GB808101A - Process for obtaining pure trimethylolpropane - Google Patents

Process for obtaining pure trimethylolpropane

Info

Publication number
GB808101A
GB808101A GB33625/55A GB3362555A GB808101A GB 808101 A GB808101 A GB 808101A GB 33625/55 A GB33625/55 A GB 33625/55A GB 3362555 A GB3362555 A GB 3362555A GB 808101 A GB808101 A GB 808101A
Authority
GB
United Kingdom
Prior art keywords
trimethylolpropane
raffinate
cyclohexanol
treated
solvent
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
GB33625/55A
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.)
Bayer AG
Original Assignee
Bayer AG
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 Bayer AG filed Critical Bayer AG
Publication of GB808101A publication Critical patent/GB808101A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/76Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
    • C07C29/86Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by liquid-liquid treatment
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/14The ring being saturated

Landscapes

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

Abstract

Pure trimethylolpropane is obtained from the aqueous reaction mixture obtained by alkaline condensation of butyraldehyde with formaldehyde, by treating the reaction mixture with a partially water-miscible solvent consisting of a monohydric aliphatic, cycloaliphatic or araliphatic alcohol containing 4-8 carbon atoms thus forming an aqueous phase and an organic phase, organic impurities going into the organic phase and the trimethylolpropane being distributed between the aqueous and organic phases. If a minor amount of solvent is used the bulk of the trimethylolpropane remains in the aqueous phase and the organic impurities, together with a small amount of trimethylolpropane pass into the organic phase. The bulk of the trimethylolpropane can be obtained from the aqueous solution by treating it with a greater quantity of the same or a different solvent as defined above. The small quantity of trimethylol propane can be recovered from the organic phase by washing with water or with a trimethylolpropane-free raffinate obtained at the end of the working process. If a major amount of the solvent is used the trimethylolpropane and organic impurities go into the organic phase. The bulk of the solvent is distilled off and the remaining extract is treated with water or a trimethylolpropane-free raffinate so that the trimethylol propane goes into the aqueous phase and the organic impurities remain behind in the solvent. In the examples: (a) a solution of trimethylolpropane obtained by the alkaline condensation of butyraldehyde and formaldehyde is treated with a minor proportion of iso-octanol to give an extract layer containing small amounts of trimethylolpropane and iso-octanol and organic impurities and a raffinate containing the major part of the trimethylolpropane; the iso-octanol is reclaimed from the extract layer by distillation; the raffinate layer is treated with a large quantity of iso-octanol, thereby giving an extract containing the bulk of the trimethylolpropane, which is obtained by evaporating the extract solution and may be further purified by distillation; and (b) a solution of trimethylolpropane obtained by the alkaline condensation of butyraldehyde and formaldehyde is treated with a major quantity of cyclohexanol thus forming an extract layer containing most of the trimethylolpropane and cyclohexanol and a raffinate containing small amounts of trimethylolpropane and cyclohexanol; the extract layer is distilled to give cyclohexanol, trimethylolpropane and a residue containing a further quantity of trimethylolpropane; the residue is treated with a major portion of the raffinate from the first extraction and a minor amount of cyclohexanol is added; the raffinate so obtained may be treated with a further quantity of cyclohexanol or may be added to some fresh crude condensation solution.
GB33625/55A 1954-11-23 1955-11-23 Process for obtaining pure trimethylolpropane Expired GB808101A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE808101X 1954-11-23

Publications (1)

Publication Number Publication Date
GB808101A true GB808101A (en) 1959-01-28

Family

ID=6723014

Family Applications (1)

Application Number Title Priority Date Filing Date
GB33625/55A Expired GB808101A (en) 1954-11-23 1955-11-23 Process for obtaining pure trimethylolpropane

Country Status (1)

Country Link
GB (1) GB808101A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999020586A1 (en) * 1997-10-16 1999-04-29 Celanese International Corporation Process improvement to produce low color trimethylolpropane
EP1848679A1 (en) * 2006-03-07 2007-10-31 LG Chem. Ltd. Method for preparing trimethylolpropane
EP2167450A1 (en) * 2007-06-18 2010-03-31 Perstorp Specialty Chemicals AB Method for extraction in a process for production of a di, tri or polyhydric alcohol
CN103467252A (en) * 2013-09-05 2013-12-25 百川化工(如皋)有限公司 Method for increasing purity of di-trimethylolpropane

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999020586A1 (en) * 1997-10-16 1999-04-29 Celanese International Corporation Process improvement to produce low color trimethylolpropane
EP1848679A1 (en) * 2006-03-07 2007-10-31 LG Chem. Ltd. Method for preparing trimethylolpropane
EP1848679A4 (en) * 2006-03-07 2010-06-09 Lg Chemical Ltd Method for preparing trimethylolpropane
EP2167450A1 (en) * 2007-06-18 2010-03-31 Perstorp Specialty Chemicals AB Method for extraction in a process for production of a di, tri or polyhydric alcohol
EP2167450A4 (en) * 2007-06-18 2010-08-04 Perstorp Specialty Chem Ab Method for extraction in a process for production of a di, tri or polyhydric alcohol
CN103467252A (en) * 2013-09-05 2013-12-25 百川化工(如皋)有限公司 Method for increasing purity of di-trimethylolpropane

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