WO2000056805A1 - Polyurethane foam stabilizers - Google Patents
Polyurethane foam stabilizers Download PDFInfo
- Publication number
- WO2000056805A1 WO2000056805A1 PCT/US2000/008002 US0008002W WO0056805A1 WO 2000056805 A1 WO2000056805 A1 WO 2000056805A1 US 0008002 W US0008002 W US 0008002W WO 0056805 A1 WO0056805 A1 WO 0056805A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- group
- silicone
- ether
- groups
- polyhydric
- 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.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0061—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
-
- 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
- C08G18/4072—Mixtures of compounds of group C08G18/63 with other macromolecular compounds
-
- 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
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/38—Polysiloxanes modified by chemical after-treatment
-
- 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
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/42—Block-or graft-polymers containing polysiloxane sequences
- C08G77/46—Block-or graft-polymers containing polysiloxane sequences containing polyether sequences
-
- 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
- C08G2110/00—Foam properties
- C08G2110/0008—Foam properties flexible
-
- 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
- C08G2110/00—Foam properties
- C08G2110/0016—Foam properties semi-rigid
-
- 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
- C08G2110/00—Foam properties
- C08G2110/0041—Foam properties having specified density
- C08G2110/005—< 50kg/m3
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
- C08J2375/04—Polyurethanes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2483/00—Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen, or carbon only; Derivatives of such polymers
Definitions
- Silicone surfactants useful for controlling stabilizing polyurethane foams are known. Specific patent documents relating to such silicones and to their use include US 5,789,454; US 5,525,640; US 5,432,206; US 5,192,812; US 5,145,879; US 5,070,112; US 5,045,571 ; US 5,041,468; US 5,001,248; and US 4,746,683, the entire disclosures of which are incorporated herein by reference. Typically silicones used as polyurethane foam stabilizers are copolymers containing polyoxyalkylene moieties thereon. Much of the research on such silicone surfactants has focused on the structure, size and distribution of alkylene oxide moieties. This approach, however, has not proved entirely satisfactory. A need therefore exists for an alternative approach to preparing silicone surfactants useful in stabilizing polyurethane foams.
- surfactant blend compositions comprising a mixture of between 5 and 20% by weight of a silicone having phenolic group substitution and between 95 and 80 % by weight of a silicone/ ethylene oxide/propylene oxide copolymer.
- Silicone polymers having polyhydric groups thereon and useful as defoamers for diesel fuel and other hydrocarbon liquids are described in DE 4032006 (unsaturated polyhydric groups) and in WO 97/38067 (saturated polyhydric groups), both incorporated herein by reference in their entirety.
- the invention hereof in various aspects, provides novel polyurethane foam compositions employing silicone surfactants; new silicone surfactants useful in the stabilization of polyurethane foams; and a novel process for modifying the properties of polyurethane foam stabilizing silicone surfactants.
- the invention is a formulation curable to a foam comprising: an active hydrogen component having an average of two or more active hydrogen groups per molecule; a polyisocyanate component having an average of two or more isocyanate groups per molecule; a blowing agent; and a silicone surfactant composition comprising a first silicone having from about 2 to about 205 siloxane repeat units and which includes at least one substituent which is a polyhydric organic group (R 2 ), an ester, ether, acetal or ketal derivative of a polyhydric organic group (R 3 ) or a phenolic group (R 4 ), and wherein the surfactant composition comprises no more than 50% by weight of a polyether silicone copolymer.
- Preferred such first silicones may be represented by the formula:
- Silicone surfactants as described above, in which the first silicone has a combination of substituent groups which include at least one each substituent selected from R 2 , R 3 and R 4 , and also has at least two different substituents selected from R 2 , R 3 , R 4 and R 5 constitutes a further aspect of the invention. Particular such combinations include R 2 and R 3 ; R 2 and R 4 ; R 2 and R 5 ; R 3 and R 4 ; R 3 and R 5 ; and R 4 and R 5 .
- Such silicones may be produced by a hydrosilation reaction process which constitutes yet a further aspect of the invention. In the inventive process, suitable aliphatically unsaturated compounds are sequentially or concurrently reacted with a hydrido silicone.
- the surfactant composition may have the first silicone, as defined above, as the sole component thereof.
- the first silicone may be used in combination with a silicone polyether copolymer or a silicone oil, provided, however, that the first silicone, or a mixture of first silicones, represents about 50% or more of the total silicone surfactant weight.
- a further aspect of the invention is a silicone surfactant composition comprising a mixture of at least one said first silicone and at least one second silicone selected from the group consisting of of a silicone polyether copolymer or a silicone oil, the first silicone constituting about 50% or more of the total weight of silicone surfactant.
- the silicone surfactants used in the invention are preferably linear, although an occurrence of one or two branching moieties in a surfactant molecule should be considered to also be encompassed within formula (I), above.
- the surfactants may be produced from hydrido functional silicones using appropriate hydrosilation reactions to introduce the R groups into the molecule and, if desired, to introduce variation in the R 1 groups.
- the hydrido functional silicones suitably may be represented by the formula:
- M' t D x D' y M u (II) wherein M' is R ⁇ HSIO Q 5 -; D is -R ⁇ SiO-; D' is -R ⁇ RSiO-; and M is R ⁇ SIO Q 5 -., and R 1 , t, x, y and u are as previously defined.
- R 1 is an aromatic or saturated aliphatic hydrocarbon group. Specific examples include methyl, ethyl, propyl, octyl, decyl, dodecyl, stearyl, phenyl, methylphenyl, dimethylphenyl, phenylethyl, cyclohexyl, methylcyclohexyl, and the like.
- Preferred R 1 groups are alkyl, most suitably methyl, optionally with relatively minor amounts of C 6 -C 22 alkyl groups. The longer alkyl groups may be introduced by hydrosilation of a corresponding C 6 -C 22 olefin.
- a polydimethylsiloxane having a specific content of methylhydrogendisiloxy and/or dimethylhydrogensiloxy units thereon can be used to hydrosilate a higher terminal olefin such as decene to produce a desired content of decyl groups grafted onto the polymer molecule.
- hydrosilations may be desirable to consume any excess silicon hydride functionality in the starting hydrido silicone polymer over that needed to introduce the respective R 2 , R 3 , R 4 and/or R 5 groups onto the molecule.
- Long chain alkyl groups can also be introduced to modify solubility or the hydrophilic/hydrophobic balance properties.
- polyhydric organic group refers to an organic group having two or more hydroxyl groups thereon.
- the polyhydric organic groups R 2 may be aliphatic, low molecular weight hydrocarbon groups, optionally interrupted with an ether oxygen atom and/or a tertiary amino group, and having at least two hydroxy groups thereon.
- Polyhydric groups interrupted with tertiary amino groups may be prepared as described in copending US provisional application 60/102,039 filed Sept. 28, 1998, incorporated herein by reference in its entirety.
- Preferred organic groups are saturated ether or saturated hydrocarbon groups.
- Polyhydric unsaturated aliphatic groups may be employed but are generally less preferred.
- the R 2 group preferably has a molecular weight between about 134 and about 644, and more preferably between about 134 and about 400.
- the R 2 group preferably is saturated completely, as disclosed in WO 97/38067, although unsaturated polyhydric groups such as disclosed in DE 4032006 may also be used.
- the R 2 group may be provided on the molecule by a hydrosilation grafting reaction wherein a silicone polymer having a content of silicon hydride groups, typically present as methylhydrogendisiloxy and/or dimethylhydrogensiloxy repeat units, can be used to hydrosilate an unsaturated hydrocarbon group on a polyhydric compound having an unsaturated site such as an allyl, methallyl or vinyl group.
- Examples of compounds which may be hydrosilated in this manner to form R 2 groups include trimethylolpropane monoallyl ether (TMPMAE), alkoxylated trimethylolpropane monoallyl ether, pentaerythritol allyl ether, alkoxylated pentaerythritol allyl ether, tri-isopropanolamine allyl ether, alkoxylated allyl sorbitol, 1,3- allyloxypropanediol and 2-butyne-l,4-diol.
- TMPMAE trimethylolpropane monoallyl ether
- alkoxylated trimethylolpropane monoallyl ether pentaerythritol allyl ether
- alkoxylated pentaerythritol allyl ether tri-isopropanolamine allyl ether
- alkoxylated allyl sorbitol 1,3- ally
- Alkoxylation may be ethoxylate, propoxylate, butoxylate or mixtures thereof and may contain multiple alkoxylate units per molecule, preferably from 1-6 such repeat units.
- Polyhydric compounds having acetylenic unsaturation, such as 2-butyne-l,4-diol, may be employed to provide polyhydric organic groups.
- the polyhydric group is preferably saturated and therefore an olefinically unsaturated polyhydric compound is preferably be used to prepare the R 2 groups.
- TMPMAE is preferred.
- An aliphatically unsaturated diol or polyol can be reacted to form esters, ethers, acetals or ketals, in accordance with well known reactions, and then the resulting unsaturated compound hydrosilated in like manner to form groups R 3 .
- an unsaturated diol can be transformed into a corresponding cyclic formal via reaction with formaldehyde, and the resulting cyclic olefins can be grafted onto the siloxane backbone by hydrosilation.
- the cyclic formal of trimethylolpropane may be prepared and the resulting mono-ol converted to the alkali alkoxylate and reacted with an unsaturated halide such as allyl chloride or methallyl chloride.
- an unsaturated halide such as allyl chloride or methallyl chloride.
- a polyorganosiloxane having polyhydric groups R 2 may have a selected fraction of the polyhydric groups converted into ester, ether, acetal or ketal derivatives, using mild condition reactants so as to avoid destroying the siloxane backbone, in order to fine tune the solubility parameters of the surfactant.
- the fraction of R 2 groups so converted may be up to 100%, preferably not more than 50%, more preferably not more than 10%.
- the R 4 groups are suitably derived from phenol compounds having unsaturated olefinic or acetylenic group thereon. A similar hydrosilation reaction to those described above may be used.
- a typical example of a phenol compound which may be grafted to a silicone polymer in this manner is eugenol (i. e. 4-allyl-2- methoxyphenol).
- Other phenol compounds which may be employed include vinylphenol, vinyl guaiacol and 4-allylphenol.
- the phenolic R 4 groups may be the sole R groups on the molecule but are preferably employed, if at all, in mixture with polyhydric R 2 groups in an amount, relative to the R 2 groups, of no more than 1:1, desirably no more than about 0.4: 1.
- the R 5 groups are polyether groups. They may be provided on a silicone backbone by a hydrosilation grafting reaction using a silicon hydride functional silicone and a polyether having an olefinically unsaturated end group, such as an allyl group.
- the polyether groups may be any polyether known as usefully employed on silicone surfactants for polyurethane foam stabilization, especially those based on ethylene oxide, propylene oxide, butylene oxide or tetrahydrofuran.
- Preferred polyether groups are derived from allyl started polyethylene oxides or polyethylene oxide/polypropylene oxide polyethers having a molecular weight of about 100 to about 350. Also preferably the ethylene oxide content of the polyether is at least 75% by weight, most preferably 100%) .
- the polyether group may suitably be terminated with a hydroxy, alkoxy or acetoxy group.
- Silicone surfactants having two or more of R 2 , R 3 , R 4 and/or R 5 groups may be prepared by hydrosilation of a mixture of two or more members of the group consisting of unsaturated polyhydric compounds, derivatives thereof, unsaturated polyether compounds and unsaturated phenol compounds.
- a sequential hydrosilation process in which the different unsaturated compounds are sequentially added to silicone having an excess of SiH groups, relative to each of the unsaturated compounds individually, may also be employed.
- the polyhydric groups R 2 typically provide greater hydrophilic character than an EO moiety so that larger starting hydrido silicones can be used in synthesizing the silicone surfactants of the invention. That is, compared to conventional silicone polyether copolymer surfactants, the invention permits a surfactant having a higher molar fraction of silicone relative to organic may be used while still maintaining adequate control over the polarity of the polymer. Furthermore, an R 3 group in which all of the hydroxyl groups are derivatized typically provides a greater hydrophobic character than a PO unit. Consequently, a wide range of properties can be obtained merely varying the R 2 to R 3 ratio.
- an R 3 group can be prepared by derivatization of the R 2 group, a single hydrosilation product can be used to provide an assortment of surfactants having a range of properties. Still further, another assortment of surfactants can be easily prepared by varying the ratio of components in the hydrosilation reaction using a single set of reactant compounds. Thus, many surfactants can be prepared from a single hydrido silicone, a single set of R group forming compounds (e.g.
- Solvents used for these purposes include DPG (dipropylene glycol), toluene and any other solvent of which has suitable solubility characteristics, such as isopropanol, various aromatic solvents such as SOLWESSO 150, aliphatic ester alcohols such as TEXANOL (2 ,2,4-trimethyl-l,3- pentanediol monoisobutyrate), isophorone, mixtures of same, and the like.
- reactive natural diluents such as castor oil, and non-reactive diluents, such as soybean oil, may be used.
- volatile solvents such as toluene and isopropanol can optionally be removed.
- Non-volatile solvents or those of a high flash point e.g., DPG) do not pose the same safety problems, and there is no need to remove them.
- an organic compound having two or more active hydrogen groups per molecule is reacted with a polyisocyanate.
- the organic compound having two or more active hydrogen groups per molecule is preferably a polyamine or a polyol, most preferably a polyol.
- Suitable polyols have an average of at least 2 and typically 2.1 to 3.5 hydroxyl groups per molecule and include compounds which consist of carbon, hydrogen and oxygen, and compounds which may also contain phosphorus, halogen, and/or nitrogen.
- Typical polyols are polyester polyols, polymer polyol graft compounds and polyether polyols. Choice of polyol tipping, i.e.
- polyether polyols are generally preferred.
- the polyether polyol is prepared by reacting a low molecular weight polyfunctional alcohol, e.g. ethylene glycol, propylene glycol, 1-4- butane diol, glycerol, trimethylolpropane, 1,2,6-hexanetriol, pentaerythritol sorbitol, sucrose or the like with one or more lower alkylene oxides.
- a low molecular weight polyfunctional alcohol e.g. ethylene glycol, propylene glycol, 1-4- butane diol, glycerol, trimethylolpropane, 1,2,6-hexanetriol, pentaerythritol sorbitol, sucrose or the like.
- Such polyols are well known in the art and are commercially available.
- organic isocyanates that are useful in producing polyurethane foams in accordance with this invention are also well known in the art and are organic compounds that contain at least two isocyanate groups per molecule. Any such compounds or mixtures thereof can be employed.
- Isocyanates may be aromatic or aliphatic and may be monomeric or oligomeric compounds.
- suitable diisocyanates include toluene diisocyanate, diphenylmethane diisocyanate, 1,6- hexamethylene diisocyanate, isophorone diisocyanate, methylene-bis-(4-cyclohexane isocyanate) and oligomers thereof.
- the urethane foaming reaction is usually effected in the presence of a minor amount of a base catalyst, preferably an amine catalyst and usually a tertiary amine.
- a base catalyst preferably an amine catalyst and usually a tertiary amine.
- Known metal catalysts may be used instead of, or in addition to, the amine catalyst in the urethane foam reaction mixture.
- Useful metal catalysts include organic derivatives of tin, e.g. tin (II) alkoxides, tin (II) carboxylates, dialkyl tin salts of carboxylic acids or hydrohalic acids.
- the blowing agent may be water, which reacts with isocyanate to generate carbon dioxide in situ, or a fluorocarbon such as dichlorodifluoromethane, 1,1-dichloro-l-fluoroethane, l-chloro-l,l-difluoroethane, 2,2- dichloroethane or the like.
- fluorocarbon such as dichlorodifluoromethane, 1,1-dichloro-l-fluoroethane, l-chloro-l,l-difluoroethane, 2,2- dichloroethane or the like.
- Non-fluorinated organic compound blowing agents such as pentane and acetone may also be employed as blowing agents.
- the amount of blowing agent required will vary according to the density of the foam which is desired. Suitable levels of blowing agent are known to the skilled person.
- auxiliary gas is added to the system as a blowing agent and is used in conjunction with the CO 2 generated from the reaction of isocyanate with water.
- the inert gas is dissolved in the foam formulation at elevated pressures, but flashes out of solution at atmospheric pressure, thereby blowing the foam.
- An exemplary such gas is CO but nitrogen, air or other common gases, including hydrocarbon gases, such as methane and ethane may also be used.
- additives may be added to the polyurethane foam to impart specific properties to the foam, including, but not limited to, coloring agents, flame retardants, UV stabilizers, antioxidants and GEOLITE ® Modifier foam additives (available from Witco Corp., Greenwich, Conn.).
- the relative amounts of the various components of the foam formulation are not narrowly critical.
- the polyether polyol and polyisocyanate are present in the foam-producing formulation in a major amount.
- the relative amounts of these two components in the amount required to produce the desired urethane structure of the foam and such relative amounts are well known in the art.
- the blowing agent, catalyst and surfactant are each present in a minor amount sufficient to foam the reaction mixture, the catalyst is present in a catalytic amount i.e., that amount necessary to catalyze the reaction to produce the urethane at a reasonable rate, and the surfactant is present in an amount sufficient to impart the properties desired.
- the surfactants are typically present at 0.01 to 5 Wt. percent of the total reaction mixture, preferably 0.2 to 1.5 wt. percent. It is sometimes convenient to add the surfactant to the reaction mixture in a premix with one or more of the blowing agents, polyol and/or catalyst components.
- the polyurethane foams produced in accordance with the present invention may be rigid, flexible, microcelluar, mechanically froathed, molded, high resiliency, or slab stock. They can be used in the in the manufacture of textile interliners, cushions, mattresses, padding, carpet underlay, packaging, gaskets, sealers, thermal insulators and the like.
- Silicone surfactants were produced by hydrosilating one or more members of the group consisting of allyl started poly ethers of varying blend average molecular weights (BAMW); TMPMAE (trimethylolpropane monoallyl ether); and/or TMPMAE formal (formaldehyde condensate of trimethylolpropane monoallyl ether), in the relative ratios shown in Table 1 , using a hydrido siloxane of formula II where R is methyl and t, u, x and y are as given in Table 1.
- BAMW blend average molecular weights
- TMPMAE trimethylolpropane monoallyl ether
- TMPMAE formal formaldehyde condensate of trimethylolpropane monoallyl ether
- the same EO/PO polyether was used, adjusted to the indicated BAMW by blending with a 400 mol. wt. 100%) EO polyether.
- the B-series examples all used a polyether having an EO/PO ratio of 75/25.
- Three different hydrido silicones (types 1, 2 and 3, respectively) were used.
- Surfactants for flexible foams are indicated by the letter A in the Example number and surfactants for rigid foams are indicated by the letter B in the Example number.
- Examples A-11, A-12 and A-27, which are made entirely from polyether are comparative examples.
- the formulations are shown in Table 2.
- the formulation FA1 results in extremely low foam density (8 kg/m 3 ) and the foam rise, the top collapse of foam made (TCj and the foam structure are of great importance.
- the formulation FA2 the form rise, top collapse and the breathability (airflow) of the foam are major properties as the foam structures are usually similar unless a serious deficiency in foam rise is recorded.
- This type of foam is not currently made by foam producers, due to the use of CFC blowing agent, but experience shows this formulation as representative of the processing latitude of a stabilizer and is therefore still useful as a test formulation. Foam stabilizers yielding more open foams are usually considered to have a desirable wide processing latitude. Table 2 gives detailed formulations.
- Foam evaluation results are collected in Table 3 where the concentration of the foam stabilizing surfactant is given on the basis of parts by weight per 100 parts of polyol (php).
- the airflow value indicates the amount of air passing through a foam specimen of a fixed thickness and under standardized pressure.
- RA1 currently used in the production of very low density foam
- RA2 a state-of-the-art stabilizer commonly employed in Europe.
- RA2 produces very open foams.
- Examples Al 1 to A18 are made with the same siloxane backbone, with RA-1, A-11, A-12, A-27 and RA-2 being Comparative Examples. It can be seen from Table 3 that the introduction of TMPMAE effects an increase in the foam rise and reduces the top collapse of foams made in FA1. This is particularly visible in the Example A15 which comes with a substantially improved foam rise at 1.5 parts.
- the stabilizing surfactants A-16, A-27, A-28 and RA-1 were also tested using a small batch foam machine with formulation FA-1 to make foam blocks having a height exceeding one meter. Such foaming conditions are more critical than the bench test reported in Table 3.
- the foam made with the Example A-27 comes with an unacceptable foam structure that is coarse with some internal voids.
- Examples A- 16 and A-28 yielded foams at least matching the reference RA-1 in terms of foam structure and offer improved foam rise.
- the copolymers made with a formal derivative of TMPMAE offer less improvement in the formulation FA1.
- the FA2 formulation their use allowed production of foams which were very stable and very open as well (A- 14, A 17). Structures made with a polyether and TMPMAE yield very stable foams in FA2 but the airflow recorded is somewhat low. However, higher airflow than that for reference RA-1 can be obtained as illustrated with example A-18.
- Silicone structures identified by the letter designation "B" in Table 1 were used to make rigid polyurethane foam blown with hydrocarbons. Foams of good structure and low foam thermal conductivity were made in the laboratory set-up.
- Silicone surfactants were produced by hydrosilating one or more members of the group consisting of: TMPMAE;
- TMPMAE formal ("TMPMAE.F” in Table 4); Eugenol; and the allyl ethers of ethoxylated cyclic trimethylolpropane formal (the (average) mono, di, tri and tetra ethoxylates are designated respectively, "CTF1,” "CTF2,” “CTF3” and '”CTF4" in Table 4), in the relative ratios shown in Table 1 , using a hydrido siloxane of formula II above, where R is methyl and t, u, x and y are as given in Table 4.
- Formulation B reflects an average formulation used in the industry.
- Foam formulations were prepared using the surfactants described in Table 4 using the average formulation B of Table 5, except where the surfactant designation in Table 6 is followed by the letter A, in which case formulation A of Table 5 was used.
- the amount of diethanol amine was 1.0 phr, except as indicated in the following discussion of specific foam tests.
- Silicones described in Table 4 were added to the formulations as solutions in inert solvent. The total weight basis concentration of the respective silicones is indicated in Table 6 as % active. In some cases influence of a silicone oil co-surfactant was added and the beauht basis concentration of the latter is also indicated in Table 6.
- FTC Force-To-Crush
- the FTC value is a good relative measure of the degree of foam openness: the lower the value, the more open the foam is.
- STAB -Foam Stability
- STR - Cell Structure
- the ideal silicone surfactant for this application gives very open foams with a FTC ranging from 100 N to less than 500 N along with an acceptable cell structure rated as "*" or "**" still producing a good stability rated below 5.
- the difficulty is to produce open foam while preserving stability as it can be observed with the results obtained with the 3 commercial references, Ref A, RefB and Ref C. when stability is improved to a rating of 3 the FTC reaches a relatively high value denoting tight foam. From the above table it can be seen that several structures based on the novel pending groups offer the benefit of substantially open foam along with superior stability.
- polyhydric groups R 2 as well as their derivatives R 3 and phenolic groups R 4 , optionally in combination with polyether groups, function as suitable organic groups to be used in the preparation and fine tuning- up of molecular properties of silicone polymers used for polyurethane foam stabilization.
- the adjustment of molecular properties can be accomplished by modification of the siloxane segmenf lengfh, the degree of its substitution and the nature of the grafted groups.
- the use of compact, highly polar moieties such as polyhydric derivatives allows a desired polarity of organosilicone to be maintained together with a high molar contribution of siloxane unites in the copolymer.
- the combination of the latter with an adequate overall polarity permits easy adjustment to improve the performance characteristics of urethane foam stabilizers in specific applications.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Polyurethanes Or Polyureas (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002342931A CA2342931A1 (en) | 1999-03-24 | 2000-03-24 | Polyurethane foam stabilizers |
| AU41772/00A AU4177200A (en) | 1999-03-24 | 2000-03-24 | Polyurethane foam stabilizers |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12587199P | 1999-03-24 | 1999-03-24 | |
| US60/125,871 | 1999-03-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2000056805A1 true WO2000056805A1 (en) | 2000-09-28 |
Family
ID=22421835
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2000/008002 Ceased WO2000056805A1 (en) | 1999-03-24 | 2000-03-24 | Polyurethane foam stabilizers |
Country Status (3)
| Country | Link |
|---|---|
| AU (1) | AU4177200A (en) |
| CA (1) | CA2342931A1 (en) |
| WO (1) | WO2000056805A1 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007037896A1 (en) * | 2005-09-15 | 2007-04-05 | Momentive Performance Materials Inc. | High mobility low emission surfactants for polyurethane foams |
| WO2007142822A1 (en) * | 2006-05-31 | 2007-12-13 | Bayer Materialscience Llc | A process for the production of rigid and semi-rigid foams with low amounts of diisocyanate using polymer polyols characterized by high solids and a high hydroxyl number and the resultant foams |
| WO2010081601A1 (en) * | 2009-01-14 | 2010-07-22 | Evonik Goldschmidt Gmbh | Method for producing cold foams |
| US9260346B2 (en) | 2011-09-12 | 2016-02-16 | Basf Se | Graft polyol and method of forming the same |
| CN106497215A (en) * | 2015-09-03 | 2017-03-15 | 赢创德固赛有限公司 | The purposes of eugenol polyethers and eugenol polyether silicone as wetting agent |
| CN112694617A (en) * | 2020-12-28 | 2021-04-23 | 南京美思德新材料有限公司 | Modified silicone oil, surfactant, preparation method and application thereof |
| US20210137276A1 (en) * | 2019-11-07 | 2021-05-13 | Evonik Operations Gmbh | Compression set |
| US11976157B2 (en) | 2015-03-12 | 2024-05-07 | HUNTSMAN ADVANCED MATERIALS (Switz | Polyol component for the production of PUR foams |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3381019A (en) * | 1963-08-27 | 1968-04-30 | Union Carbide Corp | Siloxane-alcohol ethers |
| EP0092700A1 (en) * | 1982-04-23 | 1983-11-02 | Th. Goldschmidt AG | Process for producing highly resilient cold-curing polyurethane foams |
| US4431789A (en) * | 1981-03-13 | 1984-02-14 | Shin-Etsu Chemical Co., Ltd. | Novel organopolysiloxane having alcoholic hydroxy groups and a method for the preparation thereof |
| US4746683A (en) * | 1987-09-29 | 1988-05-24 | Union Carbide Corporation | Polyether silicone copolymers with secondary or tertiary hydroxy termination for stabilizing high resiliency urethane foam |
| US5070112A (en) * | 1989-11-14 | 1991-12-03 | Union Carbide Chemicals And Plastics Technology Corporation | Process for making flexible polyurethane foam |
| US5542960A (en) * | 1993-06-30 | 1996-08-06 | Osi Specialties, Inc. | Efficient diesel fuel antifoams of low silicon content |
| WO1997038067A1 (en) * | 1996-04-04 | 1997-10-16 | Witco Corporation | Diesel fuel and lubricating oil antifoams and methods of use |
| WO1999006487A1 (en) * | 1997-08-01 | 1999-02-11 | Ppg Industries Ohio, Inc. | Curable compositions based on functional polysiloxanes |
| EP1010748A1 (en) * | 1998-12-15 | 2000-06-21 | Ck Witco Corporation | Diesel fuel antifoam composition |
-
2000
- 2000-03-24 CA CA002342931A patent/CA2342931A1/en not_active Abandoned
- 2000-03-24 WO PCT/US2000/008002 patent/WO2000056805A1/en not_active Ceased
- 2000-03-24 AU AU41772/00A patent/AU4177200A/en not_active Abandoned
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3381019A (en) * | 1963-08-27 | 1968-04-30 | Union Carbide Corp | Siloxane-alcohol ethers |
| US4431789A (en) * | 1981-03-13 | 1984-02-14 | Shin-Etsu Chemical Co., Ltd. | Novel organopolysiloxane having alcoholic hydroxy groups and a method for the preparation thereof |
| EP0092700A1 (en) * | 1982-04-23 | 1983-11-02 | Th. Goldschmidt AG | Process for producing highly resilient cold-curing polyurethane foams |
| US4746683A (en) * | 1987-09-29 | 1988-05-24 | Union Carbide Corporation | Polyether silicone copolymers with secondary or tertiary hydroxy termination for stabilizing high resiliency urethane foam |
| US5070112A (en) * | 1989-11-14 | 1991-12-03 | Union Carbide Chemicals And Plastics Technology Corporation | Process for making flexible polyurethane foam |
| US5542960A (en) * | 1993-06-30 | 1996-08-06 | Osi Specialties, Inc. | Efficient diesel fuel antifoams of low silicon content |
| WO1997038067A1 (en) * | 1996-04-04 | 1997-10-16 | Witco Corporation | Diesel fuel and lubricating oil antifoams and methods of use |
| WO1999006487A1 (en) * | 1997-08-01 | 1999-02-11 | Ppg Industries Ohio, Inc. | Curable compositions based on functional polysiloxanes |
| EP1010748A1 (en) * | 1998-12-15 | 2000-06-21 | Ck Witco Corporation | Diesel fuel antifoam composition |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007037896A1 (en) * | 2005-09-15 | 2007-04-05 | Momentive Performance Materials Inc. | High mobility low emission surfactants for polyurethane foams |
| WO2007142822A1 (en) * | 2006-05-31 | 2007-12-13 | Bayer Materialscience Llc | A process for the production of rigid and semi-rigid foams with low amounts of diisocyanate using polymer polyols characterized by high solids and a high hydroxyl number and the resultant foams |
| US7456229B2 (en) | 2006-05-31 | 2008-11-25 | Bayer Materialscience Llc | Process for the production of rigid and semi-rigid foams with low amounts of diisocyanate using polymer polyols characterized by high solids and a high hydroxyl number and the resultant foams |
| WO2010081601A1 (en) * | 2009-01-14 | 2010-07-22 | Evonik Goldschmidt Gmbh | Method for producing cold foams |
| US9260346B2 (en) | 2011-09-12 | 2016-02-16 | Basf Se | Graft polyol and method of forming the same |
| US11976157B2 (en) | 2015-03-12 | 2024-05-07 | HUNTSMAN ADVANCED MATERIALS (Switz | Polyol component for the production of PUR foams |
| CN106497215A (en) * | 2015-09-03 | 2017-03-15 | 赢创德固赛有限公司 | The purposes of eugenol polyethers and eugenol polyether silicone as wetting agent |
| CN106497215B (en) * | 2015-09-03 | 2021-06-29 | 赢创运营有限公司 | Application of eugenol polyether and eugenol polyether siloxane as wetting agent |
| US20210137276A1 (en) * | 2019-11-07 | 2021-05-13 | Evonik Operations Gmbh | Compression set |
| US12082704B2 (en) * | 2019-11-07 | 2024-09-10 | Evonik Operations Gmbh | Compression set |
| CN112694617A (en) * | 2020-12-28 | 2021-04-23 | 南京美思德新材料有限公司 | Modified silicone oil, surfactant, preparation method and application thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| AU4177200A (en) | 2000-10-09 |
| CA2342931A1 (en) | 2000-09-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DK2182020T3 (en) | SILICONE POLYETHER BLOCK COPOLYMERS WITH DEFINED POLYDISPERSITY IN THE POLYOXYAL COOLING PART AND THEIR USE AS STABILIZERS FOR PREPARING POLYURETHAN FOOD | |
| CN102617862B (en) | Silicone-polyether block copolymers with high molecular weight polyether residues and their use as stabilizers for production of polyurethane foams | |
| EP2183301B1 (en) | Silicone copolymer surfactants for use in polyurethane foams | |
| AU709737B2 (en) | Polyethers and polysiloxane copolymers manufactured with double metal cyanide catalysts | |
| KR100193922B1 (en) | Process for producing polyurethane foam using polyether silicone surfactant | |
| EP2268714B1 (en) | Polyurethane foams containing silicone surfactants | |
| JP5743544B2 (en) | Open cell polyurethane foam and its manufacturing process | |
| US9657144B2 (en) | Polysiloxane polyether copolymers having (polyether)moieties comprising carbonate groups and their use as stabilizers for the production of polyurethane foams | |
| EP2430061B1 (en) | Silicone surfactant for use in polyurethane foams prepared using vegetable oil based polyols | |
| KR100279492B1 (en) | Low emission, cell opening surfactants for polyurethane flexible and rigid foams | |
| CN102617882A (en) | Use of silicone-polyether block copolymers with high molecular weight non-endcapped polyether moieties as stabilizers for production of low-density polyurethane foams | |
| KR100407082B1 (en) | Silicone Polyether Surfactants | |
| US6245824B1 (en) | Silicone surfactants for making polyurethane flexible molded foams | |
| US12371537B2 (en) | Polyether-polysiloxane block copolymer composition, foam stabilizer and method for producing polyurethane foam | |
| US5789454A (en) | Silicone surfactant compositions useful in inert gas blown polyurethane foams | |
| US4031044A (en) | Polyether based, high resilient polyurethane foam | |
| CA1203350A (en) | Amino catalyst mixture for stabilization of polyurethane foam | |
| EP1501889B1 (en) | Fire retardant silicone surfactants for use in inert gas blown polyurethane foams | |
| WO2000056805A1 (en) | Polyurethane foam stabilizers | |
| US6235804B1 (en) | Silicone surfactants for making polyurethane flexible molded foams | |
| EP1081177A1 (en) | Silicone polyether oligomers | |
| MXPA97005754A (en) | Copolymers of polyeteros and polisiloxano manufactured with double me cyanide catalysts |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AL AM AT AU AZ BA BB BG BR BY CA CH CN CR CU CZ DE DK DM EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG UZ VN YU ZA ZW |
|
| AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG |
|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
| ENP | Entry into the national phase |
Ref document number: 2342931 Country of ref document: CA Ref country code: CA Ref document number: 2342931 Kind code of ref document: A Format of ref document f/p: F |
|
| REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
| 122 | Ep: pct application non-entry in european phase | ||
| NENP | Non-entry into the national phase |
Ref country code: JP |