Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
  • C07C41/01—Preparation of ethers
  • C07C41/34—Separation; Purification; Stabilisation; Use of additives
  • C07C41/44—Separation; Purification; Stabilisation; Use of additives by treatments giving rise to a chemical modification
• • 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
  • C08G65/30—Post-polymerisation treatment, e.g. recovery, purification, drying
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
  • C07C41/01—Preparation of ethers
  • C07C41/34—Separation; Purification; Stabilisation; Use of additives

Definitions

• the present invention relates to the production of polyether polyols, and more in particular to the neutralization and removal of the base catalyst used in the production of polyether polyols.
• polyether polyols typically involve reacting a starting compound having a plurality of active hydrogen atoms with one or more alkylene oxides in the presence of a base catalyst, preferably a strong base such as potassium hydroxide.
• Suitable starting compounds are a.o. polyfunctional alcohols, typically comprising 2 to 6 hydroxyl groups. Examples of such alcohols are glycol, e.g. diethylene glycol, dipropylene glycol, glycerol, di- and poly glycerols, pentaerythritol, trimethylolpropane, diethanolamine, triethanolamine, sorbitol, mannitol, etc.
• Alkylene oxides used are typically ethylene oxide, propylene oxide, butylene oxide or mixtures of two or more of these.
• the polyether polyol may e.g. be used as a raw material in polyurethane production, where the polyol is, in general, reacted with a polyisocyanate component, such as methylene diphenyl diisocyanate (MDI) or toluene diisocyanate (TDI).
• a polyisocyanate component such as methylene diphenyl diisocyanate (MDI) or toluene diisocyanate (TDI).
• the water is subsequently removed by distillation and the reaction mixture is filtered.
• a drawback of this method is that the metal salt hydrates must be prepared in a separate process step and that the amount of filtration residue is increased by this addition.
• the present invention aims to provide a process for the preparation of polyether polyols, wherein the neutralization of the reaction medium and removal of the base catalyst (also referred to as alkaline catalyst or alkaline polymerization catalyst), catalyzing the reaction between the alkene oxide (epoxide) and the starting polyol or the alcohol groups of the polyether polyol, is optimized with regard to particle size, particle size distribution and/or process time.
• the neutralization of the reaction medium and removal of the base catalyst also referred to as alkaline catalyst or alkaline polymerization catalyst
• catalyzing the reaction between the alkene oxide (epoxide) and the starting polyol or the alcohol groups of the polyether polyol is optimized with regard to particle size, particle size distribution and/or process time.
• a method to provide polyether polyols comprises the steps of
• the polyether polyol mixture may comprise 0.00 to 0.08 w% water, said w% being expressed over the total weight of the polyether polyol mixture .
• the water and the acid may be added separately, or the acid and water may be added as an aqueous acid solution.
• the acid and water may be added as such.
• the acid may be added to the crude polyether polyol as an aqueous acid solution.
• the base catalyst used to catalyze the reaction between the alkylene oxides and the alcohol groups during the polymerization of the polyether polyol is typically a strong base such as an alkali metal hydroxide, e.g. sodium hydroxide, potassium hydroxide or cesium hydroxide, or mixtures thereof, whereas most preferably potassium hydroxide is used.
• an amount in the range of 0.05 to 2 w%, e.g. in the range of 0.10 to 0.35 w%, and most preferred an amount in the range of 0.13 to 0.29 w% of catalyst, said w% based on the total weight of the polyether polyol to be prepared in the crude polyether polyol mixture is used in the reaction mixture during the polymerization reaction.
• the base catalyst is potassium hydroxide, sodium hydroxide, cesium hydroxide or combinations thereof.
• the crude polyether polyol mixture is provided by catalytically polymerizing a starting compound with alkylene oxides (also referred to as epoxides).
• Suitable starting compounds are a.o. polyfunctional alcohols, typically comprising 2 to 6 hydroxyl groups. Examples of such alcohols are glycols, e.g.
• MDA diaminodiphenylmethane
• alkylene oxides used are typically ethylene oxide (EO), propylene oxide (PO), butylene oxide (BO) or mixtures of two or more of these.
• the polyether polyol comprising more than one type of alkylene oxide may be a so-called block polyether comprising at least two different alkylene oxides, obtained e.g. by reacting the starting compound with one of the alkylene oxide components. After termination of this polyaddition reaction, the intermediate polyether polyol is reacted with an other of the alkylene oxides. This sequential addition of blocks of alkylene oxides can be repeated. As such blocks of different alkylene oxides are added to the polyether polyol.
• the polyether polyol comprising more than one type of alkylene oxide may be a so-called random polyether comprising at least two different alkylene oxides, obtained e.g. by reacting the starting compound with a combination of at least two different alkylene oxide components. After termination of this polyaddition reaction, the different alkylene oxides will be at random in the sequences of the polyether chains.
• the polyether polyol comprises less than 80% EO, an EO content of 5 to 80% EO, and most preferred an EO content in the range of 5 to 35 % such as in the range of 10 to 30 %.
• the EO content is the number of EO-monomers in the polyol over the total of alkyloxide monomers in the polyol, expressed as a percentage. These EO may be present at random or as blocks, and are preferably combined with PO in the polyether polyol.
• the polyether polyol is a combined EO-PO polyether polyol, meaning that the polyether polyol is provided by reacting the starting component with alkylene oxides selected from EO and PO only, and this at random or in sequences to provide block polymers.
• the polyether polyols may be EO tipped, which means that at least the last alkylene oxide added to the polyol is an EO.
• the EO content of the polyether polyol may be in the range of 5 to 80%.
• the crude, alkaline, polyether polyol mixture is mixed with an acid, optionally provided as an aqueous acid solution.
• the base catalyst is thereby neutralized.
• a mono- or polyprotic acid is added to the unneutralised polyether polyol, such that "A" moles of the mono- or polyprotic acid are added to the unneutralised polyether polyol, such that B ⁇ n*A, wherein B are the moles of protons necessary to completely neutralize the crude polyether polyol and n being the number of protons which said mono- or polyprotic acid can donate.
• B typically is the number of moles of alkali metal hydroxide in the crude polyether polyol.
• a monoprotic acid such as hydrogen chloride (HC1)
• HC1 hydrogen chloride
• diprotic acids such as adipic acid
• the acidity of the neutralized polyether polyol i.e. the acid value, is expressed as the weight of KOH (mg) per gram of polyether that needs to be added to neutralize the acid.
• the neutralized polyether polyol has an acid value of 0.01 to 0.1 mgKOH/g.
• the acid used to neutralize the base catalyst is added as such in combination with water that is added, or as an aqueous solution.
• This water may be added all as part of the aqueous acid solution, or alternatively, only a part of this water is used to provide the acid aqueous solution, the remaining water is added separately.
• Suitable acids are a.o. anorganic acids such as H 2 SO 4 , H 3 PO 4 , HC1, C0 2 (added as gas forming H 2 CO 3 in water) or organic acids such as formic acid, tartaric acid, adipic acid, oxalic acid, malonic acid, succinic acid, glutaric acid, maleic acid, fumaric acid, acetic acid, citric acid, pimelic acid, suberic acid, azelaic acid and sebacic acid, or any mixture of these acids.
• anorganic acids such as H 2 SO 4 , H 3 PO 4 , HC1, C0 2 (added as gas forming H 2 CO 3 in water) or organic acids such as formic acid, tartaric acid, adipic acid, oxalic acid, malonic acid, succinic acid, glutaric acid, maleic acid, fumaric acid, acetic acid, citric acid, pimelic acid, suberic acid, azelaic acid and sebacic
• an aqueous acid solution of the acid may be used to neutralize the crude polyether polyol mixture.
• adipic acid is used to neutralize the crude polyether polyol, 0.49 to 0.56 moles of adipic acid, and preferably 0.5 to 0.53 moles of adipic acid are added for each mole of KOH or NaOH.
• the crude, alkaline, polyether polyol mixture is preferably brought or kept at a temperature of 25 to 150 deg C, e.g. at a temperature in the range of 70 to 150 deg C, more preferred at a temperature of 80 deg C to 130 deg C before, during and/or after neutralization.
• This first dehydration process may be a distillation process, i.e. by heating the crude neutralized polyether polyol mixture to remove the water and/or subjecting the crude neutralized polyether polyol mixture to a vacuum for removing at least part of the water.
• the temperature of the crude neutralized polyether polyol mixture is brought or kept in the range of 25 to 250 deg C, such as in the range of 70 to 160 deg C, and more preferred in the range of 80 deg C to 140 deg C, while the pressure of the reactor is brought to a pressure of 0.20 to 0.01 bara.
• bara means "bar absolute”, i.e. the pressure expressed in the unit bar, zero- referenced against a perfect, i.e. absolute, vacuum. One bar equals 100000 Pa.
• the water in the first dehydrated neutralized polyether polyol mixture after removal of at least part of the water is in the range of 0.00 to 5.00%w, more preferably in the range of 0.01 to 3.00 %w, and more preferred in the range of 0.10 to 1.00 %w.
• a part of the formed crystals may be removed, e.g. filtered, from the first dehydrated polyether polyol mixture.
• This water may be e.g. distilled water (or condensate) or demineralised water.
• the addition of the water causes at least part, and preferably all the salt crystals to redissolve.
• the temperature of the dehydrated neutralized polyether polyol mixture is brought or kept in the range of 25 to 250 deg C, such as in the range of 25 to 150 deg C, more preferred in the range of 80 deg C to 140 deg C.
• the temperature of the water added can be used to control the temperature of the dehydrated neutralized polyether polyol mixture during this redissolving step.
• the water added is also brought or kept in the range of 25 to 250 deg C, typically in the range of 60 to 100 deg C, and more preferred in the range 85 to 95 deg C.
• the amount of water added may be in the range of 0.5 to 10 parts by weight, and more preferred in the range of 1 to 5 parts by weight of water per 100 parts by weight of the polyether polyol in the crude polyether polyol.
• the amount of water added to the first dehydrated neutralized polyether polyol mixture may be in the range of 0.5 to 10 parts by weight per 100 parts by weight of the polyether polyol in the crude polyether polyol.
• further components such as crystal growth promoting components (also referred to as seeds) may be added, e.g. the hydrate of a metal salt of the applied mineral acid.
• the salt crystals obtained after redissolving and recrystallisation have a larger crystal size and/or a more narrow size distribution, which allows a better and more efficient control and removal of the salt crystal in the next step.
• the improved crystal size uniformity and crystal size increase allows a more efficient and better controllable filtration process.
• Typical dimensions of the salt crystals are from less than 10 micron to about 150 micron or even more.
• This second dehydration process may be a distillation process, i.e. by heating the second crude neutralized polyether polyol mixture to remove the water and/or subjecting the second crude neutralized polyether polyol mixture to a vacuum for removing at least part of the water.
• the temperature of the crude neutralized polyether polyol mixture is brought or kept in the range of 25 to 250 deg C, such as in the range of 70 to 160 deg C, and more preferred in the range of 80 deg C to 140 deg C, while the pressure of the reactor is brought to a pressure of 0.20 to 0.01 bara.
• the temperature may be gradually raised to about 110 to 150 deg C before ending this dehydration step.
• the water in the second dehydrated neutralized polyether polyol mixture after removal of at least part of the water is less than 0.08 w%, more preferably in the range of 0.01 w% to max 0.08 w%.
• the salt crystals are removed from the second dehydrated neutralized polyether polyol.
• a polyether polyol mixture comprising said polyether polyol and optionally water, up to 0.08 w% may be provided, said w% being expressed over the total weight of the polyether polyol mixture.
• the removal of the salt crystals is preferably a filtration step where the second dehydrated neutralized polyether polyol is to flow through a filter, which retains the salt crystals on the filter and let the polyol and water, if still present, pass through the filter.
• removal of the salt crystals may be obtained by filtration.
• the polyether polyol may e.g. be used as a raw material in polyurethane production, where the polyol is, in general, reacted with a polyisocyanate component, such as methylene diphenyl diisocyanate (MDI) or toluene diisocyanate (TDI).
• a polyisocyanate component such as methylene diphenyl diisocyanate (MDI) or toluene diisocyanate (TDI).
• MDI methylene diphenyl diisocyanate
• TDI toluene diisocyanate
• Polyol # I is a glycerol-started EO-tipped EO/PO polyether polyol with average molecular weight of 6000.
• the polyol comprises 15.2 w% of EO (on total of EO and PO).
• Polyol # II is a glycerol-started EO-tipped EO/PO polyether polyol with average molecular weight of 6000.
• the polyol comprises 27.4 w% of EO (on total of EO and PO).
• Polyol # III is a dipropylene glycol-started EO-tipped EO/PO polyether polyol with average molecular weight of 3700.
• the polyol comprises 16.0 w% of EO (on total of EO and PO).
• Polyol # IV is a glycerol-started EO-tipped EO/PO polyether polyol with average molecular weight of 5000.
• the polyol comprises 17.0 w% of EO (on total of EO and PO).
• EO/PO polyether polyol refers to a polyol comprising both EO monomers and PO monomers in its polymer chain.
• a crude alkaline polyether polyol mixture is provided, comprising a polyether polyol and KOH as alkali (base) catalyst.
• the crude alkaline polyether polyol mixture contained in a vessel (hereinafter neutralization vessel), is neutralized by the addition of an aqueous adipic acid solution at 95 deg C.
• the aqueous adipic acid solution contains about 0.51 moles of adipic acid per mole of base catalyst and 2.5 parts by weight of water (condensate) per 100 parts by weight of the polyol in the crude polyether polyol mixture.
• a first neutralized polyether polyol mixture is provided.
• the water is removed by gradually decreasing the pressure in the vessel from 1.8 bara to 0.1 bara over a time span of 2 hours while maintaining the temperature at 95 deg C.
• a first dehydrated neutralized polyether polyol mixture is provided.
• the vessel When the pressure in the neutralization vessel reaches 0.1 bara, the vessel is vented to atmospheric pressure. Next, 5 parts by weight of water (condensate) per 100 parts by weight of the polyol in the crude polyether polyol mixture are added. Typically the temperature of the water is between about 80 and 100°C. As such a second crude neutralized polyether polyol mixture is provided. The dispersed potassium adipate is allowed to redissolve for 15 minutes at 95 deg C. Next, the water is removed a second time by gradually reducing the pressure from 1.8 bara to 0.25 bara, gradually increasing the temperature of the polyol mixture to 105 or 1 15 deg C, over a varying time span (see tables). Thereafter, the pressure is further gradually reduced to less than 0.01 bara over a varying time span (see tables), meanwhile gradually increasing the temperature of the polyol mixture to 140 deg C.
• water condensate
• the dispersed potassium adipate is allowed to redissolve for 15 minutes at 95 de
• a filtration process is carried out to this heated second dehydrated neutralized polyether polyol.
• the potassium adipate salts that are formed precipitate as coarse crystals, so that filtration presents no problems, even without a filtration aid.
• the polyether polyol mixtures thus obtained have residual alkali contents of less than 5 ppm and water contents of max 0.08 %. The acidity of these samples was determined obtaining values varying between 0.01 - 0.10 mgKOH/g.
• 63 %vol of the crystals have a dimension of less than 10 microns.
• the method according to the invention provide only 14 %vol of the crystals to have such small dimension, whereas the majority of the particles have a dimension in the range of 10 to 100 microns.

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