PL439237A1 - Method of thermocatalytic oxidation and desulfurization of sulfur-containing organic compounds, especially waste products - Google Patents
Method of thermocatalytic oxidation and desulfurization of sulfur-containing organic compounds, especially waste productsInfo
- Publication number
- PL439237A1 PL439237A1 PL439237A PL43923721A PL439237A1 PL 439237 A1 PL439237 A1 PL 439237A1 PL 439237 A PL439237 A PL 439237A PL 43923721 A PL43923721 A PL 43923721A PL 439237 A1 PL439237 A1 PL 439237A1
- Authority
- PL
- Poland
- Prior art keywords
- oxidation
- sulfur
- organic compounds
- containing organic
- flow rate
- Prior art date
Links
- 238000007254 oxidation reaction Methods 0.000 title abstract 8
- 230000003647 oxidation Effects 0.000 title abstract 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title abstract 5
- 150000002894 organic compounds Chemical class 0.000 title abstract 5
- 229910052717 sulfur Inorganic materials 0.000 title abstract 5
- 239000011593 sulfur Substances 0.000 title abstract 5
- 238000000034 method Methods 0.000 title abstract 4
- 239000002699 waste material Substances 0.000 title abstract 2
- 238000006477 desulfuration reaction Methods 0.000 title 1
- 230000023556 desulfurization Effects 0.000 title 1
- 239000003054 catalyst Substances 0.000 abstract 2
- 239000002253 acid Substances 0.000 abstract 1
- 239000007809 chemical reaction catalyst Substances 0.000 abstract 1
- TVZPLCNGKSPOJA-UHFFFAOYSA-N copper zinc Chemical compound [Cu].[Zn] TVZPLCNGKSPOJA-UHFFFAOYSA-N 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 230000003472 neutralizing effect Effects 0.000 abstract 1
- 239000011541 reaction mixture Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 239000000758 substrate Substances 0.000 abstract 1
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
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
-
- 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
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
-
- 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
- B01J23/005—Spinels
-
- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/80—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with zinc, cadmium or mercury
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Przedmiotem zgłoszenia jest sposób termokatalitycznego utleniania i odsiarczania związków organicznych zawierających siarkę, zwłaszcza stanowiących produkty odpadowe, polegający na poddaniu ich w stanie gazowym utlenieniu powietrzem w reaktorze przepływowym w obecności katalizatora kontaktowego reakcji utleniania, który polega na tym, że związki organiczne zawierające siarkę, stanowiące substancje ciekłe i stałe przed procesem utleniania przeprowadza się najpierw w reaktorze wstępnym w stan gazowy, przy czym związki organiczne zawierające siarkę, w stanie gazowym poddaje się w reaktorze przepływowym całkowitemu utlenieniu powietrzem na katalizatorze miedziowo-cynkowym w temperaturze 350 - 600°C, przy stosunku objętościowego natężenia przepływu powietrza użytego w procesie do objętościowego natężenia przepływu powietrza teoretycznie niezbędnego do całkowitego utlenienia substratu równym co najmniej 1,1, przy stosunku objętościowego natężenia przepływu mieszaniny reakcyjnej do objętości katalizatora równym 360 — 360000 h<sup>-1</sup>. Siarkę zaadsorbowaną na katalizatorze usuwa się w postaci jej tlenków, produkt całkowitego utlenienia związku organicznego odprowadza się do środowiska po zneutralizowaniu kwaśnych składników.The subject of the application is a method of thermocatalytic oxidation and desulphurization of sulfur-containing organic compounds, especially those that are waste products, consisting in subjecting them in a gaseous state to air oxidation in a flow reactor in the presence of a contact oxidation reaction catalyst, in which sulfur-containing organic compounds that are substances liquid and solid before the oxidation process are first converted into a gaseous state in a pre-reactor, while sulfur-containing organic compounds in a gaseous state are subjected to complete oxidation in a flow reactor with air on a copper-zinc catalyst at a temperature of 350 - 600 ° C, at a volume ratio the air flow rate used in the process to the volumetric air flow rate theoretically necessary for complete oxidation of the substrate of at least 1.1, with a reaction mixture volumetric flow rate of 360 - 360000 h<sup>-1</sup>. Sulfur adsorbed on the catalyst is removed in the form of its oxides, the product of complete oxidation of the organic compound is discharged into the environment after neutralizing the acid components.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL439237A PL245558B1 (en) | 2021-10-18 | 2021-10-18 | Method of thermocatalytic oxidation and desulfurization of sulfur-containing organic compounds, especially waste products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL439237A PL245558B1 (en) | 2021-10-18 | 2021-10-18 | Method of thermocatalytic oxidation and desulfurization of sulfur-containing organic compounds, especially waste products |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL439237A1 true PL439237A1 (en) | 2023-04-24 |
| PL245558B1 PL245558B1 (en) | 2024-09-02 |
Family
ID=86184105
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL439237A PL245558B1 (en) | 2021-10-18 | 2021-10-18 | Method of thermocatalytic oxidation and desulfurization of sulfur-containing organic compounds, especially waste products |
Country Status (1)
| Country | Link |
|---|---|
| PL (1) | PL245558B1 (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9663725B2 (en) * | 2011-07-27 | 2017-05-30 | Saudi Arabian Oil Company | Catalytic compositions useful in removal of sulfur compounds from gaseous hydrocarbons, processes for making these and uses thereof |
| US8920635B2 (en) * | 2013-01-14 | 2014-12-30 | Saudi Arabian Oil Company | Targeted desulfurization process and apparatus integrating gas phase oxidative desulfurization and hydrodesulfurization to produce diesel fuel having an ultra-low level of organosulfur compounds |
| CN109012678A (en) * | 2018-08-27 | 2018-12-18 | 鲁西催化剂有限公司 | A kind of high dispersive desulphurization catalyst preparation method |
-
2021
- 2021-10-18 PL PL439237A patent/PL245558B1/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| PL245558B1 (en) | 2024-09-02 |
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