GB840500A - Process for the production of urethane polyisocyanates - Google Patents

Process for the production of urethane polyisocyanates

Info

Publication number
GB840500A
GB840500A GB13082/58A GB1308258A GB840500A GB 840500 A GB840500 A GB 840500A GB 13082/58 A GB13082/58 A GB 13082/58A GB 1308258 A GB1308258 A GB 1308258A GB 840500 A GB840500 A GB 840500A
Authority
GB
United Kingdom
Prior art keywords
isocyanate
column
mixture
extracted
polyhydric alcohol
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
GB13082/58A
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 Corp
Original Assignee
Mobay Corp
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 Mobay Corp filed Critical Mobay Corp
Publication of GB840500A publication Critical patent/GB840500A/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
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/80Masked polyisocyanates
    • C08G18/8003Masked polyisocyanates masked with compounds having at least two groups containing active hydrogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

In a process of producing urethane polyisocyanates having a high content of available -NCO, but which do not emit toxic vapours, by reacting an organic di-isocyanate with a polyhydric alcohol, the proportions of the two reactants being such that there is more than 1 mol. of di-isocyanate for each hydroxyl group of the polyhydric alcohol whereby the formation of polymeric products of high molecular weight is minimized, the liquid reaction mixture is extracted, preferably at a temperature between 50 DEG C. and 130 DEG C., with a liquid aliphatic and/or alicyclic hydrocarbon, or a mixture of such hydrocarbons, in order to dissolve out unreacted di-isocyanate from the urethane polyisocyanate product. Hexanes, cyclohexane, the alkyl cyclohexanes, heptanes, octanes, gasoline fractions and synthetic hydrocarbon fractions are the preferred extraction media. In an example, a mixture of toluylene-2,4-di-isocyanate and toluylene-2,6-di-isocyanate is heated to 90 DEG C.; and a mixture comprising trimethylol propane and 1,3-butylene glycol is added over a period of 2 1/2 hrs. while maintaining the temperature at about 88 DEG to 100 DEG C. The resulting urethane polyisocyanate, dissolved in excess toluylene diisocyanate, is then extracted with a solvent (boiling range 315-390 DEG F.) comprising about 88% paraffins and naphthenes and about 11.5% aromatics. The extraction is carried out in an externally heated vertical column divided into seven sections, each containing a turbineagitator. The polyisocyanate is fed continuously into the top of the column, while the solvent is introduced into the bottom; the temperature of the column being held in the range of 100 DEG to 116 DEG C. The extracted product, withdrawn from the bottom of the column, is heated in vacuo to remove solvent. The final product is an amber solid which contains 18.5% available NCO. Other polyhydric alcohols which may be reacted with organic diisocyanates are: pentaerythritol, triethanolamine, neopentyl glycol, and castor oil. It is also possible to use, together with the polyhydric alcohol, a small amount of a higher-molecular polyhydroxy compound, such as hydroxyl polyesters or hydroxyl polyethers.
GB13082/58A 1957-04-29 1958-04-24 Process for the production of urethane polyisocyanates Expired GB840500A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US840500XA 1957-04-29 1957-04-29

Publications (1)

Publication Number Publication Date
GB840500A true GB840500A (en) 1960-07-06

Family

ID=22182570

Family Applications (1)

Application Number Title Priority Date Filing Date
GB13082/58A Expired GB840500A (en) 1957-04-29 1958-04-24 Process for the production of urethane polyisocyanates

Country Status (1)

Country Link
GB (1) GB840500A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114195974A (en) * 2021-12-06 2022-03-18 季华实验室 Polyurethane prepolymer and preparation method thereof, and polyurethane product

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114195974A (en) * 2021-12-06 2022-03-18 季华实验室 Polyurethane prepolymer and preparation method thereof, and polyurethane product

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