FR2381095A2 - Continuous catalytic conversion of hydrocarbon feed - with redn. and sulphiding of regenerated catalyst in zones sepd. from reactor (NL 24.7.78) - Google Patents
Continuous catalytic conversion of hydrocarbon feed - with redn. and sulphiding of regenerated catalyst in zones sepd. from reactor (NL 24.7.78)Info
- Publication number
- FR2381095A2 FR2381095A2 FR7704868A FR7704868A FR2381095A2 FR 2381095 A2 FR2381095 A2 FR 2381095A2 FR 7704868 A FR7704868 A FR 7704868A FR 7704868 A FR7704868 A FR 7704868A FR 2381095 A2 FR2381095 A2 FR 2381095A2
- Authority
- FR
- France
- Prior art keywords
- zone
- redn
- reaction
- sulphiding
- catalyst
- 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.)
- Granted
Links
Classifications
-
- 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/10—Catalytic reforming with moving catalysts
- C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
In the continuous conversion of hydrocarbons in presence of a catalyst, a feed charge consisting of hydrocarbons and H2 is circulated through >=1 reaction zone of the moving bed type. The catalyst flows progressively downwards through this zone, is removed from the bottom part of the zone, and is fed to a regeneration zone. The regenerated catalyst is led through a redn. zone, at 480-530 degrees C which is charged with H2 and which is heated by a part of the charge or by the reaction effluent. The regenerated and reduced catalyst is passed from the redn. zone to the upper part of the reaction zone through several pipes which form a sulphurisation zone, separate from the redn. zone and the reaction zone, and the catalyst circulates as a mobile bed and is sulphided at a temp. below the temp. of redn. and reaction ie. at 300-400 degrees C (310-380 degrees C) by means of a gas contg. a S cpd. The temps. of sulphiding and redn. are lower than the reaction temp. and are easily controlled; sulphiding and redn. zones are heated independently of the first reactor. The redn. and sulphiding zones are sepd. from the reaction zone, thus reducing the danger of explosion, e.g. an explosion in the redn. zone is less likely to reach the reaction zone than in known processes.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7704868A FR2381095A2 (en) | 1977-02-17 | 1977-02-17 | Continuous catalytic conversion of hydrocarbon feed - with redn. and sulphiding of regenerated catalyst in zones sepd. from reactor (NL 24.7.78) |
DE19782801841 DE2801841A1 (en) | 1977-01-20 | 1978-01-17 | Continuous catalytic conversion of hydrocarbon feed - with redn. and sulphiding of regenerated catalyst in zones sepd. from reactor (NL 24.7.78) |
NL7800622A NL7800622A (en) | 1977-01-20 | 1978-01-18 | METHOD FOR CONVERTING HYDROCARBONS WITH HYDROGEN. |
JP53005716A JPS6039110B2 (en) | 1977-01-20 | 1978-01-20 | Continuous conversion method for hydrocarbons |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7704868A FR2381095A2 (en) | 1977-02-17 | 1977-02-17 | Continuous catalytic conversion of hydrocarbon feed - with redn. and sulphiding of regenerated catalyst in zones sepd. from reactor (NL 24.7.78) |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2381095A2 true FR2381095A2 (en) | 1978-09-15 |
FR2381095B2 FR2381095B2 (en) | 1983-04-15 |
Family
ID=9186985
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7704868A Granted FR2381095A2 (en) | 1977-01-20 | 1977-02-17 | Continuous catalytic conversion of hydrocarbon feed - with redn. and sulphiding of regenerated catalyst in zones sepd. from reactor (NL 24.7.78) |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR2381095A2 (en) |
-
1977
- 1977-02-17 FR FR7704868A patent/FR2381095A2/en active Granted
Also Published As
Publication number | Publication date |
---|---|
FR2381095B2 (en) | 1983-04-15 |
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