GB827433A - Refining petroleum wax by contact filtration - Google Patents
Refining petroleum wax by contact filtrationInfo
- Publication number
- GB827433A GB827433A GB38651/57A GB3865157A GB827433A GB 827433 A GB827433 A GB 827433A GB 38651/57 A GB38651/57 A GB 38651/57A GB 3865157 A GB3865157 A GB 3865157A GB 827433 A GB827433 A GB 827433A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sieve
- solvent
- waxes
- sieves
- regenerated
- 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
- C10G25/02—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material
- C10G25/03—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material with crystalline alumino-silicates, e.g. molecular sieves
- C10G25/05—Removal of non-hydrocarbon compounds, e.g. sulfur compounds
-
- 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
- C10G25/02—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material
- C10G25/03—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material with crystalline alumino-silicates, e.g. molecular sieves
-
- 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
- C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
- C10G73/42—Refining of petroleum waxes
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Petroleum waxes are refined by contacting them at 150 DEG to 450 DEG F. with a molecular sieve having a pore size of 10 to 15 . The wax may be a paraffin or microcrystalline wax and it is preferably de-oiled to an oil content of less than 1% with a solvent such as propane or M.E.K. The Specification includes a summary of the conventional methods of extracting waxes from petroleum oils and de-oiling waxes including chilling, solvent de-waxing of oils, sweating, solvent de-oiling of waxes, H2SO4 treatment or mild hydrogenation (600 DEG F., 200 p.s.i.g.) and percolation through adsorbent clay. The contacting is preferably conducted at 300 DEG to 400 DEG F. for 5 to 60 minutes using a 13 sieve. Used sieves may be regenerated by washing with solvents, e.g. hexane, secondary butyl acetate and M.E.K. mixed with toluene, but regeneration by heating at 700-800 DEG F. for 1 to 10 hours with a regenerative gas consisting of nitrogen containing less than 2 vol. per cent each of oxygen and water, less than 0.7 vol. per cent of SO2 and minor amounts of carbon dioxide is preferred. Examples of the treatment with a 13 sieve of paraffin wax extracted from a lubricating oil extract which had been de-oiled by sweating and acid treated demonstrate: (1) the relative effectiveness of (1) 5% and 20% wt. of the sieve and conventional adsorbents at 300 DEG C.; (2) 20% wt. of the sieve and conventional adsorbents at 400 DEG C.; (3) 5% wt. of fresh, solvent regenerated, and heat regenerated sieve at 300 DEG F.; and (4) 5% wt. of the sieve at 300 DEG and 400 DEG F. Preparation of the sieves.-The sieves used are zeolites which may be synthetic. A 13 sieve may be prepared by reacting a sodium silicate of high Na:Si ratio, e.g. sodium metasilicate, with a sodium aluminate having a Na:Al ratio between 1:1 and 3:1 in proportions to give a Si:Al ratio of at least 3:1, preferably between 4:1 and 10:1. The resultant precipitate is heated (as a homogeneous paste) at 180-215 DEG F. for about 200 hours, filtered, water-washed, dried and calcined at 700 DEG to 900 DEG F.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US827433XA | 1956-12-28 | 1956-12-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB827433A true GB827433A (en) | 1960-02-03 |
Family
ID=22173156
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB38651/57A Expired GB827433A (en) | 1956-12-28 | 1957-12-12 | Refining petroleum wax by contact filtration |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB827433A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0361681A1 (en) * | 1988-08-31 | 1990-04-04 | Exxon Chemical Patents Inc. | Process for the purification of linear paraffins |
US5109139A (en) * | 1988-08-31 | 1992-04-28 | Exxon Chemical Patents Inc. | Process control of process for purification of linear paraffins |
US5171923A (en) * | 1988-08-31 | 1992-12-15 | Exxon Chemical Patents Inc. | Recycle for process for purification of linear paraffins |
-
1957
- 1957-12-12 GB GB38651/57A patent/GB827433A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0361681A1 (en) * | 1988-08-31 | 1990-04-04 | Exxon Chemical Patents Inc. | Process for the purification of linear paraffins |
US5109139A (en) * | 1988-08-31 | 1992-04-28 | Exxon Chemical Patents Inc. | Process control of process for purification of linear paraffins |
US5171923A (en) * | 1988-08-31 | 1992-12-15 | Exxon Chemical Patents Inc. | Recycle for process for purification of linear paraffins |
US5220099A (en) * | 1988-08-31 | 1993-06-15 | Exxon Chemical Patents Inc. | Purification of a hydrocarbon feedstock using a zeolite adsorbent |
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