KR100959610B1 - Dmc catalysts, polyether alcohols, and method for the production thereof - Google Patents

Abstract

The present invention relates to a process for preparing a polyether alcohol by adding alkylene oxide to an H-functional starting material using a multimetal cyanide compound as a catalyst, wherein the multi metal cyanide compound is (a) 0.05 Cyano- with a specific stirring force ε of 0 to 10 W / l, preferably 0.4 to 4 W / l, 0 to 100 ° C, preferably 20 to 60 ° C, and an addition time of 5 to 120 minutes. Adding a metal salt solution to the metal solution; (b) lowering the specific stirring force ε to 0.03 to 0.8 W / l, and simultaneously adding a surfactant; (c) heating the solution to a temperature of at most 100 ° C., preferably 55-75 ° C. with stirring at a specific stirring force ε of 0.03 to 0.8 W / l; (d) further adding a metal salt solution while stirring at a specific stirring force ε of 0.03 to 0.8 W / l; (e) when the conductivity begins to drop, for example by increasing the specific stirring force ε to> 0.7 W / l, stirring or dispersing solids by installing a transport pump circuit or dissolver with a suitable pump; (f) stirring at the specific stirring force ε of step (e) until the conductivity or pH value remains stable; (g) separating the multi-metal cyanide compound and washing it with water; And (h) optionally drying the catalyst.

Description

DMC catalyst, polyether alcohol and preparation method thereof {DMC CATALYSTS, POLYETHER ALCOHOLS, AND METHOD FOR THE PRODUCTION THEREOF}

The present invention relates to a process for preparing polyether alcohols by adding alkylene oxides on compounds with active hydrogen atoms using multimetal cyanide compounds as catalysts.

Polyether alcohols are an important starting material for the production of polyurethanes. They are usually prepared by catalytic addition of lower alkylene oxides, in particular ethylene oxide and / or propylene oxide, onto the H-functional starting material.

Catalysts used are generally soluble basic metal hydroxides or salts, with potassium hydroxide of greatest industrial importance. A disadvantage of using potassium hydroxide as a catalyst is the formation of unsaturated byproducts, in particular in the preparation of high molecular weight polyether alcohols, which lowers the functionality of the polyether alcohols and has a very detrimental effect on the production of polyurethanes. Will be.

In order to reduce the content of unsaturated components in the polyether alcohols and to increase the reaction rate of the addition reaction with propylene oxide, multimetal cyanide compounds, preferably double metal cyanide compounds (commonly called DMC catalysts) as catalysts It has been suggested to use. There are many documents in which such compounds are introduced. Such compounds are typically prepared by reacting a solution of a metal salt, generally zinc chloride, with a solution of an alkali metal or alkaline earth metal cyanometallate (eg, potassium hexacyanocobaltate or cyanometal acid). Generally, immediately after the precipitation procedure, water-miscible components containing at least one heteroatom are added to the resulting suspension. This component may also be initially contained in one or both of the starting solutions. The water miscible heteroatom containing component is preferably ether, polyether, alcohol, ketone or a mixture of two or more of the above compounds. Such a process is described, for example, in US Pat. No. 3,278,457, US-A-3,278,458, US-A-3,278,459, US-A-3,427,256.

Multimetallic cyanide compounds have very high catalytic activity and addition reactions with alkylene oxides proceed at very fast reaction rates, but they generally cannot directly add alkylene oxides to low molecular weight starting materials. Low molecular weight starting materials herein are in particular alcohols having a molecular weight of 62 to 400 g / mol. Examples are glycerol, ethylene glycol, propylene glycol, trimethylolpropane, pentaerythritol, diethylene glycol and butanediol. When these compounds are used, the initiation of the reaction, generally known as the induction period, is significantly delayed. In industrial plants this can lead to dangerous situations.

One possible way to solve this problem is to greatly increase the amount of catalyst used. However, this will adversely affect the economic aspects of the process.

In another possible way to overcome this problem, when a multi-metal cyanide compound is used, the reaction product obtained by reacting alkylene oxide having a molecular weight of 400 to 1,000 g / mol with a low molecular weight alcohol is generally used as starting material. Use as. These intermediates react with alkylene oxides without induction periods. Such intermediates are generally prepared using alkali metal hydroxide as catalyst. Since the alkali metal hydroxide acts as a catalyst poison for the multimetal cyanide compound, the intermediate must be purified.

Another possible way to overcome this problem is to continuously add the low molecular weight alcohol used as starting material during the polymerization process to the reaction mixture, as disclosed in WO 98/03571 and WO 97/29146. However, this process limits the opportunity to change the composition of the chains of polyether alcohols.

It is an object of the present invention to prepare polyether alcohols by adding alkylene oxides on H-functional starting materials using multi-metal cyanide compounds as catalysts, wherein H-functional starting without delay of initiation of the reaction It is to develop a method for the direct addition of alkylene oxides onto materials, in particular alcohols having two or more hydroxyl groups. This method should be simple and without additional process steps. The amount of catalyst used should be less than 1,000 ppm based on polyether alcohols, preferably less than 500 ppm.

The inventors have found that this object is achieved by using a multimetal cyanide compound prepared by a specific sequence of process steps. The present inventors can add alkylene oxide to the low molecular weight, preferably monomeric, H-functional starting materials without generating significant induction periods even with a small amount of the multimetal cyanide compounds described above. I found it.

The present invention therefore provides a process for preparing polyether alcohols by adding alkylene oxides onto H-functional starting materials using a multimetal cyanide compound as a catalyst, wherein the multi metal cyanide compound comprises Prepared by the method comprising:

(a) 0.05 to 10 W / l, preferably 0.4 to 4 W / l of specific stirring force ε, 0 to 100 ° C, preferably 20 to 60 ° C, and addition time of 5 to 120 minutes Adding a metal salt solution to the cyanometallate solution with

(b) lowering the specific stirring force ε to a value of 0.03 to 0.8 W / l and simultaneously adding a surfactant;

(c) heating the solution to a temperature of 100 ° C. or lower, preferably 55 to 75 ° C., with stirring at a specific stirring force ε of 0.03 to 0.8 W / l,

(d) adding additional metal salt solution while stirring at a specific stirring force ε of 0.03 to 0.8 W / l,

(e) When the conductivity begins to drop, for example, stirring with increasing specific stirring force ε> 0.7 W / l, or installing a pumping circuit with a suitable pump, or using a high speed stirrer Dispersing,

(f) stirring at the specific stirring force ε of step (e) until the conductivity or pH remains constant,

(g) separating the multi-metal cyanide compound and washing it with water, and optionally

(h) drying the catalyst.

The intermediate obtained after step (a) generally has a conductivity of about 0.7 mS / cm, a pH of about 3.0, and the intermediate obtained after step d) generally has a conductivity of about 3.7 mS / cm, a pH of about 4.0, and The intermediate obtained after f) has a conductivity of about 0.8 mS / cm and a pH of about 3.1.

At least one of the steps (a) to (f) can be carried out in the presence of one or more organic ligands and / or organic additives. These compounds are described in more detail below.

The parameter specific stirring power ε is known in the art and can be defined as follows (M. Zogg; Einfuehrung in die Mechanische Verfahrenstechnik., B.B. Teubner Stuttgart):

e = Ne * ρ * n ³ * d ⁵ / V

Where Ne is the power index of the stirrer, ρ is the density of the medium being stirred, n is the rotational speed of the stirrer, d is the stirrer diameter, and V is the volume of the liquid.

The surfactant added in step (b) is in each case generally added in an amount of 15 to 50% by weight, preferably in an amount of about 30% by weight, based on the theoretical weight of the DMC catalyst. They in particular serve to adjust the form of the DMC catalyst and are generally removed from the catalyst by washing, although a small amount of residual may remain in the catalyst. In principle it is also possible to use higher amounts of surface-active compounds. However, this adds to the cost of preparing the catalyst without significantly improving the properties of the DMC catalyst.

In the present invention, the surfactant is a compound that reduces the surface tension of water. The surfactant has a characteristic structure and has at least one hydrophilic functional group and one hydrophobic functional group. The hydrophilic portion of the molecule is generally a polar functional group (-COO-, -OSO _3- , -SO _3- ), while the hydrophobic portion is generally a nonpolar hydrocarbon radical.

In particular, nonionic and / or polymeric surfactants are used. Particularly useful examples of this group include fatty alcohol alkoxylates, block copolymers of various epoxides with different hydrophilicity, castor oil alkoxylates or block copolymers of epoxides and other monomers (eg acrylic acid or methacrylic acid). have. The materials used should be moderate to good in water solubility.

Fatty alcohol alkoxylates used as surfactants in the preparation of DMC catalysts used in accordance with the invention are fatty alcohols, preferably fatty alcohols having 8 to 36 carbon atoms, in particular 10 to 18, ethylene oxide and propylene jade. It can be prepared by reacting the seed and / or butylene oxide. The polyether portion of the fatty alcohol alkoxylates used according to the invention may consist of pure ethylene oxide, propylene oxide or butylene oxide polyethers. In addition, copolymers of two or three different alkylene oxides or block copolymers of two or three different alkylene oxides may also be used. Fatty alcohol alkoxylates with pure polyether chains are, for example, Lutensol® AO grades available from BASF AG. An example of a fatty alcohol alkoxylate having a block copolymer as the polyether moiety is Plurafac® LF grade available from BASF AG. Particular preference is given to the polyether chains consisting of 2 to 50, in particular 3 to 15, alkylene oxide units.

Block copolymers as surfactants include two different polyether blocks with different hydrophilicity. Block copolymers that may be used in accordance with the present invention may include ethylene oxide and propylene oxide (Pluronic® grade, BASF AG). Their water solubility is controlled by the length of the various blocks. The molar mass is in the range of 500 Da to 20,000 Da, preferably 1,000 Da to 6,000 Da, in particular 1,500 to 4,000 Da. In the case of ethylene oxide / propylene oxide copolymers, the proportion of ethylene oxide is 5-50% by weight, and the proportion of propylene oxide is 50-95% by weight.

Copolymers of other monomers with alkylene oxides which may be used for the purposes of the present invention preferably have ethylene oxide blocks. Examples of other monomers that may be used include butyl methacrylate (PBMA / PEO BE1010 / BE1030, Th. Goldschmidt), methyl methacrylate (PMMA / PEO ME1010 / ME1030, Th. Goldschmidt) or methacrylic acid (EA-3007, Th. Goldschmidt).

The double metal cyanide catalyst used according to the invention is represented by the formula

[Formula I]

M ¹ _a [M ² (CN) _b (A) _c ] _d ㆍ fM ¹ _g X _n ㆍ h (H ₂ O) eL · kP

Where

M ¹ is Zn ²⁺ , Fe ²⁺ , Fe ³⁺ , Co ³⁺ , Ni ²⁺ , Mn ²⁺ , Co ²⁺ , Sn ²⁺ , Sn ⁴⁺ , Pb ²⁺ , Mo ⁴⁺ , Mo ⁶⁺ , Al ³⁺ , V ⁴⁺ , V ⁵⁺ , Sr ²⁺ , W ⁴⁺ , W ⁶⁺ , Cr ²⁺ , Cr ³⁺ , Cd ²⁺ , Cu ²⁺ , La ³⁺ , Ce ³⁺ , Ce ⁴⁺ , Eu ³⁺ , Mg ²⁺ , Ti ³⁺ , Ti ⁴⁺ , Ag ⁺ , Rh ²⁺ , Ru ²⁺ , Ru ³⁺ , and a metal ion selected from the group consisting of

M ² is Fe ²⁺ , Fe ³⁺ , Co ²⁺ , Co ³⁺ , Mn ²⁺ , Mn ³⁺ , Ni ²⁺ , V ⁴⁺ , V ⁵⁺ , Cr ²⁺ , Cr ³⁺ , Rh ³⁺ , Ru ²⁺ , Ir ³⁺ is a metal ion selected from the group consisting of

At this time, M ¹ and M ² are different from each other,

A is an anionic halide, hydroxide, sulfate, hydrogensulfate, carbonate, hydrogencarbonate, cyanide, thiocyanate, isocyanate, cyanate, carboxylate, oxalate, nitrate, nitrosyl, Phosphate, hydrogenphosphate and dihydrogenphosphate and non-charged species CO, H ₂ O and NO,

X is a halide, hydroxide, sulfate, hydrogensulfate, carbonate, hydrogencarbonate, cyanide, thiocyanate, isocyanate, cyanate, carboxylate, oxalate, nitrate and nitrite (NO an anion selected from the group consisting of a) ^- ₂

L is alcohol, aldehyde, ketone, ether, polyether, ester, polyester, polycarbonate, urea, amide, nitrile, sulfide, amine, phosphide, phosphite, phosphine, phosphonate, phosphate and their Water-miscible ligands selected from the group consisting of mixtures,

P is polyether, polyester, polycarbonate, polyalkylene glycol sorbitan ester, polyalkylene glycol glycidyl ether, polyacrylamide, poly (acrylamide-co-acrylic acid), polyacrylic acid, poly (acrylic Amide-co-maleic acid), polyacrylonitrile, polyalkyl acrylate, polyalkyl methacrylate, polyvinyl methyl ether, polyvinyl ethyl ether, polyvinyl acetate, polyvinyl alcohol, poly-N-vinylpyrrolidone , Poly (N-vinylpyrrolidone-co-acrylic acid), polyvinyl methyl ketone, poly (4-vinylphenol), poly (acrylic acid-co-styrene), oxazoline polymer, polyalkyleneimine, maleic acid and male Acid anhydride copolymers, hydroxyethylcellulose, polyacetates, ionic surface active compounds, bile acids and salts thereof, esters of glycosides and polyhydric alcohols, amides, carboxylic acid esters And L and the other is an organic additive,

a, b, d, g and n are integers or fractions greater than zero,

c, f, e, h and k are integers or fractions greater than 0,

Wherein a, b, c and d and g and n are chosen such that the compound is electrically neutral,

f and k can be zero only if c is not zero and A is only carboxylate, oxalate or nitrate.

The carboxylate is particularly preferably acetate.

Such catalysts may be crystalline or amorphous. Preference is given to crystalline double metal cyanide compounds when k is zero. If k is greater than zero, both crystalline catalysts, partially crystalline and substantially amorphous catalysts are preferred.

The organic additive may be a surface active compound.

There are various preferred embodiments of the catalyst of the invention.

In one preferred embodiment, k is greater than zero in the catalyst of formula (I).

Therefore, the preferred catalyst

(a) at least one multimetal cyanide compound,

(b) at least one organic ligand,

(c) at least one organic additive P.

In another preferred embodiment, k is 0 and e can also be 0 and X is only a carboxylate, preferably formate, acetate or propionate. In such embodiments the multi-metal cyanide compound is preferably crystalline.

Particularly useful ligands are described in WO 01/03830. Such catalysts are prepared using organic sulfones of formula RS (0) ₂ -R or sulfoxides of formula RS (O) -R as organic complexing agents. DMC catalysts prepared in this way have particularly short induction times and lead to moderate exothermic polymerization of alkylene oxides.

In a particularly preferred embodiment of the process of the invention, nitriles, in particular acetonitrile, are used as the ligand (s). Such catalysts have particularly high activity and very short induction times. They can be usefully used for the addition of alkylene oxides to low molecular weight starting materials such as glycols, glycerol or trimethylolpropane.

The amount of heteroatom containing ligands present in the suspension formed after precipitation should be 1 to 60% by weight, preferably 5 to 40% by weight, in particular 10 to 30% by weight.

In a particularly preferred embodiment of the invention, the multimetal cyanide compound is crystalline and in the form of a small plate. Such catalysts are described in WO 00/74843.

The catalyst of the present invention is prepared as described above by mixing a cyanometallate solution and a metal salt solution, which may optionally additionally comprise both an organic ligand L and an organic additive P in the order of certain process steps according to the present invention. . It is also possible to add an organic ligand and an organic additive after each time the metal salt solution is mixed with the cyanometallate solution in one of the predetermined process steps according to the invention.

After the multi-metal cyanide compound is separated in step (g), it can be washed. Water is generally used for washing. Additional ligands and / or additives may be added to this water.

The multimetal cyanide compound prepared in this way can be dried and used in a dry form as a catalyst for the polymerization of alkylene oxides.

The catalyst prepared as described above is separated by filtration or centrifugation, preferably dried at 30 to 200 ° C., preferably at a pressure of 100 to 10 ⁻³ mbar, particularly preferably at 50 ° C. and 15 mbar You can.

The dried catalyst is then milled as described, for example, in US 3,829,505 and US 5,714,639. However, this catalyst can also be spray dried or lyophilized as described, for example, in US Pat. No. 5,900,384.

Alternatively, the wet filter cake obtained after separating and washing the multi-metal cyanide compound may be used as a catalyst for the polymerization of alkylene oxides.

In a preferred embodiment of the invention, the multimetal cyanide compound is used as a catalyst in the form of a suspension.

In this embodiment, the catalyst is suspended in organic or inorganic liquids, preferably in starting compounds used in the preparation of polyether alcohols. This suspension procedure is performed by applying very high shear energy in a suitable apparatus such as ultraturax, homogenizer or stirred mill. Such a procedure is described, for example, in WO # 00/74843.

The DMC catalyst of the present invention can also be applied to supports as described in WO? 01/04180 for polycarboxylic acids and WO? 01/04177 for zeolites. This allows the catalyst to be separated from the polyether alcohol in a simple manner.

Metal salts used in the preparation of the multimetal cyanide compounds of the present invention are generally salts of formula (II).

[Formula II]

M ¹ _g X _n

Wherein M ¹ and X are as defined above and g and n are chosen such that the compound is electrically neutral.

The metal salts used in steps (a) and (d) may be the same or different.

The cyanometallate compounds used in the preparation of the multimetal cyanide compounds of the present invention are generally compounds of formula III.

[Formula III]

Me _p [M ² (CN) _b ] _d

Wherein M ² , b and d are as defined above, Me is an alkali metal, alkaline earth metal or hydrogen, p is an integer or fraction greater than 0, and p, b and d are such that the compound is electrically neutral. Is selected.

In a preferred embodiment of the invention, Me is hydrogen, ie cyanometallic acid is used. Multimetal cyanide compounds prepared in this way exhibit particularly good catalytic activity. In addition, its post-treatment is simplified because the production of problematic salts can be avoided.

In another preferred embodiment of the catalyst, f, e and k are not zero. Such multi-metal cyanide compounds preferably contain water-miscible organic ligands based on the multi-metal cyanide compounds of formula (I) in an amount of 0.5 to 30% by weight, preferably organic additives based on the multi-metal cyanide compounds of formula (I). Preferably in an amount of 5 to 80% by weight.

As mentioned above, the multimetal cyanide compound produced by the process of the present invention can be used as a catalyst for the polymerization of alkylene oxides.

Polyether alcohols are prepared by addition of alkylene oxide onto the H-functional starting material in the presence of a catalyst prepared according to the invention.

Alkylene oxides that can be used are all known alkylene oxides, for example ethylene oxide, propylene oxide, butylene oxide and / or styrene oxide. Particular preference is given to using ethylene oxide, propylene oxide and mixtures thereof as alkylene oxides.

Starting materials used are H-functional compounds. Particular preference is given to using alcohols having a functionality of 1 to 8, preferably 2 to 8. Starting materials for the production of polyether alcohols which can be used in flexible polyurethane foams are specifically alcohols having a functionality of 2 to 4, in particular 2 and 3. Examples are ethylene glycol, propylene glycol, glycerol, trimethylolpropane and pentaerythritol. In the addition reaction of alkylene oxides in the presence of a DMC catalyst, it is advantageous to use the reaction product of alkylene oxides, in particular propylene oxide, with the alcohols mentioned above or with alcohols. Such reaction products preferably have a molar mass of 500 g / mol or less. The addition reaction of alkylene oxide in the production of such reaction products can be promoted with any catalyst, for example a basic catalyst. The polyether alcohols used to make flexible polyurethane foams have a hydroxyl value of 20-100 mg / KOH / g.

In the preparation of the polyether alcohol used in the method of the present invention, the addition reaction of alkylene oxide can be carried out by a known method. Thus, it is possible for the polyether alcohol to contain only one alkylene oxide. If multiple alkylene oxides are used, they can be added in blocks, ie the alkylene oxides can be added in succession, or randomly, respectively, in which case the alkylene oxides are introduced together. It is also possible to incorporate both blocked and random sections into the polyether chain in the preparation of the polyether alcohols.

In order to produce flexible polyurethane slabstock foams, polyether alcohols having a high secondary hydroxyl group content in the polyether chain and having an ethylene oxide unit content of 30% by weight or less based on the weight of the polyether alcohol are used. It is preferable. Such polyether alcohols preferably have propylene oxide blocks at the chain ends. In order to produce shaped flexible polyurethane foams, preference is given to using polyether alcohols having a high primary hydroxyl group content and a content of ethylene oxide end blocks of less than 20% by weight, based on the weight of the polyether alcohol.

The addition reaction of alkylene oxide is preferably from 0 to 20 bar, preferably at a temperature of 60 to 180 ° C., preferably at a temperature of 90 to 140 ° C., in particular at 100 to 130 ° C., under the conditions conventionally used for this purpose. Preferably at a pressure of 0 to 10 bar, in particular 0 to 5 bar. The mixture of starting material and DMC catalyst can be pretreated by stripping as described in WO 98/52689 prior to initiation of alkoxylation.

After the addition reaction of the alkylene oxides is complete, the polyether alcohols are worked up by conventional methods, wherein the unreacted alkylene oxides and volatiles are typically subjected to distillation, steam stripping or gas stripping and / or other deodorizing methods. By removing. If desired, the polyether alcohol may be filtered.

After the addition reaction of the alkylene oxide is terminated, the catalyst can be separated from the reaction mixture. However, for most uses of polyether alcohols, it is also possible to leave the catalyst in the product, especially in the production of polyurethanes.

Conventional stabilizers, especially those which inhibit thermal oxidative degradation, may be added to the post-treated polyether alcohols in amounts conventionally used for this purpose.

The catalyst of the invention may be used in an amount of less than 1,000 ppm, preferably less than 500 ppm, in particular less than 200 ppm. However, the catalyst content should not be less than 10 ppm, because in this case generally insufficient catalytic effect is obtained.

The use of multi-metal cyanide compounds produced by the process of the present invention allows the use of polyetherols with improved properties to provide low molecular weight starting materials, especially ethylene glycol, propylene glycol, glycerol, trimethylolpropane, penta, at low catalyst concentrations. It can be prepared from erythritol and mixtures thereof. Even when the catalyst concentration is very low, no induction period occurs at the beginning of the polymerization.

The polyether alcohols produced using the DMC catalyst of the invention are preferably used for the production of polyurethanes, in particular polyurethane foams and especially flexible polyurethane foams. Polyurethanes are prepared by reacting polyether alcohols with polyisocyanates in the presence of catalysts, blowing agents and optionally other conventional auxiliaries and / or additives.

Example 1

Aqueous hexacyanocobaltic acid (cobalt content: 9 g / l, calculated as cobalt) 800 liter capacity with blade turbine inclined 353.9 kg, dip tube for introduction of reactants, pH electrode, conductivity measuring cell and scattered light probe Was added to a stirred vessel of, and heated to 50 ° C. while stirring. Then, 215.7 kg of an aqueous zinc acetate dihydrate solution (zinc content: 2.5% by weight), also heated to 50 ° C., was added for 45 minutes with stirring at 1 W / L of stirring force.

After the addition was complete, the agitation force was set to 0.4 W / L and a solution of 7.67 kg of Pluronic® PE 6200 (Bass AG) in 10 kg of water was added. This mixture was heated to 60 ° C. and stirred at this temperature for 2 hours. Then 70.5 kg of an aqueous zinc acetate dihydrate solution (zinc content: 2.5% by weight) was metered in while stirring at 0.4 W / L at agitation power over 60 minutes at 60 ° C. After a few minutes the conductivity began to drop. This mixture was then further stirred at agitation force 1.5 W / l.

The suspension was stirred at 60 ° C. and stirring force 1.5 W / l until the pH remained constant at 4.15 to 3.09. The suspension thus produced is then filtered using a filter press and the precipitate is washed with 400 L of water in the filter press.

The wet filter cake was dried at 50 ° C. under reduced pressure.

Example 2

Preparation of Polyether Alcohols

134 g (1 mole) of the starting material dipropylene glycol were added to 2 L of a stirred autoclave with 0.18 g (200 ppm based on the amount of polyether alcohol) from Example 1. The mixture was then dehydrated at 100 ° C. and 0-10 mbar for 2 hours, then nitrogen was added to bring the pressure to atmospheric pressure and the mixture was stirred at 100 ° C. overnight. This mixture was then heated to 135 ° C. and alkoxylation started. To this end, 50 ml of propylene oxide, which was under initial nitrogen pressure, were added to increase the pressure to 4 bar over 30 minutes.

The internal pressure of the reactor was then increased to 8 bar over an additional 30 minutes while introducing 250 g of propylene oxide.

At 9 bar and reaction temperature 135 ° C., a significant pressure drop from 9 bar to 1 bar was observed after about 4-5 hours. The remaining propylene oxide was then added at a temperature of 1-3 bar and 135 ° C. to bring the total amount of propylene oxide to 756 g (13.03 moles). After the reaction was completed, the reaction mixture was stripped with nitrogen, unreacted propylene oxide was removed at 100 ° C. under reduced pressure (10 mbar), and the mixture was filtered by passing through a deep bed filter.

This gave 886.8 g of a colorless liquid, which corresponds to 13 moles of propylene oxide / 1 mole of starting material.                 

Characteristics of the resulting polymer:

Polydispersity: 1.053, measured by GPC

Co (residual content): 1 ppm

Zn (residual content): 3 ppm

Hydroxyl number: 119 mg / KOH / g

Kaufmann Iodine: <1 g Iodine / 100 g

Comparative Example 1

Preparation of the catalyst

800 ℓ capacity with blade turbine inclined 370 kg of aqueous hexacyanocobaltic acid (cobalt content: 9 g / l, calculated as cobalt), dip tube for introduction of reactants, pH electrode, conductivity measuring cell and scattered light probe Was added to a stirred vessel of, and heated to 50 ° C. while stirring. Thereafter, 209.5 kg of an aqueous zinc acetate dihydrate solution (zinc content: 2.7 wt%), also heated to 50 ° C., was added over 50 minutes with stirring at 1 W / l of stirring force.

Subsequently, 8 kg of surfactant Pluronic® PE 6200 (BASF AG) and 10.7 kg of water were added with stirring. Then 67.5 kg of an aqueous zinc acetate dihydrate solution (zinc content: 2.7 wt%) was introduced with stirring at 1 W / l of stirring power over 55 minutes at 55 ° C.

The resulting suspension was stirred at 55 ° C. until the pH remained constant at 2.7 to 2.7. The suspension thus produced is then filtered using a filter press and the precipitate is washed with 400 L of water in the filter press.                 

Comparative Example 2-Preparation of Polyether Alcohol

134 g (1 mol) of dipropylene glycol were mixed with 0.18 g (200 ppm) of the catalyst of Comparative Example 1. 30 g of molecular sieves were added thereto. The starting mixture thus prepared was dehydrated at 100 ° C. for 3 hours under a pressure of about 1 mbar. Nitrogen was added to release the vacuum, the molecular sieve was filtered off and the starting mixture was introduced into a 2 L stirred reactor.

A pressure test was then performed and the reactor was charged with nitrogen three times to make the reactor inactive. The mixture was then heated to 130 ° C. After reaching the temperature and increasing the pressure from 0.2 bar to 4 bar at a predetermined rate so that the onset of the reaction could be observed, 50 g of propylene oxide was fed to the reactor.

After 11 minutes, the pressure in the reactor had dropped to 3.9 bar and after 120 minutes the pressure had dropped to 1.8 bar. No exothermic reaction was observed. After an additional pressure rise (5 bar to 1.8 bar), 102 g of propylene oxide was fed to the reactor. The internal temperature of the reactor showed a clear initial rise, but after a few minutes the temperature dropped significantly. After 120 minutes, the pressure had dropped to 4.4 bar and then remained constant at this value. No exothermic reactivity or additional uptake of PO was observed. The experiment was stopped.

Comparative Example 3

134 g (1 mole) of dipropylene glycol and 2.22 g of DMC catalyst from Comparative Example 1 (corresponding to 2,500 ppm based on polyether alcohol) were added to a 2 L stirred autoclave. The mixture was heated to 100 ° C. and dehydrated at this temperature for 2 hours under reduced pressure (<20 mbar). Nitrogen was then added to release the vacuum and the mixture was heated to 130 ° C. 20 g of propylene oxide was added at an initial pressure of 0.3 bar to increase the pressure to 2 bar. After the pressure had dropped to 1.3 bar, 50 g of PO was further added. After 4 hours an exothermic reaction was observed at 3.2 bar internal pressure. After 5 hours more, the metered addition was completed (calculated propylene oxide) and no exothermic reaction was observed anymore. The mixture was stirred for 9 hours at 130 ° C. and a pressure of 5 bar to allow for after-reaction. The weight of the resulting polypropylene glycol was 902.3 g (corresponding to 13.2 moles of PO / 1 mole of starting material) and was pink. However, deep filtration yielded a colorless transparent product.

Claims (5)

(a) Formula M ¹ _g X _n [wherein M ¹ is added to the cyanometallate solution at a specific stirring force? of 0.05 to 10 W / l, a temperature of 0 to 100 ° C., and an addition time of 5 to 120 minutes. Silver Zn ²⁺ , Fe ²⁺ , Fe ³⁺ , Co ³⁺ , Ni ²⁺ , Mn ²⁺ , Co ²⁺ , Sn ²⁺ , Sn ⁴⁺ , Pb ²⁺ , Mo ⁴⁺ , Mo ⁶⁺ , Al ³⁺ , V ⁴⁺ , V ⁵⁺ , Sr ²⁺ , W ⁴⁺ , W ⁶⁺ , Cr ²⁺ , Cr ³⁺ , Cd ²⁺ , Cu ²⁺ , La ³⁺ , Ce ³⁺ , Ce ⁴⁺ , Eu ³⁺ , Mg ²⁺ , Ti ³⁺ , Ti ⁴⁺ , Ag ⁺ , Rh ²⁺ , Ru ²⁺ , Ru ³⁺ are metal ions selected from the group, g and n are compounds that are electrically neutral Selected to be a metal salt solution of (b) lowering the specific stirring force ε to a value of 0.03 to 0.8 W / l and simultaneously adding a surfactant; (c) heating the solution to a temperature of 100 ° C. or less while stirring at a specific stirring force ε of 0.03 to 0.8 W / l, (d) further adding a metal salt solution while stirring at a specific stirring force ε of 0.03 to 0.8 W / l, (e) when the conductivity begins to drop, stirring while increasing the specific stirring force? to> 0.7 W / l; Install a pumping circuit with a suitable pump; Or dispersing the solid using a high speed stirrer, (f) stirring at the specific agitation force of step (e) until the conductivity or pH remains constant, and (g) separating the multi-metal cyanide compound and washing it with water A method for producing a double metal cyanide catalyst comprising a. delete delete delete delete