GB363330A - Improvements in refining acid oils and tar acids from tar distillates and the like - Google Patents

Improvements in refining acid oils and tar acids from tar distillates and the like

Info

Publication number
GB363330A
GB363330A GB17956/30A GB1795630A GB363330A GB 363330 A GB363330 A GB 363330A GB 17956/30 A GB17956/30 A GB 17956/30A GB 1795630 A GB1795630 A GB 1795630A GB 363330 A GB363330 A GB 363330A
Authority
GB
United Kingdom
Prior art keywords
oil
sodium hydrate
tar
tar acids
phenolate
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
GB17956/30A
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.)
COAL OIL EXTRACTION Ltd
Original Assignee
COAL OIL EXTRACTION 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 COAL OIL EXTRACTION Ltd filed Critical COAL OIL EXTRACTION Ltd
Publication of GB363330A publication Critical patent/GB363330A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10CWORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C1/00Working-up tar
    • C10C1/20Refining by chemical means inorganic or organic compounds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Fats And Perfumes (AREA)

Abstract

Acid tar oils or the tar acids extracted therefrom are refined so as to yield white not pink emulsions with water, by adding alkali and passing in gas containing oxygen. For example, to oil from which the more volatile portions have been removed for use as fuel there is added an aqueous solution containing 0,1 of the sodium hydrate necessary for neutralization, and air is blown in until oxidation of the constituents producing the pink colour is complete; the oil is then acidified to liberate the combined tar acids, or is allowed to settle and removed from the phenolate layer which is treated separately; dead oil may then be added in any desired quantity. Tar acids are preferably obtained by removing all the phenols by the theoretical quantity of sodium hydrate solution, and treating the extract with air at atmospheric temperature or while steam is blown in to remove entrained hydrocarbons and pyridine; the phenolate is then acidified. A disinfectant may be produced by mixing 20 grams of oil, 6,8 cc. of rosin, and 4 cc. of an aqueous solution containing 200 grams of sodium hydrate per litre.ALSO:Acid tar oils or the tar acids extracted therefrom are refined so as to yield white not pink emulsions with water, by adding alkali and passing in gas containing oxygen. For example to oil from which the more volatile portions have been removed for use as fuel there is added an aqueous solution containing 0,1 of the sodium hydrate necessary for neutralization, and air is blown in until oxidation of the constituents producing the pink colour is complete ; the oil is then acidified to liberate the combined tar acids, or is allowed to settle and removed from the phenolate layer which is treated separately ; dead oil may then be added in any desired quantity. Tar acids are preferably obtained by removing all the phenols by the theoretical quantity of sodium hydrate solution, and treating the extract with air at atmospheric temperature or while steam is blown in to remove entrained hydrocarbons and pyridine ; the phenolate is then acidified. A disinfectant may be produced by mixing 20 grams of oil, 6,8 c.c. of rosin and 4 c.c. of an aqueous solution containing 200 grams of sodium hydrate per litre.ALSO:Acid tar oils or the tar acids extracted therefrom are refined so as to yield white, not pink, emulsions with water, by adding alkali and passing in gas containing oxygen. For example to oil from which the more volatile portions have been removed for use as fuel there is added an aqueous solution containing 0,1 of the sodium hydrate necessary for neutralization, and air is blown in until oxidation of the constituents producing the pink colour is complete; the oil is then acidified to liberate the combined tar acids, or is allowed to settle and removed from the phenolate layer which is treated separately; dead oil may then be added in any desired quantity. Tar acids are preferably obtained by removing all the phenols by the theoretical quantity of sodium hydrate solution, and treating the extract with air at atmospheric temperature or while steam is blown in to remove entrained hydrocarbons and pyridine; the phenolate is then acidified. A disinfectant may be produced by mixing 20 grams of oil, 6,8 c.c. of rosin and 4 c.c. of an aqueous solution containing 200 grams of sodium hydrate per litre.
GB17956/30A 1929-06-11 1930-06-11 Improvements in refining acid oils and tar acids from tar distillates and the like Expired GB363330A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US363330XA 1929-06-11 1929-06-11

Publications (1)

Publication Number Publication Date
GB363330A true GB363330A (en) 1931-12-11

Family

ID=21888003

Family Applications (1)

Application Number Title Priority Date Filing Date
GB17956/30A Expired GB363330A (en) 1929-06-11 1930-06-11 Improvements in refining acid oils and tar acids from tar distillates and the like

Country Status (1)

Country Link
GB (1) GB363330A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1094758B (en) * 1957-07-24 1960-12-15 Metallgesellschaft Ag Process for the production of neutral oil-free and lightfast phenols from phenol-containing oils or crude phenols
US4595489A (en) * 1982-12-27 1986-06-17 Exxon Research And Engineering Co. Removal of phenols from phenol-containing streams

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1094758B (en) * 1957-07-24 1960-12-15 Metallgesellschaft Ag Process for the production of neutral oil-free and lightfast phenols from phenol-containing oils or crude phenols
US4595489A (en) * 1982-12-27 1986-06-17 Exxon Research And Engineering Co. Removal of phenols from phenol-containing streams

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