GB850176A - Purification of lower aliphatic acids - Google Patents

Purification of lower aliphatic acids

Info

Publication number
GB850176A
GB850176A GB8095/57A GB809557A GB850176A GB 850176 A GB850176 A GB 850176A GB 8095/57 A GB8095/57 A GB 8095/57A GB 809557 A GB809557 A GB 809557A GB 850176 A GB850176 A GB 850176A
Authority
GB
United Kingdom
Prior art keywords
acids
acid
heating
weight
liquid phase
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
GB8095/57A
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.)
Celanese Corp
Original Assignee
Celanese Corp
Celanese Corp of America
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 Celanese Corp, Celanese Corp of America filed Critical Celanese Corp
Publication of GB850176A publication Critical patent/GB850176A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/487Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Acetic, propionic, and butyric acids respectively containing small proportions of impurities are purified by heating the acid in the liquid phase to a temperature of at least 235 DEG C. but below that at which the acid decomposes to any substantial extent and then distilling off purified acid from the impure product. Preferably the acid is heated to between 235 DEG C. and 330 DEG C. and in the presence of a small proportion by weight, e.g. between 0,2 and 10% by weight, of an ionisable salt soluble in the acid, e.g. a sodium or potassium salt of the acid being treated. It is also desirable to have present a small proportion by weight of water, e.g. from 1 to 10% by weight based on the weight of the acid. The impure acids submitted to the heating process may be obtained by the liquid phase oxidation of lower aliphatic hydrocarbons containing up to 7 carbon atoms, e.g. propane or butane, such acids containing up to 2,000 parts per million of residual impurities such as aldehydes, hydroxycarbonylic compounds and ethylenically unsaturated compounds. To maintain the acids in the liquid phase a high superatmospheric pressure must be applied thereto and this may be the autogenous pressure developed by heating the acids in a closed vessel when the heating operation is carried out on a batch basis. The superatmospheric pressure may also be applied to the acids by means of a pump when the heating is carried out in a continuous manner by forcing the acids into and through a heating chamber. Suitable heating times are normally between 1 and 20 hours. During the heating period the impurities present decompose or condense to form high boiling compounds from which the fatty acids are separated by fractional distillation. A portion of the decomposition products is gaseous and may simply be vented from the acids during or after the heating period. Examples are given for the purification of acetic acid containing about 2,000 parts per million of impurities and which has been prepared by the liquid phase oxidation of propane and butane and which has first been purified by fractional distillation.
GB8095/57A 1956-03-12 1957-03-12 Purification of lower aliphatic acids Expired GB850176A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US850176XA 1956-03-12 1956-03-12

Publications (1)

Publication Number Publication Date
GB850176A true GB850176A (en) 1960-09-28

Family

ID=22188838

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8095/57A Expired GB850176A (en) 1956-03-12 1957-03-12 Purification of lower aliphatic acids

Country Status (1)

Country Link
GB (1) GB850176A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5227520A (en) * 1991-10-02 1993-07-13 Bp Chemicals Limited Process for the purification of carboxylic acids and/or their anyhdrides
WO1997001525A1 (en) * 1995-06-28 1997-01-16 Biochemie Gesellschaft Mbh Process for separating pivalic acid from spent reaction mixtures
CN114133090A (en) * 2021-12-15 2022-03-04 江西吉煜新材料有限公司 Method and equipment for recycling propionic acid and butyric acid secondary mother liquor water

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5227520A (en) * 1991-10-02 1993-07-13 Bp Chemicals Limited Process for the purification of carboxylic acids and/or their anyhdrides
WO1997001525A1 (en) * 1995-06-28 1997-01-16 Biochemie Gesellschaft Mbh Process for separating pivalic acid from spent reaction mixtures
US5990351A (en) * 1995-06-28 1999-11-23 Biochemie Gmbh Process for separating pivalic acid from spent reaction mixtures
CN114133090A (en) * 2021-12-15 2022-03-04 江西吉煜新材料有限公司 Method and equipment for recycling propionic acid and butyric acid secondary mother liquor water
CN114133090B (en) * 2021-12-15 2022-12-13 江西吉煜新材料有限公司 Method and equipment for recycling propionic acid and butyric acid secondary mother liquor water

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