BE766150A - Petroleum coke desulphurised demetallisedwith synthesis gas - Google Patents
Petroleum coke desulphurised demetallisedwith synthesis gasInfo
- Publication number
- BE766150A BE766150A BE766150A BE766150A BE766150A BE 766150 A BE766150 A BE 766150A BE 766150 A BE766150 A BE 766150A BE 766150 A BE766150 A BE 766150A BE 766150 A BE766150 A BE 766150A
- Authority
- BE
- Belgium
- Prior art keywords
- coke
- synthesis gas
- degrees
- effluent
- demetallisedwith
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/02—Treating solid fuels to improve their combustion by chemical means
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Industrial Gases (AREA)
Abstract
Petroleum coke of high sulphur content and contaminated with metals is purified and calcined to form metallurgical grade coke by (1) pre-oxidising the coke at 650-850 degrees F to increase its surface area., (2) hydrosulphurising the coke with synthesis gas at 1300 degrees F or above, and (3) demetallising the coke by contact at 275-430 degrees F and elevated pressure with the H2S-containing synthesis gas effluent from the hydrodesulphurisation step to form gaseous carbonyls of the metals, the H2S functioning as catalyst. The synthesis gas required is suitably generated by gasifying a portion of the coke with O2 and steam. The H2S- containing effluent from the desulphurisation step is pref. used to preheat the coke before the effluent is used in the carbonylation of the metal impurities.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE766150A BE766150A (en) | 1971-04-22 | 1971-04-22 | Petroleum coke desulphurised demetallisedwith synthesis gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE766150A BE766150A (en) | 1971-04-22 | 1971-04-22 | Petroleum coke desulphurised demetallisedwith synthesis gas |
Publications (1)
Publication Number | Publication Date |
---|---|
BE766150A true BE766150A (en) | 1971-10-22 |
Family
ID=3858029
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BE766150A BE766150A (en) | 1971-04-22 | 1971-04-22 | Petroleum coke desulphurised demetallisedwith synthesis gas |
Country Status (1)
Country | Link |
---|---|
BE (1) | BE766150A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114456825A (en) * | 2022-03-10 | 2022-05-10 | 山东联星能源集团有限公司 | Petroleum coke desulfurization method |
-
1971
- 1971-04-22 BE BE766150A patent/BE766150A/en unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114456825A (en) * | 2022-03-10 | 2022-05-10 | 山东联星能源集团有限公司 | Petroleum coke desulfurization method |
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