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GB679536A - Improvements in epoxide preparation - Google Patents

Improvements in epoxide preparation

Info

Publication number
GB679536A
GB679536A GB13838/48A GB1383848A GB679536A GB 679536 A GB679536 A GB 679536A GB 13838/48 A GB13838/48 A GB 13838/48A GB 1383848 A GB1383848 A GB 1383848A GB 679536 A GB679536 A GB 679536A
Authority
GB
United Kingdom
Prior art keywords
epichlorhydrin
reacted
mols
condensed
dioxane
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
GB13838/48A
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 Coatings Co Inc
Original Assignee
Devoe and Raynolds Co Inc
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 Devoe and Raynolds Co Inc filed Critical Devoe and Raynolds Co Inc
Publication of GB679536A publication Critical patent/GB679536A/en
Expired legal-status Critical Current

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  • Polyurethanes Or Polyureas (AREA)
  • Epoxy Compounds (AREA)

Abstract

"Complex halohydrins" are made by condensing an epihalohydrin with a polyhydric compound such as a polyhydric phenol or alcohol or mixture thereof. They are treated with alkali metal zincates, silicates or aluminates in non-aqueous media to yield epoxides. Epihalohydrins exclude epifluorohydrins. Many polyhydric compounds are specified representative being ethylene glycol, 1,12-dihydroxy octadecane, 1,4-dihydroxycyclohexane, glycerol, mannitol, polyallyl alcohol, 4,41-dimethylol diphenyl triglycerol, dimethylolanisoles, the bis-(beta-hydroxyethyl ether) of bisphenol, condensates of alkylene oxides with polyhydric alcohols, fructose, resorcinol, monostearin and glycerol monochlorohydrins. Homologues of epihalohydrins, e.g. 1,4-dichloro-2,3-epoxybutane may also be used. Epichlorhydrin is preferred. Many condensation agents are specified representative being Friedel-Crafts catalysts, e.g. AlCl3 and BF3 etherates, acid type catalysts, e.g. HF and H2SO4 and others, e.g. POCl3 and SbCl5. Generally, the condensation catalyst is used in up to about 5 per cent, usually less than 1 per cent, of the total reactants and temperatures indicated are 25-175 DEG C., advantageously 75-125 DEG C. With high melting and relatively insoluble polyhydric alcohols it is an advantage to use a solvent which may be a polyhydric alcohol which enters into the reaction. Thus pentaerythritol and poly-pentaerythritol may be reacted in ethylene glycol, diglycerol or trimethylol propane. Solvents for the dehydrohalogenation include hydrocarbons, ketones, ethers and halides and members of these classes are specified, dioxane being preferred. Solvents completely miscible with water facilitate filtration particularly when sodium zincate is used. The epoxide obtained may contain hydroxy and halogen groups. In dehydro-halogenation when sodium aluminate is used, temperatures of -25-125 DEG C. are specified, preferably 70-105 DEG C. for a reaction time of 1-3 hours, the aluminate is preferably in slight excess and 1-15 per cent or 30 per cent of water is preferably added, with zincates, temperatures of -125-125 DEG C. are specified although in general lower temperatures than those for aluminates are used, the quantity of salt used is from 1/3 rd to 1 mol. equivalent, depending on whether excess epihalohydrin or polyhydric compound is used, the product containing halogen when less than an equivalent of zincate is used and with silicates temperatures of -25-125 DEG C., preferably 50-105 DEG C., are used and quantities taken similar to those of the zincates. Silicates are more effective when ground. Products are recovered by filtration and distillation. Super- and sub-atmospheric pressure may be used. In examples, a condensation product prepared by reacting 18 mols. of epichlorhydrin with 6 mols. of glycerol in ethereal BF3 is treated with sodium aluminate in (1) dioxane, (2) ethyl ether and in (3) with caustic soda in ether (this example is given for comparative purposes only) with dioxane and (4) sodium ortho-silicate, (5) sodium metasilicate pentahydrate, (6) sodium sesquisilicate and (7) sodium zincate, condensation products from glycerol and epichlorhydrin in ratios of 1 : 2 and 1 : 4 respectively are reacted with (8) sodium zincate in dioxane and (9) sodium aluminate in dioxane, (10) 1 mol. of trimethylol propane is condensed with 3 mols. of epichlorhydrin and reacted in dioxane with sodium aluminate, (11) equimolar quantities of glycerol monochlorhydrin and epichlorhydrin are condensed and reacted with sodium aluminate in dioxane, (12) epichlorhydrin (2 mols.) and 1,12-dihydroxy-octadecane (1 mol.) are condensed and reacted with sodium aluminate in dioxane, (13) epichlorhydrin (3.3 mols.) and erythritol (0.84 mols.) are condensed and reacted with sodium zincate in dioxane containing a little water, (14) epichlorhydrin (5 mols.) and triglycerol (1 mol.) are condensed and reacted as in (13), (15) epichlorhydrin (6 mols.) and polyallyl alcohol (400 gms.) are condensed and treated with sodium zincate in dioxane, (16) epichlorhydrin (5.3 mols.), dextrose (0.7 mol.) and ethylene glycol (0.7 mol.) are condensed and reacted with aqueous dioxane and sodium zincate, (17) epichlorhydrin (7 mols.) and sorbitol (1 mol.) are condensed and reacted with sodium zincate in dioxane, (18) epichlorhydrin (3 mols.) and sorbitol (1 mol.) are condensed and reacted with sodium aluminate in aqueous dioxane, (19) epichlorhydrin (6 mols.) and sorbitol (1 mol.) are condensed and reacted as in (18), (20) epichlorhydrin (12 mols.) commercial pentaerythritol (317 gms.) and trimethylol propane (0.8 mol.) are condensed and reacted as in (18), (21) ethylene glycol (2 mols.), nitration grade pentaerythritol (7 mols.) and epichlorhydrin are condensed and reacted as in (18), (22) epichlorhydrin (15 mols.), dipentaerythritol (1.5 mols.) and trimethylol propane (3 mols.) are condensed and reacted as in (18), (24) ethylene oxide (157 gms.), diglycerol (1.0 mol.), pentaerythritol (1.25 mols.) and epichlorhydrin (9 mols.) are condensed and reacted as in (18), (25) a soybean monoglyceride (711 gms.) and epichlorhydrin (4 mols.) are condensed and reacted with sodium zincate in dioxane, (26) glycerol phthalate (314 gms.) and epichlorhydrin (7 mols.) are condensed and reacted as in (25) and in (27) bisphenol (228 gms.) and epichlorhydrin (185 gms.) are condensed and reacted with sodium aluminate in dioxane. The products of the examples all contained chlorine. The Specification as open to inspection under Sect. 91 relates to aluminates, zincates and silicates generally and includes in the preparation of complex halohydrins many specified sulphur containing compounds, e.g. 2,21-dihydroxy diethyl sulphide, 2-mercapto ethanol and dihydroxy diaryl sulphones. Complex halohydrins are also made by reacting hydroxyepoxides, e.g. glycidol, with halogen-containing compounds, e.g. organic acid halides such as benzoyl and acetyl chloride, inorganic acid halides such as ACl3 and SOCl2 and compounds such as diethyl and ethyl dichlorosilane. The halogen atoms of the products may be replaced by such groups as OH, SCN, S or NH2 by reaction with such compounds as sodium bicarbonate, thiocyanate or sulphide or ammonia. They may also be reacted with alkali metal phenolates to give resins. This subject-matter does not appear in the Specification as accepted. In two additional examples, (27) bisphenol and epichlorhydrin are condensed in the presence of sodium acetate and the products reacted with sodium aluminate in dioxane, and (29) the epichlorhydrin-glycerol product of (1) is reacted with aqueous caustic soda and bisphenol to give a resinous product.ALSO:Epoxides are made by reacting a basic reacting alkali metal aluminate, silicate or zirconate with a halohydrin in a substantially non-aqueous medium. Typical of many specified alkali metal reactants are Na3AlO3, K2Al2O4, Na2SiO3.5H2O and Na4SiO4 the sodium and potassium salts being preferred. The halohydrins may be aliphatic, cycloaliphatic and aryl-substituted aliphatic compounds containing at least one halogen atom and at least one hydroxy group each of which is attached to a different, preferably adjacent, carbon atom of the molecule. Many halohydrins are specified representative being ethylene chlorhydrin, propylene bromhydrin, 1-chloro-3-hydroxy butane, 1,4-dihydroxy-2,3-dichloro - butane, 1 - chloro - 2 - hydroxy cyclohexane and 1 - bromo - and 1 - iodo - 2-hydroxy-2 phenyl ethane. So-called "complex halohydrins" may also be used. They are made by condensing an epihalohydrin which does not include fluorohydrins with a polyhydric compound such as a polyhydric phenol or alcohol or mixtures thereof in the presence of condensing agents. Many polyhydric compounds are specified representative being ethylene glycol, 1,12-dihydroxy octadecane, 1,4-dihydroxycyclohexane, glycerol, mannitol, polyallyl alcohol, 4,41-dimethylol diphenyl, triglycerol, dimethylolamides, the bis - (beta hydroxyethyl ether) of bisphenol, condensates of alkylene oxides with polyhydric alcohols, fructose, resorcinol, monostearin and glycerol monochlorhydrins. Homologues of epihalohydrins, e.g. 1,4-dichloro-2,3-epoxy-butane may also be used. Epichlorhydrin is preferred. Many condensing agents are specified representative being Friedel-Crafts catalysts, e.g. AlCl3 and BF3 etherates, acid-type catalysts, e.g. HF and H2SO4 and others, e.g. SbCl5. Generally the condensation catalyst is used in up to about 5 per cent, usually less than 1 per cent, of the total reactants and temperatures indicated for this reaction are 25-175 DEG C. advantageously 75-125 DEG C. With high melting and relatively insoluble polyhydric alcohols it is advantage to use a solvent which may be a polyhydric alcohol which itself enters into the reaction. Thus pentaerythritol and poly-pentaerythritol may be reacted in ethylene glycol, diglycerol or trimethylol propane. Solvents for the dehydrohalogenation reaction include hydrocarbons, ketones, ethers and halides and members of these classes are specified, dioxane being preferred. Solvents completely miscible with water facilitate filtration particularly when sodium zincate is used. When complex halohydrins are reacted the epoxide obtained may contain hydroxy and halogen groups. In dehydrohalogenation when sodium aluminate is used temperatures of -25 DEG to 125 DEG C. are specified, preferably 70-105 DEG C. for a reaction time of 1-3 hours, the aluminate is preferably in slight excess and 1-15 per cent or 30 per cent of water is preferably added, with zincates temperatures of -25-125 DEG C. are specified although in general lower temperatures than those employed for aluminates are used, the quantity of salt used is preferably substantially equivalent to the theoretical although with complex halohydrins quantities of from 1/3 to 1 mol. equivalent are indicated depen
GB13838/48A 1947-06-11 1948-05-21 Improvements in epoxide preparation Expired GB679536A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US679536XA 1947-06-11 1947-06-11

Publications (1)

Publication Number Publication Date
GB679536A true GB679536A (en) 1952-09-17

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Application Number Title Priority Date Filing Date
GB13838/48A Expired GB679536A (en) 1947-06-11 1948-05-21 Improvements in epoxide preparation

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Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2862644A1 (en) * 2003-11-20 2005-05-27 Solvay Production of organic compounds comprises producing glycerol from renewable raw materials and producing organic compounds from the glycerol
WO2005054167A1 (en) * 2003-11-20 2005-06-16 Solvay (Société Anonyme) Process for producing dichloropropanol from glycerol, the glycerol coming eventually from the conversion of animal fats in the manufacture of biodiesel
EP1760060A1 (en) * 2003-11-20 2007-03-07 SOLVAY (Société Anonyme) Process for producing dichloropropanol from glycerol
US7557253B2 (en) 2005-05-20 2009-07-07 Solvay (Societe Anonyme) Method for converting polyhydroxylated aliphatic hydrocarbons into chlorohydrins
EP2107075A1 (en) * 2008-04-05 2009-10-07 Cognis IP Management GmbH Emulgators for epoxy resins
US7930651B2 (en) 2007-01-18 2011-04-19 Research In Motion Limited Agenda display in an electronic device
US7939696B2 (en) 2005-11-08 2011-05-10 Solvay Societe Anonyme Process for the manufacture of dichloropropanol by chlorination of glycerol
US8067645B2 (en) 2005-05-20 2011-11-29 Solvay (Societe Anonyme) Process for producing a chlorhydrin from a multihydroxylated aliphatic hydrocarbon and/or ester thereof in the presence of metal salts
US8124814B2 (en) 2006-06-14 2012-02-28 Solvay (Societe Anonyme) Crude glycerol-based product, process for its purification and its use in the manufacture of dichloropropanol
US8197665B2 (en) 2007-06-12 2012-06-12 Solvay (Societe Anonyme) Aqueous composition containing a salt, manufacturing process and use
US8258350B2 (en) 2007-03-07 2012-09-04 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8273923B2 (en) 2007-06-01 2012-09-25 Solvay (Societe Anonyme) Process for manufacturing a chlorohydrin
US8314205B2 (en) 2007-12-17 2012-11-20 Solvay (Societe Anonyme) Glycerol-based product, process for obtaining same and use thereof in the manufacturing of dichloropropanol
US8378130B2 (en) 2007-06-12 2013-02-19 Solvay (Societe Anonyme) Product containing epichlorohydrin, its preparation and its use in various applications
US8471074B2 (en) 2007-03-14 2013-06-25 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8507643B2 (en) 2008-04-03 2013-08-13 Solvay S.A. Composition comprising glycerol, process for obtaining same and use thereof in the manufacture of dichloropropanol
US8536381B2 (en) 2008-09-12 2013-09-17 Solvay Sa Process for purifying hydrogen chloride
US8715568B2 (en) 2007-10-02 2014-05-06 Solvay Sa Use of compositions containing silicon for improving the corrosion resistance of vessels
US8795536B2 (en) 2008-01-31 2014-08-05 Solvay (Societe Anonyme) Process for degrading organic substances in an aqueous composition
US9309209B2 (en) 2010-09-30 2016-04-12 Solvay Sa Derivative of epichlorohydrin of natural origin

Cited By (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8415509B2 (en) 2003-11-20 2013-04-09 Solvay (Societe Anonyme) Process for producing dichloropropanol from glycerol, the glycerol coming eventually from the conversion of animal fats in the manufacture of biodiesel
EP2253609A1 (en) * 2003-11-20 2010-11-24 SOLVAY (Société Anonyme) Process for producing organic compounds from glycerol, the glycerol coming from renewable raw material
EP1752435A1 (en) * 2003-11-20 2007-02-14 SOLVAY (Société Anonyme) Process for producing dichloropropanol from glycerol , the glycerol coming eventualy from the manufacture of biodiesel
US9663427B2 (en) 2003-11-20 2017-05-30 Solvay (Société Anonyme) Process for producing epichlorohydrin
EP1770081A1 (en) * 2003-11-20 2007-04-04 SOLVAY (Société Anonyme) Process for producing dichloropropanol from glycerol , the glycerol coming eventualy from the conversion of animal fats in the manufacture of biodiesel
WO2005054167A1 (en) * 2003-11-20 2005-06-16 Solvay (Société Anonyme) Process for producing dichloropropanol from glycerol, the glycerol coming eventually from the conversion of animal fats in the manufacture of biodiesel
FR2862644A1 (en) * 2003-11-20 2005-05-27 Solvay Production of organic compounds comprises producing glycerol from renewable raw materials and producing organic compounds from the glycerol
EA010337B1 (en) * 2003-11-20 2008-08-29 Солвей (Сосьете Аноним) Process for producing dichloropropanol
EP1760060A1 (en) * 2003-11-20 2007-03-07 SOLVAY (Société Anonyme) Process for producing dichloropropanol from glycerol
EA012736B1 (en) * 2003-11-20 2009-12-30 Солвей (Сосьете Аноним) Process for producing epichlorohydrin and epoxy resins
US8420871B2 (en) 2005-05-20 2013-04-16 Solvay (Societe Anonyme) Process for producing an organic compound
US8519198B2 (en) 2005-05-20 2013-08-27 Solvay (Societe Anonyme) Method for making an epoxide
US7906691B2 (en) 2005-05-20 2011-03-15 Solvay (Societe Anonyme) Method for making chlorohydrin in corrosion-resistant equipment
US7906692B2 (en) 2005-05-20 2011-03-15 Solvay (Societe Anonyme) Method for making a chlorohydrin by chlorinating a polyhydroxylated aliphatic hydrocarbon
US7557253B2 (en) 2005-05-20 2009-07-07 Solvay (Societe Anonyme) Method for converting polyhydroxylated aliphatic hydrocarbons into chlorohydrins
US8389777B2 (en) 2005-05-20 2013-03-05 Solvay (Société Anonyme) Continuous method for making chlorhydrines
US8067645B2 (en) 2005-05-20 2011-11-29 Solvay (Societe Anonyme) Process for producing a chlorhydrin from a multihydroxylated aliphatic hydrocarbon and/or ester thereof in the presence of metal salts
US8106245B2 (en) 2005-05-20 2012-01-31 Solvay (Société Anonyme) Method for preparing chlorohydrin by converting polyhydroxylated aliphatic hydrocarbons
US8344185B2 (en) 2005-05-20 2013-01-01 SOLVAY (Société Anonyme Method for making a chlorhydrine by reaction between a polyhydroxylated aliphatic hydrocarbon and a chlorinating agent
US7893193B2 (en) 2005-05-20 2011-02-22 Solvay (Société Anonyme) Method for making a chlorohydrin
US7615670B2 (en) 2005-05-20 2009-11-10 Solvay (Société Anonyme) Method for making chlorohydrin in liquid phase in the presence of heavy compounds
US8173823B2 (en) 2005-05-20 2012-05-08 Solvay (Société Anonyme) Method for making an epoxide
US8591766B2 (en) 2005-05-20 2013-11-26 Solvay (Societe Anonyme) Continuous process for preparing chlorohydrins
US7939696B2 (en) 2005-11-08 2011-05-10 Solvay Societe Anonyme Process for the manufacture of dichloropropanol by chlorination of glycerol
US8106246B2 (en) 2005-11-08 2012-01-31 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol by chlorination of glycerol
US8124814B2 (en) 2006-06-14 2012-02-28 Solvay (Societe Anonyme) Crude glycerol-based product, process for its purification and its use in the manufacture of dichloropropanol
US7930651B2 (en) 2007-01-18 2011-04-19 Research In Motion Limited Agenda display in an electronic device
US8258350B2 (en) 2007-03-07 2012-09-04 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8471074B2 (en) 2007-03-14 2013-06-25 Solvay (Societe Anonyme) Process for the manufacture of dichloropropanol
US8273923B2 (en) 2007-06-01 2012-09-25 Solvay (Societe Anonyme) Process for manufacturing a chlorohydrin
US8399692B2 (en) 2007-06-12 2013-03-19 Solvay (Societe Anonyme) Epichlorohydrin, manufacturing process and use
US8378130B2 (en) 2007-06-12 2013-02-19 Solvay (Societe Anonyme) Product containing epichlorohydrin, its preparation and its use in various applications
US8197665B2 (en) 2007-06-12 2012-06-12 Solvay (Societe Anonyme) Aqueous composition containing a salt, manufacturing process and use
US8715568B2 (en) 2007-10-02 2014-05-06 Solvay Sa Use of compositions containing silicon for improving the corrosion resistance of vessels
US8314205B2 (en) 2007-12-17 2012-11-20 Solvay (Societe Anonyme) Glycerol-based product, process for obtaining same and use thereof in the manufacturing of dichloropropanol
US8795536B2 (en) 2008-01-31 2014-08-05 Solvay (Societe Anonyme) Process for degrading organic substances in an aqueous composition
US8507643B2 (en) 2008-04-03 2013-08-13 Solvay S.A. Composition comprising glycerol, process for obtaining same and use thereof in the manufacture of dichloropropanol
US8273853B2 (en) 2008-04-05 2012-09-25 Cognis Ip Management Gmbh Emulsifiers for epoxy resins
EP2107075A1 (en) * 2008-04-05 2009-10-07 Cognis IP Management GmbH Emulgators for epoxy resins
US8536381B2 (en) 2008-09-12 2013-09-17 Solvay Sa Process for purifying hydrogen chloride
US9309209B2 (en) 2010-09-30 2016-04-12 Solvay Sa Derivative of epichlorohydrin of natural origin

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