GB359013A - Improvements in removing phenols from oils, tars and the like - Google Patents

Improvements in removing phenols from oils, tars and the like

Info

Publication number
GB359013A
GB359013A GB2103630A GB2103630A GB359013A GB 359013 A GB359013 A GB 359013A GB 2103630 A GB2103630 A GB 2103630A GB 2103630 A GB2103630 A GB 2103630A GB 359013 A GB359013 A GB 359013A
Authority
GB
United Kingdom
Prior art keywords
phenols
water
per cent
stream
mixture
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
Application number
GB2103630A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NORMAN ROY HOOD
Imperial Chemical Industries Ltd
Original Assignee
NORMAN ROY HOOD
Imperial Chemical Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by NORMAN ROY HOOD, Imperial Chemical Industries Ltd filed Critical NORMAN ROY HOOD
Priority to GB2103630A priority Critical patent/GB359013A/en
Publication of GB359013A publication Critical patent/GB359013A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G31/00Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/08Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by treating with water

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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Phenol, cresol, xylenol, and other phenols are removed from oils, tars, and the like by treating a mixture of the oil and water in countercurrent column with a descending stream of water. Preferably the mixture, the stream of water, or both are heated to above the critical solution temperature of the phenols in water, i.e. above 63 DEG C. for phenol and above 120 DEG C. for cresols. Residual phenols may be removed by other methods, e.g. extraction with aqueous alcohol. In an example, a fraction boiling up to 200 DEG C. obtained by the hydrogenation of bituminous coal in presence of ferric oxide, and containing 11 per cent of phenols, is mixed with an equal volume of water in the centrifuge at 170 DEG C. and 3-4 atmospheres, and the hot mixture is passed up a coke-filled tower against a stream of 0,5 volume of water at 170 DEG C. and 3-4 atmospheres, the time of contact being 15 minutes. Phenols are separated from the 2-3 per cent aqueous solution passing out at the foot of the tower by cooling and allowing to separate into layers. The lower layer containing 1 per cent of phenols is heated to 170 DEG C. and re-used as solvent.ALSO:Phenol, cresol, xylenol and other phenols are removed from oils, tars, and the like by treating a mixture of the oil and water in countercurrent column with a descending stream of water. Preferably the mixture, the stream of water, or both are heated to above the critical solution temperature of the phenols in water, i.e. above 63 DEG C. for phenol and above 120 DEG C. for cresols. Residual phenols may be removed by other methods, e.g. extraction with aqueous alcohol. In an example, a fraction boiling up to 200 DEG C. obtained by the hydrogenation of bituminous coal in presence of ferric oxide, and containing 11 per cent of phenols, is mixed with an equal volume of water in a centrifuge at 170 DEG C. and 3-4 atmospheres, and the hot mixture is passed up a coke-filled tower against a stream of 0,5 volume of water at 170 DEG C. and 3-4 atmospheres, the time of contact being 15 minutes. Phenols are separated from the 2-3 per cent aqueous solution passing out at the foot of the tower by cooling and allowing to separate into layers. The lower layer containing 1 per cent of phenols is heated to 170 DEG C. and re-used as solvent.
GB2103630A 1930-07-11 1930-07-11 Improvements in removing phenols from oils, tars and the like Expired GB359013A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2103630A GB359013A (en) 1930-07-11 1930-07-11 Improvements in removing phenols from oils, tars and the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2103630A GB359013A (en) 1930-07-11 1930-07-11 Improvements in removing phenols from oils, tars and the like

Publications (1)

Publication Number Publication Date
GB359013A true GB359013A (en) 1931-10-12

Family

ID=10156089

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2103630A Expired GB359013A (en) 1930-07-11 1930-07-11 Improvements in removing phenols from oils, tars and the like

Country Status (1)

Country Link
GB (1) GB359013A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2888491A (en) * 1956-10-03 1959-05-26 Metallgesellschaft Ag Separation of phenols from their mixtures with neutral oils
US3261872A (en) * 1960-12-02 1966-07-19 Still Fa Carl Process for extracting acid substances such as phenols, thiophenols and/or their homologs from nonaqueous mixtures containing them

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2888491A (en) * 1956-10-03 1959-05-26 Metallgesellschaft Ag Separation of phenols from their mixtures with neutral oils
US3261872A (en) * 1960-12-02 1966-07-19 Still Fa Carl Process for extracting acid substances such as phenols, thiophenols and/or their homologs from nonaqueous mixtures containing them

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