GB431609A - A process for the manufacture of valuable products, such as lubricating oils resistant to oxidation, transformer oils, and the like - Google Patents
A process for the manufacture of valuable products, such as lubricating oils resistant to oxidation, transformer oils, and the likeInfo
- Publication number
- GB431609A GB431609A GB19159/34A GB1915934A GB431609A GB 431609 A GB431609 A GB 431609A GB 19159/34 A GB19159/34 A GB 19159/34A GB 1915934 A GB1915934 A GB 1915934A GB 431609 A GB431609 A GB 431609A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- paraffinous
- liquid
- phase
- oils
- 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
- C10G71/00—Treatment by methods not otherwise provided for of hydrocarbon oils or fatty oils for lubricating purposes
Abstract
Lubricating and transformer oils are obtained by polymerizing unsaturated hydrocarbons obtained by: (1) liquid-phase cracking of such materials as paraffin wax, ozokerite, ceresine, wax-tailings, paraffinous shale, and paraffinous distillates and residues from brown coal tar, to obtain mainly a product of B.P. 150--450 DEG C.; (2) refining this fraction, e.g. by chemical agents, adsorbents, or selective solvents such as liquid sulphur dioxide, nitrobenzol, furfurol, or mixtures; (3) cracking the refined product in the vapour phase, followed or not by refining, preferably by aluminium chloride at elevated temperature, to remove diolefines. For example, 1000 kg. of topped paraffinous Roumanian crude oil is cracked in the liquid phase at 450 DEG C. and 44 atmospheres with reflux above 400 DEG C., and the 810 kg. fraction of B.P. 200--400 DEG C. is treated with liquid sulphur dioxide; the 690 kg. of raffinate is cracked in the vapour phase at 580 DEG C. and atmos. pressure, yielding 420 gm. of suitable unsaturated oil which is polymerized with the aid of aluminium chloride; in addition to 300 kg. of first class lubricating oil there is obtained a Diesel oil and a spindle oil.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL431609X | 1933-07-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB431609A true GB431609A (en) | 1935-07-11 |
Family
ID=19786154
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB19159/34A Expired GB431609A (en) | 1933-07-15 | 1934-06-28 | A process for the manufacture of valuable products, such as lubricating oils resistant to oxidation, transformer oils, and the like |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB431609A (en) |
-
1934
- 1934-06-28 GB GB19159/34A patent/GB431609A/en not_active Expired
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