US1795382A - Process for obtaining phenols from phenol-bearing industrial liquors - Google Patents

Process for obtaining phenols from phenol-bearing industrial liquors Download PDF

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US1795382A
US1795382A US90684A US9068426A US1795382A US 1795382 A US1795382 A US 1795382A US 90684 A US90684 A US 90684A US 9068426 A US9068426 A US 9068426A US 1795382 A US1795382 A US 1795382A
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phenols
phenol
liquors
bases
obtaining
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US90684A
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Ulrich Fritz
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ZECHE MATHIAS STINNES
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ZECHE MATHIAS STINNES
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/005Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by obtaining phenols from products, waste products or side-products of processes, not directed to the production of phenols, by conversion or working-up

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  • the above mentioned objection is removed by adding to the extraction media hitherto employed tar bases viz., bases of coke-plant tar or of low-temperature distillation tar, such as pyridine, quinoline or their homologues, the
  • Example I 500 cubic centimetres of an ammoniacal liquor which as before contains 3.19 grams of phenols per litre is washed three times, each time with. 100 cubic centimetres of bases, which have been obtained from tar oil having a boiling point of from240 C. to 320 C.
  • the phenols could be iron I ing treating the said liquors with tar bases.
  • a process for obtaining phenols from phenol-bearing industrial liquors comprising treating said liquors with bases from coke-plant tar.
  • a process for obtaining phenols from phenol bearing industrial liquors comprising treating said liquors with tar oils from which the phenols have been removed but which still contain bases.
  • a process for obtaining phenols from phenol bearing industrial liquors comprising treating the said liquors with a mixture of aromatic hydrocarbons and tar bases.
  • a process for obtaining phenols from phenol-bearing industrial liquors comprising treating the said liquors with a mixture of aromatic hydrocarbons and bases from coke plant tar.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Patented Mar. 10, 1931 UNITED STATES P E To Flca IRI'rz ULRIcn, or KARNAZP, NEAR ESSEN-RUHR, GERMANY, AssIeNo ro zEcRE MATHIAS STINNES, or nssE JwnR, GERMANY PROCESS FOR OBTAINING PHENOLS FROM runner-BE RIN INDUSTRIAL LIoUoRs No Drawing. Application filed February 25, 1926, Serial No. 90,684, and in Germany March-13, 1925.
According to the processes hitherto known the washing of phenol-bearing industrial liquors including ammoniacal liquor for the purpose of removing phenol therefrom is efi'ected exclusively by means of benzene or its homologues. This process has the great disadvantage that it does not make it possible to obtain the Whole of the phenols of the ammoniacal liquor and in particular the valuable water-soluble carbolic acid. Many experiments carried out on the basis of this process have yielded the result that on an average only about per cent of the phenols present in the ammoniacal liquor can be recovered economically, while the remaining 35 per cent consisting mainly of carbolic acid is to be abandoned.
According to the present invention the above mentioned objection is removed by adding to the extraction media hitherto employed tar bases viz., bases of coke-plant tar or of low-temperature distillation tar, such as pyridine, quinoline or their homologues, the
boiling point of which is preferably so high that the solubility in water of this class of substances is no longer in evidence. The greater cleansing action which is obtained with such a basic gas-washing oil, readily admits of being explained by the chemical affinity of the bases for the acid phenols. Accordingly the actual washing action in this process is to be attributed to the bases themselves, while benzene and its homologues are to be regarded as solvents or diluents for these substances and may therefore be replaced by petrol or other neutral oils.
Comparative experiments based on the processes hitherto usual and the process forming the subject matter of the present inven tion have given the following results:
Example I centimeters of a washing medium consisting of. 90degree benzene and 10 per cent. bases (boiling point from 200 to 250 0.). The yield of phenolamounts in this case to 82 per cent of the whole quantity of phenols in the ammonical liquor; Theincreased yield of phenol as compared withexperiment (a) Example [I 2 litres of the same ammoniacal liquor are. washed twice with a 20 per cent. quantity (that is, 2 400 cubic centimetres) of washing oil consisting of 90-degree benzene with 20 per cent. of bases boiling at 230 O. From the liquor so treated no perceptible quantities of phenols can be obtained by subsequent extraction with ether. The yield is therefore to be regarded as practically quantitative.
In the'case of a similarly arranged experiment with 90-degree benzene as washing medium, only a yield of about 65 per cent could be obtained. I
E wamplc I l I 500 cubic centimetres of a crude ammoniacal liquor with 3.19 grams of phenols per litre are washed three times with 200 cubic centimetres of a tar, oil from which phenol has been removed and which has a boiling point of from 200 to 250 C. in which 4 per cent of bases as such are contained, which here come into action in a free state. In this way 82 per cent of the phenols could be recovered.
Example I V 500 cubic centimetres of an ammoniacal liquor which as before contains 3.19 grams of phenols per litre is washed three times, each time with. 100 cubic centimetres of bases, which have been obtained from tar oil having a boiling point of from240 C. to 320 C.
About 7 5 per cent of, the phenols could be iron I ing treating the said liquors with tar bases.
2. A process for obtaining phenols from phenol-bearing industrial liquors, comprising treating said liquors with bases from coke-plant tar.
3. A process for obtaining phenols from phenol bearing industrial liquors, comprising treating said liquors with tar oils from which the phenols have been removed but which still contain bases.
4. A process for obtaining phenols from phenol bearing industrial liquors, comprising treating the said liquors with a mixture of aromatic hydrocarbons and tar bases.
5. A process for obtaining phenols from phenol-bearing industrial liquors, comprising treating the said liquors with a mixture of aromatic hydrocarbons and bases from coke plant tar.
In testimony whereof I afiiX my signature.
DooroR FRITZ ULRICH.
US90684A 1925-03-13 1926-02-25 Process for obtaining phenols from phenol-bearing industrial liquors Expired - Lifetime US1795382A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2432064A (en) * 1943-10-20 1947-12-02 Reilly Tar & Chem Corp Purification of quinaldine
US2432062A (en) * 1943-07-05 1947-12-02 Reilly Tar & Chem Corp Separation of metacresol from paracresol
US2432065A (en) * 1943-10-29 1947-12-02 Reilly Tar & Chem Corp Purification of isoquinoline
US2526807A (en) * 1945-08-20 1950-10-24 Francis E Cislak Process for separating 1, 3, 4-xylenol and 1, 4, 2-xylenol from mixtures containing the same and organic base complexes derived therefrom
US2808375A (en) * 1954-05-10 1957-10-01 Jones & Laughlin Steel Corp Phenol removal from phenol-contaminated waste waters
US2812305A (en) * 1954-08-25 1957-11-05 Jones & Laughlin Steel Corp Phenol removal from phenol-bearing waters
US2829175A (en) * 1953-10-14 1958-04-01 Gulf Research Development Co Purification of bis-phenols

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2432062A (en) * 1943-07-05 1947-12-02 Reilly Tar & Chem Corp Separation of metacresol from paracresol
US2432064A (en) * 1943-10-20 1947-12-02 Reilly Tar & Chem Corp Purification of quinaldine
US2432065A (en) * 1943-10-29 1947-12-02 Reilly Tar & Chem Corp Purification of isoquinoline
US2526807A (en) * 1945-08-20 1950-10-24 Francis E Cislak Process for separating 1, 3, 4-xylenol and 1, 4, 2-xylenol from mixtures containing the same and organic base complexes derived therefrom
US2829175A (en) * 1953-10-14 1958-04-01 Gulf Research Development Co Purification of bis-phenols
US2808375A (en) * 1954-05-10 1957-10-01 Jones & Laughlin Steel Corp Phenol removal from phenol-contaminated waste waters
US2812305A (en) * 1954-08-25 1957-11-05 Jones & Laughlin Steel Corp Phenol removal from phenol-bearing waters

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