GB487785A - Process and apparatus for the catalytic treatment of hydrocarbons and the regeneration of the catalyst used therein - Google Patents
Process and apparatus for the catalytic treatment of hydrocarbons and the regeneration of the catalyst used thereinInfo
- Publication number
- GB487785A GB487785A GB35272/36A GB3527236A GB487785A GB 487785 A GB487785 A GB 487785A GB 35272/36 A GB35272/36 A GB 35272/36A GB 3527236 A GB3527236 A GB 3527236A GB 487785 A GB487785 A GB 487785A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- regeneration
- passed
- converter
- hydrocarbons
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/10—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16K—VALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
- F16K17/00—Safety valves; Equalising valves, e.g. pressure relief valves
- F16K17/02—Safety valves; Equalising valves, e.g. pressure relief valves opening on surplus pressure on one side; closing on insufficient pressure on one side
- F16K17/04—Safety valves; Equalising valves, e.g. pressure relief valves opening on surplus pressure on one side; closing on insufficient pressure on one side spring-loaded
- F16K17/10—Safety valves; Equalising valves, e.g. pressure relief valves opening on surplus pressure on one side; closing on insufficient pressure on one side spring-loaded with auxiliary valve for fluid operation of the main valve
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Catalysts (AREA)
Abstract
<PICT:0487785/III/1> Catalysts which have become contaminated with carbon &c. in the catalytic treatment of hydrocarbons are regnerated by means of an oxygen-containing gas under superatmospheric pressure, e.g. of 40-100 lb. per sq. in. absolute pressure. The oxygen content of the gas may be regulated to control the temperature of the regeneration. A suitable gas may be obtained by the combustion in a chamber 8 of fuel and air supplied under pressure by pumps 9, 11 respectively, further air being optionally added to the combustion products at 13. The gas is passed through the catalyst chamber 1 which may be provided with heating or cooling means (not shown), e.g. as described in Specification 471,931. The products may be mixed with more air by pipe 15 and passed to a catalyst chamber 6 wherein carbon monoxide is oxidized to dioxide. The energy of the resulting gas may be utilized in a turbine or steam boiler 16 to supply, e.g. by means of an electric generator 18 and motor 19, the motive power for compressing the initial gas. In a modification, a part of the gas leaving the converter 1 is passed through a heat-exchanger and recycled through the converter. In another modification, the single converter 1 is replaced by a battery of converters which are placed on stream and on regeneration in sequence. The catalyst to be regenerated may be of the type described in Specification 416,025.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US487785XA | 1916-03-31 | 1916-03-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB487785A true GB487785A (en) | 1938-06-23 |
Family
ID=21956398
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB35272/36A Expired GB487785A (en) | 1936-01-13 | 1936-12-23 | Process and apparatus for the catalytic treatment of hydrocarbons and the regeneration of the catalyst used therein |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR487785A (en) |
GB (1) | GB487785A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2421381A (en) * | 1942-07-03 | 1947-06-03 | Linde Air Prod Co | Chemical production of oxygen |
-
1917
- 1917-02-03 FR FR487785D patent/FR487785A/en not_active Expired
-
1936
- 1936-12-23 GB GB35272/36A patent/GB487785A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2421381A (en) * | 1942-07-03 | 1947-06-03 | Linde Air Prod Co | Chemical production of oxygen |
Also Published As
Publication number | Publication date |
---|---|
FR487785A (en) | 1918-07-24 |
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