GB776495A - Process for the production of hardenable condensation products - Google Patents

Process for the production of hardenable condensation products

Info

Publication number
GB776495A
GB776495A GB16221/55A GB1622155A GB776495A GB 776495 A GB776495 A GB 776495A GB 16221/55 A GB16221/55 A GB 16221/55A GB 1622155 A GB1622155 A GB 1622155A GB 776495 A GB776495 A GB 776495A
Authority
GB
United Kingdom
Prior art keywords
phenol
novolak
cresol
epichlorhydrin
formaldehyde
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
GB16221/55A
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.)
Beck Koller and Company England Ltd
Original Assignee
Beck Koller and Company England 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 Beck Koller and Company England Ltd filed Critical Beck Koller and Company England Ltd
Publication of GB776495A publication Critical patent/GB776495A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G8/00Condensation polymers of aldehydes or ketones with phenols only
    • C08G8/28Chemically modified polycondensates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/02Polycondensates containing more than one epoxy group per molecule
    • C08G59/04Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof
    • C08G59/06Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols
    • C08G59/08Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols from phenol-aldehyde condensates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Epoxy Resins (AREA)

Abstract

Epoxy resins soluble in the usual solvents for such resins, e.g. ketones and glycol monoethers, and suitable for casting or for electrical insulation, are produced by reacting an epihalogenhydrin in alkaline medium with a novolak which has been produced by reacting excess phenol with formaldehyde under acid conditions, separating the aqueous layer and distilling to remove excess phenol and render the resin anhydrous, excess phenol being added during the novolak-epichlorhydrin reaction; alternatively the novolak containing the original excess phenol and without dehydration may be reacted with the epichlorhydrin. The additional phenol added may be phenol, cresol, xylenol, chlorphenol or their glycide ethers may be employed. The optimum formaldehyde/phenol ratio for the production of the novolak is 0.5, but for phenol homologues, e.g. p- or o-cresol the ratio may be somewhat higher. The product may be mixed with fillers or dyestuffs and then hardened by addition of conventional hardening agents, e.g. amines-triethanolamine or piperidine, or polybasic acids or their anhydrides, e.g. phthalic and maleic acids, (1) 440 gs. novolak produced by reacting formaldehyde and phenol in molar ratio 0.5/1 and freeing the product of water and phenol by distillation is mixed with 170 gs. phenol dissolved in 2400 gs. 10 per cent NaOH solution and 556 gs. epichlorhydrin are added, the resulting exothermic reaction being maintained at 80 DEG C. by cooling; the resin is dehydrated by decantation, distillation and purified by solution in acetone and filtering followed by distillation or reduced pressure. In Examples (2)-(5), the novolak obtained in Example (1) is reacted with epichlorhydrin and (2) cresol, (3) xylenol, (4) glycide phenol ether, (7) chlorphenol. In Examples (5) and (6) a cresol-formaldehyde novolak is reacted, (5) with phenol, and (6) with cresol. Example (8), 1410 gs. phenol, 645 gs. 36 per cent formaldehyde and 14 gs. oxalic acid are boiled under reflux; the CH2O content of the aqueous layer is then 0.2-0.3 per cent 600 gs. NaOH dissolved in 6000 gs. water are added, the mixture is heated to 60 DEG C. and 1390 gs. epichlorhydrin added; after decantation, washing and filtration, 1840 gs. resin are obtained.
GB16221/55A 1954-06-04 1955-06-06 Process for the production of hardenable condensation products Expired GB776495A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE334654X 1954-06-04
DE160654X 1954-06-16

Publications (1)

Publication Number Publication Date
GB776495A true GB776495A (en) 1957-06-05

Family

ID=25753573

Family Applications (1)

Application Number Title Priority Date Filing Date
GB16221/55A Expired GB776495A (en) 1954-06-04 1955-06-06 Process for the production of hardenable condensation products

Country Status (4)

Country Link
CH (1) CH334654A (en)
FR (1) FR1125761A (en)
GB (1) GB776495A (en)
NL (2) NL100644C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1132729B (en) * 1958-10-31 1962-07-05 Elizabeth Shen Lo Process for the production of epoxy resins
DE1148077B (en) * 1958-04-01 1963-05-02 Ciba Geigy Process for the preparation of fusible glycidyl polyethers
GB2128616A (en) * 1982-08-20 1984-05-02 Sumitomo Chemical Co Glycidyl ether of novolak type substituted phenolic resin and its production

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1148077B (en) * 1958-04-01 1963-05-02 Ciba Geigy Process for the preparation of fusible glycidyl polyethers
DE1132729B (en) * 1958-10-31 1962-07-05 Elizabeth Shen Lo Process for the production of epoxy resins
GB2128616A (en) * 1982-08-20 1984-05-02 Sumitomo Chemical Co Glycidyl ether of novolak type substituted phenolic resin and its production

Also Published As

Publication number Publication date
NL197796A (en)
NL100644C (en)
CH334654A (en) 1958-12-15
FR1125761A (en) 1956-11-07

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