No. three electronic cutting ball valves for upper setting;
Further include the horizontal stand being arranged above each catalyst layer, pivoting support is provided on the horizontal stand, it is described
It is with teeth on the inner ring of pivoting support, the motor for driving pivoting support inner ring to rotate, the electricity are additionally provided on horizontal stand
The driving gear with tooth engagement on pivoting support inner ring is connected on the armature spindle of machine;It is also connected on the inner ring of the pivoting support
There is cylinder, the piston rod of the cylinder stretches out straight down, and scraper plate is connected on the piston rod end of cylinder;
The bottom of the cylindrical shell is additionally provided with the drainage conduit of discharge catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721825356.4U CN207951402U (en) | 2017-12-22 | 2017-12-22 | Convenient for the hydrogenation reactor of loading catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721825356.4U CN207951402U (en) | 2017-12-22 | 2017-12-22 | Convenient for the hydrogenation reactor of loading catalyst |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207951402U true CN207951402U (en) | 2018-10-12 |
Family
ID=63729881
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721825356.4U Expired - Fee Related CN207951402U (en) | 2017-12-22 | 2017-12-22 | Convenient for the hydrogenation reactor of loading catalyst |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207951402U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115414870A (en) * | 2022-08-25 | 2022-12-02 | 江苏博颂能源科技有限公司 | ADHO device is anti for unit again catalyst flourishing device |
-
2017
- 2017-12-22 CN CN201721825356.4U patent/CN207951402U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115414870A (en) * | 2022-08-25 | 2022-12-02 | 江苏博颂能源科技有限公司 | ADHO device is anti for unit again catalyst flourishing device |
CN115414870B (en) * | 2022-08-25 | 2023-11-03 | 江苏博颂能源科技有限公司 | Catalyst loading device for ADHO device anti-regeneration unit |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN206122292U (en) | Tube cleaning device for biological teaching | |
CN201330159Y (en) | Activated carbon rinsing equipment | |
CN205095466U (en) | Kitchen waste oil -water separation device | |
CN207951402U (en) | Convenient for the hydrogenation reactor of loading catalyst | |
CN107399866A (en) | A kind of plumbing waste water aeration apparatus | |
CN106823458A (en) | A kind of extraction equipment | |
CN108201912A (en) | A kind of dry cow dung smashes device | |
CN207130393U (en) | Raw cotton mixing arrangement is used in one kind weaving | |
CN207313452U (en) | The effective integrated production equipment of closed fermented livestock excrement | |
CN107008034A (en) | A kind of oily water separating equipment | |
CN211436897U (en) | Powder coating device that sieves | |
CN115175855B (en) | Chemical product packaging device | |
CN209338582U (en) | For energy saving and environment friendly tanning equipment used in suede production and processing | |
CN205517546U (en) | Solution agitated vessel and deep are transferred to drive and are used solution preparation | |
CN207270834U (en) | A kind of highly effective petroleum filter easy to cleaning | |
CN206613792U (en) | A kind of cleaning equipment for parts | |
CN205552778U (en) | A processing apparatus for wood, bamboo timber are modified | |
JP3164370U (en) | Kneading equipment | |
CN205708170U (en) | A kind of chemical reagent holding vessel of vehicle-mounted integrated form soil restoring device | |
CN217614786U (en) | Production of VOC adsorbent is with dipping loaded active noble metal device | |
JP2721388B2 (en) | Sludge dewatering equipment | |
CN217511639U (en) | High-efficient intelligent heating equipment | |
CN204350999U (en) | A kind of compressed coconut stirs loose rehydration depickling cleaning equipment | |
CN204125216U (en) | The chemicals dosing plant of novel powder medicament | |
CN205435045U (en) | Plant medicine cosmetics production facility |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
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: 20181012 Termination date: 20191222 |