PL447712A1 - Method of purifying air from volatile organic compounds using a fluidized bed reactor - Google Patents
Method of purifying air from volatile organic compounds using a fluidized bed reactorInfo
- Publication number
- PL447712A1 PL447712A1 PL447712A PL44771224A PL447712A1 PL 447712 A1 PL447712 A1 PL 447712A1 PL 447712 A PL447712 A PL 447712A PL 44771224 A PL44771224 A PL 44771224A PL 447712 A1 PL447712 A1 PL 447712A1
- Authority
- PL
- Poland
- Prior art keywords
- fluidized bed
- organic compounds
- volatile organic
- bed reactor
- purifying air
- Prior art date
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/60—Platinum group metals with zinc, cadmium or mercury
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/51—Spheres
- B01J35/53—Spheres with a core-shell structure
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Przedmiotem zgłoszenia jest sposób oczyszczania powietrza z lotnych związków organicznych (LZO), polegający na tym, że powietrze zanieczyszczone LZO podaje się do przepływowego reaktora fluidalnego, charakteryzujący się tym, że złoże fluidalne w reaktorze stanowi układ cenosfer o nienaruszonych, niepołamanych ściankach, o wielkości ziaren od 100 do 160 µm, pokrytych warstwą katalityczną nanocząstek platyny w matrycy z tlenku cynku (układ Pt/ZnO/Cenosfery), w którym zawartość nanocząstek platyny wynosi co najmniej 0,5%o w odniesieniu do masy początkowej cenosfer. Rozmiary nanocząstek platyny, osadzone na matrycy ZnO/cenosfery są nie większe niż 20 nm. Natomiast powietrze podgrzewa się do temperatury od 200°C do 500°C, a jego przepływ prowadzi się w zakresie prędkości liniowej strumienia gazowego 0,3 do 0,8 cm/s. Z kolei stosunek średnicy do wysokości złoża fluidalnego wynosi od 2/1 do 1/8.The subject of the application is a method for purifying air from volatile organic compounds (VOCs), which involves feeding VOC-contaminated air into a fluidized bed reactor, characterized in that the fluidized bed in the reactor is a system of cenospheres with intact, unbroken walls, with a grain size of 100 to 160 µm, coated with a catalytic layer of platinum nanoparticles in a zinc oxide matrix (Pt/ZnO/Cenosphere system), wherein the platinum nanoparticle content is at least 0.5% based on the initial mass of the cenospheres. The size of the platinum nanoparticles deposited on the ZnO/cenosphere matrix is no larger than 20 nm. The air is heated to a temperature of 200°C to 500°C, and its flow is conducted within the linear gas stream velocity range of 0.3 to 0.8 cm/s. In turn, the ratio of the diameter to the height of the fluidized bed is from 2/1 to 1/8.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL447712A PL248435B1 (en) | 2024-02-07 | 2024-02-07 | Method of purifying air from volatile organic compounds using a fluidized bed reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL447712A PL248435B1 (en) | 2024-02-07 | 2024-02-07 | Method of purifying air from volatile organic compounds using a fluidized bed reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL447712A1 true PL447712A1 (en) | 2025-08-11 |
| PL248435B1 PL248435B1 (en) | 2025-12-15 |
Family
ID=96658329
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL447712A PL248435B1 (en) | 2024-02-07 | 2024-02-07 | Method of purifying air from volatile organic compounds using a fluidized bed reactor |
Country Status (1)
| Country | Link |
|---|---|
| PL (1) | PL248435B1 (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100196213A1 (en) * | 2007-06-04 | 2010-08-05 | Ceca S.A. | Spherical agglomerates based on zeolite(s), process for the production thereof and use thereof in adsorption processes or in catalysis |
| CN104906946A (en) * | 2015-04-29 | 2015-09-16 | 南京工业大学 | A kind of preparation method of catalytic membrane for gas purification |
| CN107626307A (en) * | 2017-09-29 | 2018-01-26 | 北京工业大学 | A kind of method of ZnO doping regulation and control Pt base catalyst oxidation activities |
| CN114786813A (en) * | 2019-12-20 | 2022-07-22 | 阿克森斯公司 | Catalyst support comprising hollow microspheres |
| CN116532113A (en) * | 2023-05-08 | 2023-08-04 | 中国矿业大学 | Preparation and application of carbon bridging atom dispersed Pt in MOF-derived ZnO/C catalyst |
-
2024
- 2024-02-07 PL PL447712A patent/PL248435B1/en unknown
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100196213A1 (en) * | 2007-06-04 | 2010-08-05 | Ceca S.A. | Spherical agglomerates based on zeolite(s), process for the production thereof and use thereof in adsorption processes or in catalysis |
| CN104906946A (en) * | 2015-04-29 | 2015-09-16 | 南京工业大学 | A kind of preparation method of catalytic membrane for gas purification |
| CN107626307A (en) * | 2017-09-29 | 2018-01-26 | 北京工业大学 | A kind of method of ZnO doping regulation and control Pt base catalyst oxidation activities |
| CN114786813A (en) * | 2019-12-20 | 2022-07-22 | 阿克森斯公司 | Catalyst support comprising hollow microspheres |
| CN116532113A (en) * | 2023-05-08 | 2023-08-04 | 中国矿业大学 | Preparation and application of carbon bridging atom dispersed Pt in MOF-derived ZnO/C catalyst |
Also Published As
| Publication number | Publication date |
|---|---|
| PL248435B1 (en) | 2025-12-15 |
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