CN204841633U - Production system of load type catalyst - Google Patents
Production system of load type catalyst Download PDFInfo
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- CN204841633U CN204841633U CN201520387408.9U CN201520387408U CN204841633U CN 204841633 U CN204841633 U CN 204841633U CN 201520387408 U CN201520387408 U CN 201520387408U CN 204841633 U CN204841633 U CN 204841633U
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Abstract
The utility model belongs to a manufacture of catalyst technical field, concretely relates to production system of load type catalyst, it includes the reactor, and solid -liquid separation equipment is connected to the reactor, and solid -liquid separation equipment passes through material conveyor and connects the vibration funnel, and the vibratory liquefaction bed is connected to the vibration funnel. Solid -liquid separation equipment adopts the centrifugal separator, and material conveyor goes on through electric block, and vibrating motor is installed on the funnel both sides of vibration funnel, an installation screen cloth in the funnel of vibration funnel, and screen net hole can select according to the catalyst granules size in the footpath. The utility model discloses a production system mainly used preparation microballon type beaded catalyst has not only improved productivity, has eliminated the mutual bonding between the catalyst particle moreover.
Description
Technical field
The utility model metal catalyst manufacturing technology field, is specifically related to a kind of production system of loaded catalyst.
Background technology
The preparation method of solid catalyst has multiple, infusion process is one wherein, this method is normally used for preparing loaded catalyst, namely be soak in solution carrier being placed with active component, be attached to after on carrier until the active specy in solution, obtain catalyst through Separation of Solid and Liquid, drying, roasting and activation.
In catalyst manufacturing procedures, the process of usual Separation of Solid and Liquid adopts filter tunnel suction filtration, and dry run adopts baking oven to dry, and adopts revolving drier during roasting.
Usually, in loaded catalyst manufacture process, adopt filter tunnel suction filtration can reach Separation of Solid and Liquid object completely, but for large-scale production, solid particle after Separation of Solid and Liquid to be shifted out from funnel and waste time and energy very much, its labor productivity is lower, affects Catalyst Production production capacity.For the process of drying, if adopt baking oven to dry, not only can cause the bonding between catalyst particle, and catalyst uneven drying can be caused, adopt manpower transport to pass in and out baking oven simultaneously, cause labor productivity lower equally.
In view of above reason, the utility model improves above production process, selects the production equipment that can reach above effect, not only increases labor productivity, and eliminates the mutual bonding between catalyst particle.
Summary of the invention
The purpose of this utility model is to provide a kind of manufacturing system for the production of loaded catalyst.This technology is for the production of microspheric beaded catalyst.
Main technical schemes of the present invention: the production system of loaded catalyst, is characterized in that it comprises reactor, and reactor connects equipment for separating liquid from solid, and equipment for separating liquid from solid connects Vibrating funnel by device for transporting objects, and Vibrating funnel connects vibrated fluidized bed.
Usually, described equipment for separating liquid from solid adopts centrifuge.
Described device for transporting objects is undertaken by electric block.
The funnel both sides of described Vibrating funnel are provided with vibrating motor.
Install a screen cloth in the funnel of described Vibrating funnel, mesh size can be selected according to catalyst particle size.
Production system of the present invention is mainly for the preparation of microspheric beaded catalyst.
Production system of the present invention is run like this: joined in the reactor that carrier is housed by the solution containing catalyst activity component and flood; After having flooded, carry out Separation of Solid and Liquid, the solid obtained is carried out washing and obtains material; Then transport material in Vibrating funnel, joined in vibrated fluidized bed by funnel and carry out drying, finally obtain finished catalyst.
The present invention not only increases labor productivity, and eliminates the mutual bonding between catalyst particle.
Accompanying drawing explanation
Fig. 1 is the connection diagram of embodiment of the present invention production system.
Fig. 2 is Vibrating funnel structural representation in embodiment.
In figure, 1-reactor; 2-solid material; 3-centrifuge; 4-vibrated fluidized bed; 5-Vibrating funnel; 6-electric block; 7-vibrating motor; 8-screen cloth.
Detailed description of the invention
Be described in detail below by drawings and Examples.
Following examples are see attached Fig. 1 and 2, and production system mainly comprises reactor 1, and reactor 1 connects equipment for separating liquid from solid, and equipment for separating liquid from solid connects Vibrating funnel 5 by device for transporting objects, and Vibrating funnel 5 connects vibrated fluidized bed 4.
In embodiment, equipment for separating liquid from solid adopts centrifuge 3 to carry out centrifugation; Device for transporting objects carries out the conveying of solid material 2 by electric block 6; The funnel both sides of Vibrating funnel 5 are provided with vibrating motor 7, and install a screen cloth 8 in the funnel of Vibrating funnel 5, screen cloth 8 aperture catalyst particle size is selected.
Embodiment is for the preparation of microspheric beaded catalyst, the certain density solution containing catalyst activity component is excessively joined in the reactor having added good vector and floods, after having flooded, solid-liquid is passed through Action of Gravity Field, put into centrifugal separator together and carry out Separation of Solid and Liquid and washing, the charging hopper then transporting material to the present embodiment by electric block join vibrated fluidized bed carry out high temperature drying and finished catalyst.
Embodiment 1
The certain density solution containing catalyst activity component is excessively joined in the reactor having added good vector and floods, after having flooded, solid-liquid is put into together centrifugal separator and carry out Separation of Solid and Liquid, be separated and about need about 5 minutes, its active component content of isolated mother liquor is lower, recoverable, then is hung out by the solids after being separated, its water content of isolated solids is 40% by analysis, proves that the method by centrifugation can reach the object of Separation of Solid and Liquid thus.
Embodiment 2
Solids after centrifugation is joined in the charging hopper with vibrating device, solids enters vibrated fluidized bed from charging hopper, regulate the vibration frequency of vibrated fluidized bed, control the load volume by vibrated fluidized bed, regulate carrier gas temperature by the mode of heating, solids can be dried after vibrated fluidized bed simultaneously.Through water content analysis, its water content is 2% ~ 5%.
The production process of embodiment is without the need to a dead lift material, and labour intensity is low, constant product quality.
Claims (6)
1. a production system for loaded catalyst, is characterized in that it comprises reactor, and reactor connects equipment for separating liquid from solid, and equipment for separating liquid from solid connects Vibrating funnel by device for transporting objects, and Vibrating funnel connects vibrated fluidized bed.
2. production system as claimed in claim 1, is characterized in that described equipment for separating liquid from solid adopts centrifuge.
3. production system as claimed in claim 1, is characterized in that described device for transporting objects is undertaken by electric block.
4. production system as claimed in claim 1, is characterized in that the funnel both sides of described Vibrating funnel are provided with vibrating motor.
5. the production system as described in claim 1 or 4, it is characterized in that the funnel of described Vibrating funnel is interior and install a screen cloth, mesh size is selected according to catalyst particle size.
6. production system as claimed in claim 1, is characterized in that for the preparation of microspheric beaded catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520387408.9U CN204841633U (en) | 2015-06-08 | 2015-06-08 | Production system of load type catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520387408.9U CN204841633U (en) | 2015-06-08 | 2015-06-08 | Production system of load type catalyst |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204841633U true CN204841633U (en) | 2015-12-09 |
Family
ID=54732231
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520387408.9U Active CN204841633U (en) | 2015-06-08 | 2015-06-08 | Production system of load type catalyst |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204841633U (en) |
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2015
- 2015-06-08 CN CN201520387408.9U patent/CN204841633U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Liuhe District of Nanjing City, Jiangsu province 210048 geguan Road No. 699 Patentee after: China Petroleum & Chemical Corp. Patentee after: SINOPEC NANJING CHEMICAL RESEARCH INSTITUTE Co.,Ltd. Address before: Liuhe District of Nanjing City, Jiangsu province 210048 geguan Road No. 699 Patentee before: China Petroleum & Chemical Corp. Patentee before: Nanhua Group Research Institute |