GB711818A - Separation of aromatics from gasoline or kerosene fractions - Google Patents
Separation of aromatics from gasoline or kerosene fractionsInfo
- Publication number
- GB711818A GB711818A GB16952A GB16952A GB711818A GB 711818 A GB711818 A GB 711818A GB 16952 A GB16952 A GB 16952A GB 16952 A GB16952 A GB 16952A GB 711818 A GB711818 A GB 711818A
- Authority
- GB
- United Kingdom
- Prior art keywords
- charge
- desorbent
- silica gel
- aromatics
- aromatic
- 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
- C10G25/00—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
- C07C15/02—Monocyclic hydrocarbons
-
- 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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A cyclic process for separating aromatics from a gasoline or kerosene fraction comprises introducing into a bed of silica gel during each cycle, liquid charge equivalent to 50 to 85 per cent of "equilibrium amount" to adsorb aromatics selectively, displacing adsorbed aromatics by introducing an aromatic hydrocarbon liquid desorbent boiling below 500 DEG F. and outside the range of the charge, in an amount of 0.05 to 0.14 gal./lb. silica gel and sufficient to cause the charge hydrocarbon content of the effluent from the silica gel during each cycle to decrease below 5, preferably below 3, per cent by volume, and directly re-using the wet silica gel to treat further charge in the next cycle. The "equilibrium amount" is the quantity of charge which contains aromatics necessary to saturate 1 lb. silica gel when equilibrium is reached at the operating temperature. Equilibrium curves which relate per cent aromatic in the liquid phase to volume of aromatic apparently adsorbed per lb. silica gel are given for mixtures of toluene or benzene, and n-heptane, and mixtures of aromatics and saturateds from 300 DEG to 400 DEG F. straight-run naphtha. The charge may first be diluted with saturated hydrocarbons, e.g. propane, butane, pentanes or cyclopentane, suitably in a ratio of 4 vols. naphtha: 1 diluent. Curves are given showing how the aromatic recovery falls sharply when the charge exceeds 85 per cent of the "equilibrium amount" for naphtha + isopentane diluent and for a catalytic reformate. The effect of varying the amount of desorbent on the aromatic recovery is also illustrated. The desorbent may be a single aromatic hydrocarbon or a mixture and may boil below or above the charge. For a charge boiling above benzene, benzene is suitable and for a naphtha boiling below xylene, xylene is suitable. In a modification of the process, immediately following the charge and prior to introducing the desorbent, a low boiling saturated p hydrocarbon is introduced in relatively small amount, generally 0.01 to 0.03 gal./lb. silica gel, which results in an improved separation. The effluent from each phase of the cycle, containing saturated and aromatics respectively together with desorbent, is separately fractionated to recover the desired products, the desorbent being recycled. Examples relate to straight-run naphtha with or without isopentane diluent, a catalytic gasoline fraction containing also olefins, and a catalytic reformate, the desorbent being benzene or commercial xylenes, and isopentane being used in one case as the intermediate treating liquid.ALSO:A cyclic process for separating aromatics from a gasoline or kerosene fraction comprises introducing into a bed of silica gel during each cycle, liquid charge equivalent to 50-85 per cent. of "equilibrium amount" to adsorb aromatics selectively, displacing adsorbed aromatics by introducing an aromatic hydrocarbon liquid desorbent boiling below 500 DEG F. and outside the range of the charge, in an amount of .05-.14 gal./lb. silica gel and sufficient to cause the charge hydrocarbon content of the effluent from the silica gel during each cycle to decrease below 5, preferably below 3 per cent. by volume, and directly re-using the wet silica gel to treat further charge in the next cycle. The "equilibrium amount" is the quantity of charge which contains aromatics necessary to saturate 1 lb. silica gel when equilibrium is reached at the operating temperature. Equilibrium curves which relate per cent. aromatic in the liquid phase to volume of aromatic apparently adsorbed per lb. silica gel are given for mixtures of toluene or benzene and n-heptane and mixtures of aromatics and saturateds from a 300-400 DEG F. straight run naphtha. The charge may first be diluted with saturated hydrocarbons, e.g. propane, butane, pentanes or cyclopentane, suitably in a ratio of 4 vols. naphtha: 1 diluent. Curves are given showing how the aromatic recovery falls sharply when the charge exceeds 85 per cent. of the "equilibrium amount" for naphtha + isopentane diluent and for a catalytic reformate. The effect of varying the amount of desorbent on the aromatic recovery is also illustrated. The desorbent may be a single aromatic hydrocarbon or a mixture and may boil below or above the charge. For a charge boiling above benzene, benzene is suitable and for a naphtha boiling below scylene, scylene is suitable. In a modification of the process, immediately following the charge and prior to introducing the desorbent, a low boiling saturated hydrocarbon is introduced in relativity small amount, generally .01-.03 gal./lb. silica gel, which results in an improved separation. The effluent from each phase of the cycle, containing saturateds and aromatics respectively together with desorbent, is separately fractionated to recover the desired products, the desorbent being recycled. Examples relate to straight run naphtha with or without isopentane diluent, a catalytic gasoline fraction containing also olefins, and a catalytic reformate, the desorbent being benzene or commercial scylenes, and isopentane being used in one case as the intermediate treating liquid.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL80577D NL80577C (en) | 1952-01-02 | ||
BE511388D BE511388A (en) | 1952-01-02 | ||
GB16952A GB711818A (en) | 1952-01-02 | 1952-01-02 | Separation of aromatics from gasoline or kerosene fractions |
FR1066841D FR1066841A (en) | 1952-01-02 | 1952-04-29 | Process for separating aromatic products from gasoline or kerosene fractions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB16952A GB711818A (en) | 1952-01-02 | 1952-01-02 | Separation of aromatics from gasoline or kerosene fractions |
Publications (1)
Publication Number | Publication Date |
---|---|
GB711818A true GB711818A (en) | 1954-07-14 |
Family
ID=9699621
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB16952A Expired GB711818A (en) | 1952-01-02 | 1952-01-02 | Separation of aromatics from gasoline or kerosene fractions |
Country Status (4)
Country | Link |
---|---|
BE (1) | BE511388A (en) |
FR (1) | FR1066841A (en) |
GB (1) | GB711818A (en) |
NL (1) | NL80577C (en) |
-
0
- BE BE511388D patent/BE511388A/xx unknown
- NL NL80577D patent/NL80577C/xx active
-
1952
- 1952-01-02 GB GB16952A patent/GB711818A/en not_active Expired
- 1952-04-29 FR FR1066841D patent/FR1066841A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
FR1066841A (en) | 1954-06-10 |
BE511388A (en) | |
NL80577C (en) |
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