CN213425021U - Automatic production line for platinum-carbon catalyst - Google Patents
Automatic production line for platinum-carbon catalyst Download PDFInfo
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- CN213425021U CN213425021U CN202022316472.1U CN202022316472U CN213425021U CN 213425021 U CN213425021 U CN 213425021U CN 202022316472 U CN202022316472 U CN 202022316472U CN 213425021 U CN213425021 U CN 213425021U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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Abstract
The utility model provides an automatic production line of platinum-carbon catalyst, wherein a pure water preparation chamber, a liquid distribution chamber, a stock solution chamber and a carbon powder treatment chamber are arranged in a third building, and a carbon powder treatment tank and an ultrasonic crusher are arranged in the carbon powder treatment chamber; the premixing chamber, the ultrasonic chamber and the at least one mixing reaction kettle are arranged on a second floor, a first premixing groove is arranged in the premixing chamber, a second premixing groove is arranged in the ultrasonic chamber, and a premixing groove placing area and an auxiliary material placing platform are arranged on the second floor close to the mixing reaction kettle; at least one sedimentation cleaning tank and a freeze drying chamber are arranged on the first floor; a platinum precursor compound preparation pool, an auxiliary inorganic salt compound preparation pool and a complexing agent storage pool which are arranged in the stock solution chamber are respectively communicated with the first premixing tank, a carbon powder treatment pool is communicated with the second premixing tank, and a discharge port of at least one mixing reaction kettle is communicated with at least one precipitation cleaning pool in a one-to-one correspondence manner. The utility model discloses structural arrangement is reasonable, compact, convenient automatic assembly line control.
Description
Technical Field
The utility model relates to a platinum carbon catalyst automatic production line.
Background
The catalyst is a key material of a fuel cell, and is usually a platinum carbon catalyst, while the platinum carbon catalyst is prepared by a plurality of methods, different production lines are adopted by different preparation methods, and the arrangement pattern of the production lines is different.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a platinum carbon catalyst automatic production line that structural arrangement is reasonable, compact, convenient automatic assembly line control.
The utility model discloses a following scheme realizes:
an automatic production line for platinum-carbon catalysts comprises a pure water preparation chamber, a liquid preparation chamber, a stock solution chamber, a carbon powder treatment chamber, a premixing chamber, an ultrasonic chamber, at least one mixing reaction kettle, at least one precipitation cleaning pool and a freeze drying chamber, wherein the pure water preparation chamber, the liquid preparation chamber, the stock solution chamber and the carbon powder treatment chamber are arranged in a third floor, a platinum precursor compound preparation pool and an auxiliary inorganic salt compound preparation pool are arranged in the liquid preparation chamber, a complexing agent storage pool is arranged in the stock solution chamber, and a carbon powder treatment pool and an ultrasonic crusher are arranged in the carbon powder treatment chamber; the premixing chamber, the ultrasonic chamber and the at least one mixing reaction kettle are arranged on a second floor, the at least one mixing reaction kettle is arranged together side by side, a first premixing groove is arranged in the premixing chamber, a second premixing groove is arranged in the ultrasonic chamber, and a premixing groove placing area and an auxiliary material placing platform are arranged on the position, close to the mixing reaction kettle, of the second floor; at least one sedimentation cleaning tank and a freeze drying chamber are arranged on the first floor; the pure water preparation chamber respectively provides pure water for a platinum precursor compound preparation pool and an auxiliary inorganic salt compound preparation pool of the liquid preparation chamber, a complexing agent storage pool of the stock solution chamber and a carbon powder treatment pool of the carbon powder treatment chamber, the platinum precursor compound preparation pool, the auxiliary inorganic salt compound preparation pool and the complexing agent storage pool are respectively communicated with the first premixing tank, the carbon powder treatment tank is communicated with the second premixing tank, the mixed materials in the first premixing tank are provided for the second premixing tank, the mixed materials in the second premixing tank are provided for the mixing reaction kettle, the discharge hole of at least one mixing reaction kettle is communicated with at least one sedimentation cleaning tank in a one-to-one correspondence manner, the precipitation cleaning pool is used for carrying out precipitation cleaning treatment on the turbid liquid flowing out of the mixing reaction kettle to obtain a wet product and providing the obtained wet product to the freeze drying chamber, and the freeze drying chamber is used for carrying out drying treatment on the wet product to obtain a final product. The first premixing tank is used for premixing materials in the platinum precursor compound preparation tank, the auxiliary inorganic salt compound preparation tank and the complexing agent storage tank in proportion, the second premixing tank is used for premixing the uniformly mixed materials in the first premixing tank and the materials in the carbon powder treatment tank in proportion, and the mixing reaction kettle is used for uniformly mixing and reacting the materials in the second premixing tank and the materials on the auxiliary material placement platform in proportion.
Further, the first floor is provided with a dose packing room and a warehouse, and the dose packing room is used for subpackaging final products according to dose requirements.
Further, the first floor is provided with a detection chamber, and the detection chamber is used for detecting whether the final product meets the requirements.
Further, a monitoring chamber is arranged on the first floor, and the monitoring chamber is used for monitoring the liquid levels and the flow rates of the platinum precursor compound preparation pool, the auxiliary inorganic salt compound preparation pool and the carbon powder treatment pool, and is used for monitoring the liquid levels, the flow rates and the temperatures of the complexing agent storage pool and the mixing reaction kettle.
Further, a first annular conveying belt is arranged in the carbon powder processing chamber and used for conveying carbon powder into the carbon powder processing pool; and a second annular conveyer belt is arranged on the second floor and used for conveying the second premixing tank with mixed materials to the premixing tank placing area and correspondingly conveying the empty second premixing tank back to the premixing chamber and the ultrasonic chamber.
In practice, when a production line is arranged, specific arrangement positions of a pure water preparation chamber, a liquid preparation chamber, a stock solution chamber, a carbon powder treatment chamber, a premixing chamber, an ultrasonic chamber, at least one mixing reaction kettle, a precipitation cleaning tank, a freeze drying chamber, a dose packaging chamber, a warehouse, a detection chamber and a monitoring chamber can be determined according to specific conditions, and the arrangement is carried out on the basis of the compact arrangement and convenient automatic production line production.
The utility model discloses a platinum carbon catalyst automatic production line, structural arrangement is reasonable, compact, utilizes the gravity effect, and the energy saving makes things convenient for automatic assembly line control, improves production efficiency.
Drawings
FIG. 1 is a block diagram showing the arrangement of an automatic production line for a platinum-carbon catalyst in example 1.
Detailed Description
The embodiment is only for illustrating one implementation of the present invention, and is not to be taken as a limiting illustration of the protection scope of the present invention.
Example 1
An automatic production line for platinum-carbon catalysts is shown in figure 1 and comprises a pure water preparation chamber 1, a liquid preparation chamber 2, a raw liquid chamber 3, a carbon powder treatment chamber 4, a premixing chamber 5, an ultrasonic chamber 6, two mixing reaction kettles 7, two precipitation cleaning tanks 8, a freeze drying chamber 9, a detection chamber 10, a dose packaging chamber 11, a warehouse 12 and a monitoring chamber 13, wherein the pure water preparation chamber 1, the liquid preparation chamber 2, the raw liquid chamber 3 and the carbon powder treatment chamber 4 are sequentially arranged in a third floor from left to right, a platinum precursor compound preparation tank 14 and an auxiliary inorganic salt compound preparation tank 15 are arranged in the liquid preparation chamber 2, a complexing agent storage tank 16 is arranged in the raw liquid chamber 3, a carbon powder treatment tank 17, an ultrasonic crusher 18 and a first annular conveying belt 19 are arranged in the carbon powder treatment chamber 4, and the first annular conveying belt 19 is used for conveying carbon powder into the carbon powder treatment tank; the premixing chamber 5, the ultrasonic chamber 6 and the two mixing reaction kettles 7 are sequentially arranged on a second floor from left to right, the two mixing reaction kettles 7 are arranged side by side, a premixing tank placing area 20 and an auxiliary material placing platform 21 are arranged on the position, close to the mixing reaction kettles 7, of the second floor, a first premixing tank 22 is arranged in the premixing chamber 5, a second premixing tank 23 is arranged in the ultrasonic chamber 6, a second annular conveyer belt 24 is arranged on the second floor, the second annular conveyer belt 24 is used for conveying the second premixing tank 23 with mixed materials to the premixing tank placing area 20, and the empty second premixing tank 23 is correspondingly conveyed back to the premixing chamber 5 and the ultrasonic chamber 6; the two sedimentation cleaning tanks 8 are arranged at the first floor and are positioned right below the two mixing reaction kettles 7, the discharge ports of the two mixing reaction kettles 7 are correspondingly communicated with the two sedimentation cleaning tanks 8 one by one, and the freeze drying chamber 9, the detection chamber 10, the dose packaging chamber 11, the warehouse 12 and the monitoring chamber 13 are sequentially arranged at the first floor from left to right; the pure water preparation chamber 1 respectively provides pure water for a platinum precursor compound preparation pool 14 and an auxiliary inorganic salt compound preparation pool 15 of the liquid preparation chamber 2, a complexing agent storage pool 16 of the stock solution chamber 3 and a carbon powder treatment pool 17 of the carbon powder treatment chamber 4, the platinum precursor compound preparation pool 14, the auxiliary inorganic salt compound preparation pool 15 and the complexing agent storage pool 16 are respectively communicated with a first premixing tank 22, the carbon powder treatment pool 17 is communicated with a second premixing tank 23, the mixed material in the first premixing tank 22 is provided for the second premixing tank 23, the mixed material in the second premixing tank 23 is provided for the mixing reaction kettle 7, the precipitation cleaning pool 8 is used for carrying out precipitation cleaning treatment on the turbid liquid flowing out from the mixing reaction kettle 7 to obtain a wet product and providing the obtained wet product to the freeze drying chamber 9, the freeze drying chamber 9 is used for carrying out drying treatment on the wet product to obtain a final product, the detection chamber 10 is used for detecting whether the final product meets the requirement or not, and the dose packaging chamber 11 is used for subpackaging the final product according to the dose requirement; the monitoring chamber 13 is used for monitoring the liquid levels and the flow rates of the platinum precursor compound preparation tank 14, the auxiliary inorganic salt compound preparation tank 15 and the carbon powder treatment tank 17, and for monitoring the liquid levels, the flow rates and the temperatures of the complexing agent storage tank 16 and the mixing reaction kettle 7.
During production, a platinum precursor compound and an auxiliary inorganic salt compound specified in the platinum-carbon catalyst preparation process are respectively prepared in a platinum precursor compound preparation pool and an auxiliary inorganic salt compound preparation pool in a solution preparation chamber according to the proportion requirement, a complexing agent specified in the platinum-carbon catalyst preparation process is placed in a complexing agent storage pool in a stock solution chamber, carbon powder specified in the platinum-carbon catalyst preparation process is placed in a carbon powder treatment pool according to the proportion and is dispersed by an ultrasonic crusher, then materials in the platinum precursor compound preparation pool, the auxiliary inorganic salt compound preparation pool and the complexing agent storage pool respectively flow into a first premixing tank of a premixing chamber according to the proportion for premixing, the materials in the carbon powder treatment pool and the uniformly mixed materials in the first premixing tank flow into a second premixing tank in an ultrasonic chamber according to the proportion for premixing, and then the second premixing tank of the premixed materials is conveyed to a premixing tank placing area through a second annular conveying belt, and (2) proportionally filling the materials in the second premixing tank and the materials (generally reducing agent compounds) on the auxiliary material placing platform into a mixing reaction kettle through a pipeline for treatment, then flowing the turbid liquid treated by the mixing reaction kettle into a precipitation cleaning pool, obtaining wet products after precipitation cleaning, conveying the wet products into a freeze drying chamber for drying treatment to obtain final products, detecting the final products, conveying the final products into a dose packaging chamber after the final products are detected to be qualified, subpackaging the final products in the dose packaging chamber according to the dose requirement, and conveying the subpackaged products into a warehouse for storage. In the whole production process, the monitoring chamber monitors the liquid levels and the flow rates of the platinum precursor compound preparation pool, the auxiliary inorganic salt compound preparation pool and the carbon powder treatment pool, and monitors the liquid levels, the flow rates and the temperatures of the complexing agent storage pool and the mixing reaction kettle.
Claims (5)
1. The utility model provides a platinum carbon catalyst automatic production line which characterized in that: the device comprises a pure water preparation chamber, a liquid preparation chamber, a stock solution chamber, a carbon powder treatment chamber, a premixing chamber, an ultrasonic chamber, at least one mixing reaction kettle, at least one precipitation cleaning pool and a freeze drying chamber, wherein the pure water preparation chamber, the liquid preparation chamber, the stock solution chamber and the carbon powder treatment chamber are arranged in a third floor, a platinum precursor compound preparation pool and an auxiliary inorganic salt compound preparation pool are arranged in the liquid preparation chamber, a complexing agent storage pool is arranged in the stock solution chamber, and a carbon powder treatment pool and an ultrasonic crusher are arranged in the carbon powder treatment chamber; the premixing chamber, the ultrasonic chamber and the at least one mixing reaction kettle are arranged on a second floor, the at least one mixing reaction kettle is arranged together side by side, a first premixing groove is arranged in the premixing chamber, a second premixing groove is arranged in the ultrasonic chamber, and a premixing groove placing area and an auxiliary material placing platform are arranged on the position, close to the mixing reaction kettle, of the second floor; at least one sedimentation cleaning tank and a freeze drying chamber are arranged on the first floor; the pure water preparation chamber respectively provides pure water for a platinum precursor compound preparation pool and an auxiliary inorganic salt compound preparation pool of the liquid preparation chamber, a complexing agent storage pool of the stock solution chamber and a carbon powder treatment pool of the carbon powder treatment chamber, the platinum precursor compound preparation pool, the auxiliary inorganic salt compound preparation pool and the complexing agent storage pool are respectively communicated with the first premixing tank, the carbon powder treatment tank is communicated with the second premixing tank, the mixed materials in the first premixing tank are provided for the second premixing tank, the mixed materials in the second premixing tank are provided for the mixing reaction kettle, the discharge hole of at least one mixing reaction kettle is communicated with at least one sedimentation cleaning tank in a one-to-one correspondence manner, the precipitation cleaning pool is used for carrying out precipitation cleaning treatment on the turbid liquid flowing out of the mixing reaction kettle to obtain a wet product and providing the obtained wet product to the freeze drying chamber, and the freeze drying chamber is used for carrying out drying treatment on the wet product to obtain a final product.
2. The platinum-carbon catalyst automatic production line according to claim 1, characterized in that: the first floor is provided with a dose packing room and a warehouse, and the dose packing room is used for subpackaging final products according to dose requirements.
3. The platinum-carbon catalyst automatic production line according to claim 2, characterized in that: the first floor is provided with a detection chamber used for detecting whether a final product meets requirements.
4. The platinum-carbon catalyst automatic production line according to claim 3, characterized in that: the first floor is provided with a monitoring chamber, and the monitoring chamber is used for monitoring the liquid levels and the flow rates of a platinum precursor compound preparation pool, an auxiliary inorganic salt compound preparation pool and a carbon powder treatment pool and monitoring the liquid levels, the flow rates and the temperatures of a complexing agent storage pool and a mixing reaction kettle.
5. The automatic production line of a platinum-carbon catalyst according to any one of claims 1 to 4, characterized in that: a first annular conveying belt is arranged in the carbon powder processing chamber and used for conveying carbon powder into the carbon powder processing tank; and a second annular conveyer belt is arranged on the second floor and used for conveying the second premixing tank with mixed materials to the premixing tank placing area and correspondingly conveying the empty second premixing tank back to the premixing chamber and the ultrasonic chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022316472.1U CN213425021U (en) | 2020-10-19 | 2020-10-19 | Automatic production line for platinum-carbon catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022316472.1U CN213425021U (en) | 2020-10-19 | 2020-10-19 | Automatic production line for platinum-carbon catalyst |
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| CN213425021U true CN213425021U (en) | 2021-06-11 |
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| CN202022316472.1U Active CN213425021U (en) | 2020-10-19 | 2020-10-19 | Automatic production line for platinum-carbon catalyst |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113680392A (en) * | 2021-09-15 | 2021-11-23 | 中耐工程科技有限公司 | Automatic production line for producing catalyst |
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- 2020-10-19 CN CN202022316472.1U patent/CN213425021U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113680392A (en) * | 2021-09-15 | 2021-11-23 | 中耐工程科技有限公司 | Automatic production line for producing catalyst |
| CN113680392B (en) * | 2021-09-15 | 2023-08-01 | 中耐工程科技有限公司 | Automatic production line for producing catalyst |
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