EP4314111A1 - Nouveaux polyéthers à base de 2,3-époxybutane et procédé pour leur préparation - Google Patents

Nouveaux polyéthers à base de 2,3-époxybutane et procédé pour leur préparation

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Publication number
EP4314111A1
EP4314111A1 EP22714181.9A EP22714181A EP4314111A1 EP 4314111 A1 EP4314111 A1 EP 4314111A1 EP 22714181 A EP22714181 A EP 22714181A EP 4314111 A1 EP4314111 A1 EP 4314111A1
Authority
EP
European Patent Office
Prior art keywords
epoxybutane
polyether
carbon atoms
trans
mol
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.)
Pending
Application number
EP22714181.9A
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German (de)
English (en)
Inventor
Frank Schubert
Sarah OTTO
Daniela HERMANN
Heike Hahn
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Evonik Operations GmbH
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Evonik Operations GmbH
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Filing date
Publication date
Application filed by Evonik Operations GmbH filed Critical Evonik Operations GmbH
Publication of EP4314111A1 publication Critical patent/EP4314111A1/fr
Pending legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2642—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds characterised by the catalyst used
    • C08G65/2645—Metals or compounds thereof, e.g. salts
    • C08G65/2663—Metal cyanide catalysts, i.e. DMC's
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2603—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen
    • C08G65/2606—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen containing hydroxyl groups
    • C08G65/2609—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen containing hydroxyl groups containing aliphatic hydroxyl groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2696—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds characterised by the process or apparatus used

Definitions

  • the invention relates to an alkoxylation process for the production of new polyethers based on 2,3-epoxybutane and polyethers that can be produced using this process.
  • polyether alcohols often simply referred to as polyethers for short, are mainly produced in an alkoxylation reaction of propylene oxide and ethylene oxide and have been known for a long time.
  • other epoxy monomers such as 1,2-butylene oxide, isobutylene oxide, styrene oxide, 1,2-octene oxide, 1,2-decene oxide, 1,2-dodecene oxide or, for example, cyclohexene oxide.
  • the nature of the monomers used in the alkoxylation reaction and the chain initiator, the copolymerization of different epoxide monomers and the choice of the catalyst in the alkoxylation reaction are of crucial importance for the chemical composition and the application properties of the final alkoxylation products.
  • the catalysis and reaction conditions in the alkoxylation depend on the choice of the respective chain starter, the monomers and, for example, the desired molar mass and the product purity. The relationships are described in the literature and known to those skilled in the art.
  • GB 1147791 discloses the production of partially crystalline polyethers by acid-catalyzed homopolymerization of trans-2,3-epoxybutane at low temperatures of -10°C to 30°C in CH2Cl2. Crystalline poly(trans-2,3-epoxybutane) is obtained according to US Pat. No. 3,356,620 using a trialkylaluminum catalyst at 0° C. in toluene.
  • poly(trans-2,3-epoxybutane) and poly(c/s-2,3-epoxybutane) are obtained by alkoxylation of the isomerically pure 2,3-epoxybutanes in the presence of dialkylaluminum halides and dialkylaluminum alkoxides 30°C in diethyl ether.
  • the polyethers have different properties depending on the 2,3-epoxybutane isomer.
  • the crystalline products have different Melting points and solubility properties. It is recommended to use isomerically pure cis or trans
  • Organoaluminum catalysts for the alkoxylation of 2,3-epoxybutane are also used in US Pat. No. 3,280,045.
  • Vandenberg Journal of Polymer Science (1960), 47, 489-91
  • polyethers with very different physical properties, such as the tendency to crystallize, melting points and solubility behavior, are obtained .
  • US 20130248756 describes mixtures of polyethers and abrasive particles, the polyether being produced by means of DMC catalysis and in block form from an EO block and a
  • 2.3-epoxybutane block is constructed. Glycerin and sorbitol are mentioned as starters.
  • montmorillonite is used as a catalyst for the alkoxylation of mixtures of 2,3-epoxybutane and 1,2-butylene oxide.
  • DE 2246598 describes copolymers of 1-butylene oxide, propylene oxide and 2,3-epoxybutane, which are prepared in an alkaline-catalyzed alkoxylation reaction and then linked to one another via a Williamson etherification with CH2Cl2. According to US Pat. No.
  • C/s-2,3-epoxybutane is polymerized with ethylene oxide in the presence of triethylaluminum.
  • US 20120016048 covers polyether polyols based on natural oils for PU foams produced by means of DMC catalysis. 2,3-Epoxybutane is mentioned as a possible monomer.
  • the process disclosed in WO 2011135027 relates to the DMC-catalyzed production of polyols from fatty acid esters by an alkoxylation reaction of ethylene oxide with another alkylene oxide, e.g. 2,3-epoxybutane.
  • starter polyols such as glycerol and sorbitol are first acidified and then alkoxylated using DMC catalysis.
  • the possible monomers that can be used also include 2,3-epoxybutane.
  • NL 6413172 covers PU foams made from polyols, which are produced by blockwise alkoxylation of ethylene oxide and other alkylene oxides with >3 carbon atoms. KOH is mentioned as a catalyst.
  • the object of the present invention was to overcome at least one disadvantage of the prior art and to provide an improved industrially applicable alkoxylation process for preparing polyethers based on 2,3-epoxybutane. It is also the object of the invention to provide a new class of polyether structures based on 2,3-epoxybutane which can be produced by this process.
  • the process according to the invention opens up the homopolymerization of 2,3-epoxybutane and the copolymerization of 2,3-epoxybutane with other epoxide compounds in a simple and reproducible manner for the first time.
  • an alkoxylation process for the production of polyethers based on c/s-2,3-epoxybutane and trans-2,3-epoxybutane solves the above problem, which comprises the following steps: a) Reaction of at least one starter compound (A) in the presence of a double metal cyanide catalyst (B) with 2,3-epoxybutane (C) and optionally further epoxide monomers (D) to form at least one polyether (E);
  • the process according to the invention also comprises the following step: b) reaction of the at least one polyether (E) with at least one end-capping reagent (F) to form at least one end-capped polyether (G).
  • isomer mixtures of c/s-2,3-epoxybutane and trans-2,3-epoxybutane in particular can be alkoxylated with ring opening in the presence of, preferably, zinc/cobalt double metal cyanide catalysts.
  • the process of the invention grants the synthetic freedom to alkoxylate any cis-ltrans-2,3-epoxybutane mixtures alone (homopolymerizing) or in combination with other epoxy compounds (D), the oxybutylene units resulting from epoxy ring opening being both terminal and isolated, block-like cumulatively as well as randomly interspersed in the polyoxyalkylene chain of the reaction product.
  • FIG 1 and FIG 2 short description of the figures FIG 1 and FIG 2:
  • Example 1 shows the GPC curve of a polyether (E) of the formula (2) based on cis/trans-2,3-epoxybutane produced by means of alkaline catalysis, as described in Example 1 in the experimental part.
  • the signal intensity (norm.) measured by the RI detector is plotted against the molar mass in Dalton.
  • the number-average molar mass M n , the weight-average molar mass M and the polydispersity (M /M n ) are preferably determined by means of gel permeation chromatography (GPC), as described in the examples, unless explicitly stated otherwise.
  • Range specifications include the range limits X and Y, unless otherwise stated.
  • Formula (2) below describes compounds or radicals which are built up from repeating units, such as repeating fragments, blocks or monomer units, and can have a molecular weight distribution.
  • the frequency of the repeating units is indicated by indices.
  • the indices used in the formulas are to be regarded as statistical averages (number averages) unless explicitly stated otherwise.
  • the index numbers used and the value ranges of the specified indices are understood to be mean values of the possible statistical distribution of the structures actually present and/or their mixtures.
  • the various fragments or repeating units of the compounds described in formula (2) below can be randomly distributed.
  • Statistical distributions are built up in blocks with any number of blocks and any sequence or are subject to a randomized distribution, they can also be built up alternatingly, or also form a gradient via the chain, if one exists, in particular they can also form all mixed forms , where groups of different distributions may follow one another. All permutations of repeating units are included in the formulas below.
  • compounds which can have different units more than once, these can be both disordered, e.g. statistically distributed, or ordered occurrences in these compounds.
  • the data on the number or relative frequency of units in such compounds are to be understood as the average (number average) averaged over all corresponding compounds.
  • Special implementations can result in the statistical distributions being restricted by the embodiment. For all areas that are not affected by the restriction, the statistical distribution does not change.
  • a first object of the invention is therefore a process for preparing polyethers based on c/s-2,3-epoxybutane and trans-2,3-epoxybutane, comprising the steps: a) reacting at least one starter compound (A) in the presence one
  • starter compounds are substances which form the beginning (start) of the polyether to be prepared, which is obtained by the inventive addition of epoxide-functional monomers (C) and possibly further comonomers (D).
  • starting compounds (A) for the alkoxylation reaction preferably all compounds of the formula (1)
  • R is a saturated or unsaturated, linear or branched radical having 1 to 500 carbon atoms, preferably having 2 to 250 carbon atoms, particularly preferably having 3 to 100 carbon atoms, in which the carbon chain can be interrupted by heteroatoms such as oxygen, nitrogen or silicon, a is an integer from 1 to 8, preferably from 1 to 6, particularly preferably from 1 to 4 and very particularly preferably from 1 to 3.
  • the starter compounds (A) can be used alone or in any mixture and are preferably selected from the group of alcohols, polyether oils or phenols.
  • the OH-functional starter compounds of the formula (1) used are preferably compounds with molar masses of from 30 to 15000 g/mol, in particular from 50 to 5000 g/mol.
  • Illustrative of compounds of formula (1) are allyl alcohol, allyloxyethanol, allyloxypropanol, methallyl alcohol, butanol, 1-hexen-6-ol, hexanol, octanol, 3,5,5-trimethylhexanol, isononanol, decanol, dodecanol, tetradecanol, hexadecanol, stearyl alcohol , 2-ethylhexanol, cyclohexanol, benzyl alcohol, trimethylolpropane diallyl ether, trimethylolpropane monoallyl ether, glycerol diallyl ether, glycerol monoallyl ether, diethylene glycol monomethyl ether, diethylene glycol monobut
  • any compounds with phenolic OH functions are suitable. These include, for example, phenol, alkyl and aryl phenols, bisphenol A and/or novolaks.
  • Zinc/cobalt DMC catalysts are preferably used, in particular those which contain zinc hexacyanocobaltate(III).
  • the DMC catalysts described in US Pat. No. 5,158,922, US 20030119663, WO 01/80994 are preferably used.
  • the catalysts can be amorphous or crystalline.
  • the catalyst concentration is from >0 wppm to 1000 wppm, more preferably from >0 wppm to 700 wppm, most preferably from >10 wppm to 500 wppm based on the total mass of the resulting products (E) "wppm" is equal to parts by weight per million.
  • the catalyst is preferably metered into the reactor only once. This should preferably be clean, dry and free from basic contaminants that could inhibit the DMC catalyst.
  • the amount of catalyst should preferably be adjusted so that there is sufficient catalytic activity for the process.
  • the catalyst can be metered in as a solid or in the form of a catalyst suspension. If a suspension is used, the starter is particularly suitable as a suspending agent.
  • the catalyst In order to start the D MC-catalyzed reaction, it can be advantageous to first mix the catalyst with a portion of the at least one epoxy-functional compound (C) or (D), preferably selected from the group of alkylene oxides, in particular with 2,3-epoxybutane. Activate propylene oxide and/or ethylene oxide. After the alkoxylation reaction has started, the continuous addition of monomer can be started.
  • the reaction temperature is preferably from 50°C to 180°C, more preferably from 60°C to 150°C, and most preferably from 80°C to 140°C.
  • the internal pressure of the reactor is preferably from 0.02 bar to 100 bar, more preferably from 0.05 bar to 20 bar, most preferably from 0.1 bar to 10 bar (absolute).
  • a DMC-catalyzed reaction is carried out at a temperature of 80°C to 140°C and a pressure of 0.1 bar to 10 bar.
  • the monomer 2,3-epoxybutane exists in the form of the two isomers c/s-2,3-epoxybutane (c/s-2-butylene oxide) and trans-2,3-epoxybutane (trans-2-butylene oxide). According to the prior art, the two stereoisomers differ in their reactivity and lead to products with different properties.
  • c/s-2,3-epoxybutane and trans-2,3-epoxybutane are fed simultaneously as an isomer mixture to the reaction mixture of starter (A) and catalyst (B), the isomer mixture preferably making up 10% up to 95% of trans-2,3-epoxybutane and 5% to 90% of c/s-2,3-epoxybutane, preferably 20% to 85% of trans-2,3-epoxybutane and 15% to 80% c/s-2,3-epoxybutane, particularly preferably 40% to 80% of trans-2,3-epoxybutane and 20% to 60% of c/s-2,3-epoxybutane, particularly preferably 60% to 75% % is trans-2,3-epoxybutane and 25% to 40% c/s-2,3-epoxybutane, and the sum of trans-2,3-epoxybutane and c/s-2,3-epoxybutane, and the sum of trans-2,3-e
  • the mixture of trans-2,3-epoxybutane and c/s-2,3-epoxybutane used according to the invention has a purity of >90% by weight, preferably >94% by weight, according to GC analysis preferably >96% by weight and very particularly preferably >98% by weight.
  • the water content of the mixture of trans-2,3-epoxybutane and c/s-2,3-epoxybutane used according to the invention, determined by the Karl Fischer method, is preferably ⁇ 1.5% by weight, more preferably ⁇ 1.0% by weight. -%, more preferably ⁇ 0.6% by weight, very preferably ⁇ 0.4% by weight and most preferably ⁇ 0.2% by weight.
  • the proportion of C4 hydrocarbons such as butane, 1-butene, isobutane, c/s-2-butene, trans-2- is preferably ⁇ 3% by weight, preferably ⁇ 2% by weight, particularly preferably ⁇ 1% by weight, very particularly preferably ⁇ 0.5% by weight and most preferably ⁇ 0.2% by weight.
  • a proportion of other possible secondary components that may be contained in the mixture of trans-2,3-epoxybutane and c/s-2,3-epoxybutane, which, for example, originate from the production process, such as Alcohols or chlorinated hydrocarbons, according to GC analysis, is preferably ⁇ 3% by weight, preferably ⁇ 2% by weight, particularly preferably ⁇ 1% by weight, very particularly preferably ⁇ 0.5% by weight and most preferably ⁇ 0.2% by weight.
  • the reaction is an alkoxylation reaction, ie a polyaddition of alkylene oxides onto the at least one hydroxy-functional starter (A).
  • the reaction according to the invention of the mixture of trans-2,3-epoxybutane and c/s-2,3-epoxybutane can be carried out together with other epoxide monomers (D) from the group of alkylene oxides or else glycidyl compounds.
  • the at least one further epoxy-functional compound is from the group of alkylene oxides, more preferably from the group of alkylene oxides having 2 to 18 carbon atoms, even more preferably from the group of alkylene oxides having 2 to 8 carbon atoms, most preferably from the group consisting of ethylene oxide , propylene oxide, 1-butylene oxide, isobutylene oxide and/or styrene oxide; and/or that the at least one further epoxy-functional compound from the group of glycidyl compounds, more preferably from the group of monofunctional glycidyl compounds, most preferably from the group consisting of phenyl glycidyl ether, o-cresyl glycidyl ether, tert-butylphenyl glycidyl ether, allyl glycidyl ether, butyl glycidyl ether, 2-ethylhexyl glycidyl ether, Ci 2 /C
  • the monomers (C) and (D) can optionally be added individually in pure form, alternately one after the other in any metering order, but also mixed at the same time.
  • the sequence of the monomer units in the resulting polyether chain is therefore subject to a blockwise distribution or a statistical distribution or a gradual distribution in the end product.
  • the process according to the invention builds up polyether chains on the starter (A), which are distinguished in that they can be produced in a targeted and reproducible manner in terms of structural build-up and molar mass.
  • the sequence of the monomer units can be varied within wide limits by the order in which they are added.
  • the molar masses of the resulting polyethers can be varied within wide limits by the process according to the invention and can be controlled in a targeted and reproducible manner via the molar ratio of the added monomers (C) and (D) in relation to the OH groups of the at least one starter (A).
  • the reaction conditions are preferably selected in such a way that the side reactions known from alkaline catalysis are largely suppressed. These include the rearrangements of 2,3-epoxybutane and the elimination of water from the terminal tertiary hydroxyl group of the growing polyether chain.
  • the reactor partially filled with the starter and the DMC catalyst (B) is rendered inert, for example with nitrogen. This is done, for example, by repeatedly evacuating and supplying nitrogen in alternation. It is advantageous to evacuate the reactor to below 200 mbar after the final injection of nitrogen.
  • the addition of the first quantity of epoxide monomer thus preferably takes place in the evacuated reactor.
  • the monomers are preferably metered in with stirring and, if necessary, cooling in order to dissipate the heat of reaction liberated and to maintain the preselected reaction temperature.
  • the at least one hydroxy-functional compound (A) serves as the starter, or a polyether (E) already prepared by the process according to the invention can also be used as the starter.
  • the reaction can be carried out in a suitable solvent, for example in order to reduce the viscosity.
  • an after-reaction preferably follows to complete the conversion.
  • the after-reaction can be carried out, for example, by further reaction under reaction conditions (ie maintaining the temperature, for example) without adding starting materials.
  • the D MC catalyst usually remains in the reaction mixture.
  • Unreacted epoxides and any other volatile components can be removed after the reaction by vacuum distillation, steam or gas stripping or other deodorization methods. Finally, the finished product is preferably filtered at ⁇ 100 °C in order to remove any turbid matter that may be present.
  • stabilizers or antioxidants during the process according to the invention for stabilizing the products.
  • Suitable for this purpose are, for example, the sterically hindered phenols known to the person skilled in the art, commercially available, for example, as Anox® 20, Irganox® 1010 (BASF), Irganox® 1076 (BASF) and Irganox® 1135 (BASF).
  • the at least one polyether (E) based on 2,3-epoxybutane (C) is reacted with at least one endcapping reagent (F) to form at least one polyether (G) containing endcapped polyether radicals.
  • the terminal hydroxy groups of the polyethers (E) are further converted into ester, ether, urethane and/or carbonate groups.
  • polyethers are known to those skilled in the art, such as esterification with carboxylic acids or carboxylic acid anhydrides, in particular acetylation using acetic anhydride, etherification with halogenated hydrocarbons, in particular methylation with methyl chloride according to the Williamson ether synthesis principle, urethanization by Reaction of the OH groups with isocyanates, in particular with monoisocyanates such as stearyl isocyanate, and carbonation by reaction with dimethyl carbonate and diethyl carbonate.
  • the present invention also relates to polyethers (E) of the formula (2) based on 2,3-epoxybutane (C), as can be prepared by the process according to the invention,
  • R is a saturated or unsaturated, linear or branched radical having 1 to 500 carbon atoms, preferably having 2 to 250 carbon atoms, particularly preferably having 3 to 100 carbon atoms, in which the carbon chain can be interrupted by heteroatoms such as oxygen, nitrogen or silicon, a is an integer from 1 to 8, preferably from 1 to 6, particularly preferably from 1 to 4 and very particularly preferably from 1 to 3,
  • R 1 are each independently a monovalent hydrocarbon radical having 1 to 16
  • each is carbon atoms; preferably each is independently an alkyl radical having 1 to 16 carbon atoms or a phenyl radical; most preferably each independently is methyl, ethyl or phenyl;
  • R 2 is a group of the formula -CH2-OR 3 ;
  • R 3 are each independently a monovalent hydrocarbon radical with 3 to 18
  • each is independently an allyl group, a butyl group, an alkyl group having 8 to 15 carbon atoms or a phenyl group which may be substituted with monovalent groups selected from hydrocarbon groups having 1 to 4 carbon atoms; most preferably a tert-butylphenyl radical or an o-cresyl radical;
  • each R 4 is independently a monovalent organic radical having 1 to 18 carbon atoms or hydrogen, preferably hydrogen; m, n, p and q are each independently from 0 to 300, preferably from 0 to 200, most preferably from 0 to 100, o is a number from 1 to 300, preferably from 1 to 200, particularly preferably from 2 to 150, very particularly preferably from 3 to 100, with the proviso that the sum of m, n, o, p and q is greater than 1, preferably greater than 5, most preferably greater than 10.
  • radicals R 1 , R 2 , R 3 and R 4 can each independently be linear or branched, saturated or unsaturated, aliphatic or aromatic, substituted or unsubstituted.
  • the repeating units resulting from the ring opening of c/s-2,3-epoxybutane and trans-2,3-epoxybutane are contained o-fold in the polyether chain of the formula (2).
  • the radical R corresponds to the radical of the starter compound (A) defined in formula (1).
  • R is a radical derived from the starter compounds of the formula (1), such as allyl alcohol, allyloxyethanol, allyloxypropanol, methallyl alcohol, butanol, 1-hexen-6-ol, hexanol, octanol, 3,5,5-trimethylhexanol, isononanol , decanol, dodecanol, tetradecanol, hexadecanol, stearyl alcohol, 2-ethylhexanol, cyclohexanol, benzyl alcohol, trimethylolpropane diallyl ether, trimethylolpropane monoallyl ether, glycerol diallyl ether, glycerol monoallyl ether, diethylene glycol monomethyl ether, diethylene glycol monobutyl ether, dipropylene glycol monomethyl ether, dipropylene glycol monobutyl ether, ethylene glycol,
  • nolic OH functions include, for example, phenol, alkyl and aryl phenols, bisphenol A and/or novolaks.
  • R is preferably an organic radical which differs from allyl alcohol, allyloxyethanol, allyloxypropanol, methallyl alcohol, butanol, dipropylene glycol, glycerol and/or polyether oils with 1-8 hydroxyl groups and molecular weights of 50 to 5000 g/mol, which in turn have been previously prepared by alkoxylation, derives.
  • Each R 5 is independently alkyl or alkenyl of 1 to 18 carbon atoms, preferably 1 to 10 carbon atoms, most preferably methyl.
  • R 6 is each independently an alkyl or an aryl radical having 1 to 18 carbon atoms, preferably having 6 to 18 carbon atoms.
  • R 7 is each independently an alkyl radical having 1 to 18 carbon atoms, preferably having 1 to 2 carbon atoms.
  • the proportion of the repeating units listed in formula (2) and originating from c/s-2,3-epoxybutane and trans-2,3-epoxybutane with the index o is preferably > 0% to 100%, more preferably from 10% to 100%, even more preferably from 20% to 100%, most preferably from 25% to 80%, the proportion being according to [o/(m+n+o+p+q )j * 100% calculated.
  • the repeating units with the indices m, n, o, p and q are randomly distributed over the polyether chain. All indicated index values are therefore to be understood as mean values.
  • the number-average molar mass M n , weight-average molar mass M and polydispersity of the polyether (E) are arbitrary.
  • the number average molar mass M n of the polyether (E) is from 200 g/mol to 30000 g/mol, more preferably from 300 g/mol to 10000 g/mol, most preferably from 400 g/mol to 5000 g/mol .
  • the polydispersity (M /M n ) of the polyethers (E) can be varied within wide ranges and is preferably from 1.05 to 5, more preferably from 1.1 to 4, particularly preferably from 1.15 to 3.
  • C C double bonds introduced into the polyether (E) by unsaturated starters (A) such as allyl alcohol or other unsaturated epoxy monomers (D) such as allyl glycidyl ether are not included.
  • the unsaturated compounds formed by unavoidable side reactions of 2,3-epoxybutane cannot be removed from the finished polyether (E) and are therefore an inseparable part of the polyether (E) according to the invention.
  • GPC measurements to determine the polydispersity (M /M n ), the weight-average molar mass (M ) and the number-average molar mass (M n ) of the polyethers (E) were carried out under the following measurement conditions: column combination SDV 1000/10000 A (length 65 cm ), temperature 30 °C, THF as mobile phase, flow rate 1 ml/min, sample concentration 10 g/l, RI detector, evaluation against polypropylene glycol standard.
  • the acid number was determined using a titration method based on DIN EN ISO 2114.
  • Hydroxyl numbers were determined using the DGF C-V 17 a (53) method of the German Society for Fat Science. The samples were acetylated with acetic anhydride in the presence of pyridine and the consumption of acetic anhydride was determined by titration with 0.5N potassium hydroxide solution in ethanol against phenolphthalein.
  • part of the sample is analyzed directly using GC/TCD. This is carried out in a gas chromatograph equipped with a split/splitless injector, a capillary column and a thermal conductivity detector under the following conditions:
  • Carrier gas Helium, constant flow, 2 mL/min
  • Carrier gas hydrogen, constant flow, 2 mL/min
  • Temperature program condition 2 min at 50 °C - 200 °C at 5 °C/min, then 200 °C - 300 °C at 25 °C/min, then 5 min at 300 °C Detector: FID at 310 °C
  • the cis/trans isomer ratio is determined using the area percentages.
  • the turbidity values were determined using a 2100AN IS Lange turbidity photometer, ISO, 230 V from Hach, an 870 nm LED light source and 11 mm round cuvettes.
  • the melting points and enthalpies were determined using the Discovery DSC from TA Instruments. The measurement was carried out in an aluminum T Zero crucible and a weight of 15 mg under nitrogen, at a temperature of 0-150 °C and a ramp rate of 5.0 °C per minute.
  • the proportion of unsaturated compounds, based on the amount of 2,3-epoxybutane used, is caused, for example, by side reactions of 2,3-epoxybutane and/or elimination of water from terminal tertiary OH groups.
  • the determination was made using 13 C-NMR spectroscopy. A Bruker Avance 400 NMR spectrometer was used. For this purpose, the samples were dissolved in deuterochloroform.
  • the content of unsaturated compounds is defined as the proportion of unsaturated compounds based on the amount of 2,3-epoxybutane * 100% used.
  • the content is determined by determining the number of moles of double bonds based on 1 mole of starter using 13 C-NMR and dividing this by the number of moles of 2,3-epoxybutane based on 1 mole of starter specified by the recipe, multiplied by 100 %.
  • the proportion of unsaturated compounds based on the amount of 2,3-epoxybutane used does not reflect the total amount of the proportion of unsaturated compounds.
  • the product was cooled to below 80°C, neutralized with lactic acid and 500 ppm Irganox ® 1135 was added. 168.3 g of the liquid polyether, which was brown at room temperature, were obtained.
  • the GPC curve shows a multimodal distribution and high proportions of low-molecular unsaturated compounds, see figure FIG 1.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 50/50 w/w (GC/FID) Purity: > 98%
  • Example 2 alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane mixture (according to the invention)
  • the GPC curve of the product shows a monomodal distribution, see figure FIG 2.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 50/50 w/w (GC/FID)
  • the product is crystalline.
  • the DSC shows a melting peak at 48.4 °C.
  • the enthalpy of fusion is 19.29 J/g.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 0/100 w/w Purity: > 98%
  • Example 4 Alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane mixture
  • the product is only slightly crystalline. DSC shows a small melting peak at 43.4 °C. The enthalpy of fusion is 3.05 J/g.
  • composition of the c/s/?rans-2,3-epoxybutane used cis/trans ratio: 12/88 w/w (GC/FID)
  • Example 5 Alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane mixture
  • composition of the 2,3-epoxybutane used cis/trans ratio: 50/50 w/w (GC/FID)
  • the product is only slightly crystalline. DSC shows a small melting peak at 48.1 °C. The enthalpy of fusion is 7.12 J/g.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 0/100 w/w Purity: > 98%
  • Example 7 Alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane mixture
  • a polyether (E) of the formula (2) based on c/s/?rans-2,3-epoxybutane 73.0 g of a butanol-started polyether having a molecular weight of 385 g/mol were prepared in a 3 liter autoclave and 0.09 g of DMC catalyst under nitrogen. The mixture was then heated to 130° C. with stirring and the reactor was evacuated to an internal pressure of 30 mbar in order to remove any volatile constituents by distillation. 32.8 g of propylene oxide were metered in with stirring and cooling.
  • the product is only slightly crystalline.
  • the DSC shows a small melting peak at 43.8 °C.
  • the enthalpy of fusion is only 1.65 J/g.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 12/88 w/w (GC/FID) Purity: >98%
  • Example 8 Alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane mixture
  • composition of the 2,3-epoxybutane used cis/trans ratio: 50/50 w/w (GC/FID)
  • Example 9 Alkoxylation with Zn/Co catalyst (DMC) and a trans-2,3-
  • composition of the 2,3-epoxybutane used cis/trans ratio: 0/100 w/w (GC/FID)
  • Example 10 Alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane/propylene oxide mixture
  • the significantly lower turbidity value compared to Example 9 shows the lower crystallinity of the product obtained by using an isomeric mixture of cis- and trans-2,3-epoxybutane.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 12/88 w/w (GC/FID) Purity: >98%
  • step c) 643.2 g of the in step b) polyether produced and 1.65 g of potassium methylate under nitrogen. It was then heated to 115° C. with stirring and the reactor up to an internal pressure evacuated to 30 mbar in order to remove any volatile ingredients by distillation. 79.0 g of ethylene oxide were metered in continuously with stirring and cooling at 115° C. and a maximum internal reactor pressure of 3.0 bar (absolute) over a period of 2.5 hours. The after-reaction at 115° C. for one hour was followed by degassing.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 33/67 w/w (GC/FID)
  • Example 12 Alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane mixture. Preparation of a bifunctional polyether
  • composition of the 2,3-epoxybutane used cis/trans ratio: 33/67 w/w (GC/FID)
  • Example 13 Alkoxylation with Zn/Co catalyst (DMC) and a cis/trans-2,3-epoxybutane mixture
  • an allyl-functional polyether (E) of the formula (2) based on cis-rans-2,3-epoxybutane 50.2 g of allyl alcohol and 0.28 g of DMC catalyst were placed under nitrogen in a 3 liter autoclave. With stirring, the reactor is evacuated to an internal pressure of 100 mbar and the contents are then heated to 130.degree. 50.4 g of propylene oxide was added with stirring and cooling. After a noticeable drop in pressure, a further 150.0 g of propylene oxide and then 917.8 gc/s/frans-2,3-epoxybutane were added continuously with stirring and cooling at 130° C. and a maximum internal reactor pressure of 3.0 bar (absolute) for three hours dosed.
  • composition of the 2,3-epoxybutane used cis/trans ratio: 33/67 w/w (GC/FID)

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  • Chemical Kinetics & Catalysis (AREA)
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  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Toxicology (AREA)
  • Polyethers (AREA)

Abstract

L'invention concerne un procédé de préparation de polyéthers à base de cis-2,3-époxybutane et de trans-2,3-époxybutane, comprenant les étapes consistant à a) faire réagir au moins un composé de départ (A) en présence d'un catalyseur à base de cyanure bimétallique (B) avec du 2,3-époxybutane (C) et éventuellement d'autres monomères époxydes (D) pour former au moins un polyéther (E) ; et éventuellement b) faire réagir ledit au moins un polyéther (E) avec au moins un réactif de coiffage terminal (F) pour former au moins un polyéther à extrémité coiffée (G).
EP22714181.9A 2021-03-26 2022-03-14 Nouveaux polyéthers à base de 2,3-époxybutane et procédé pour leur préparation Pending EP4314111A1 (fr)

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Publication number Priority date Publication date Assignee Title
US3065187A (en) 1960-07-26 1962-11-20 Hercules Powder Co Ltd Poly(2, 3-epoxybutane)
NL6413172A (fr) 1963-11-14 1965-05-17
US3280045A (en) 1964-02-26 1966-10-18 Hercules Inc Process for polymerizing epoxides with an alkyl aluminum compound
US3272889A (en) 1964-05-27 1966-09-13 Hercules Inc Epoxide copolymers
US3356620A (en) 1964-09-17 1967-12-05 Hercules Inc Process for preparing crystalline poly
GB1147791A (en) 1965-08-16 1969-04-10 Ici Ltd Polyethers
JPS512085B2 (fr) 1971-09-23 1976-01-23
US5158922A (en) 1992-02-04 1992-10-27 Arco Chemical Technology, L.P. Process for preparing metal cyanide complex catalyst
US5426174A (en) 1992-12-08 1995-06-20 Arco Chemical Technology, L.P. Hydroxy-functionalized polyoxyalkylene ether compositions derived from mixtures of C4 epoxides
DE10008630A1 (de) 2000-02-24 2001-09-06 Basf Ag Verfahren zur Herstellung von Polyetherpolyolen in Gegenwart eines Multimetallcyanidkomplex-Katalysators
HU226653B1 (en) 2000-04-20 2009-05-28 Bayer Ag Method for producing double metal cyanide (dmc) catalysts
DE10122019A1 (de) 2001-05-07 2002-11-14 Bayer Ag Doppelmetallcyanid-Katalysatoren für die Herstellung von Polyetherpolyolen
US20080021191A1 (en) 2006-07-20 2008-01-24 Reese Jack R High water content tolerant process for the production of polyethers
MX2012012596A (es) 2010-04-30 2013-05-06 Basf Se Polioles de polieter, proceso para preparar polioles de polieter y su uso para producir poliuretanos.
US8598248B2 (en) 2010-07-16 2013-12-03 Bayer Materialscience Llc Flexible polyurethane foams made from alkoxylated natural oil
EP2649144A4 (fr) 2010-12-10 2014-05-14 Basf Se Composition de polissage aqueuse et procédé de polissage mécano-chimique de substrats contenant un diélectrique en oxyde de silicium et des films en polysilicium

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