WO1996033231A1 - Process for preparing a storage-stable mixture of polyisocyanate and phosphate - Google Patents
Process for preparing a storage-stable mixture of polyisocyanate and phosphate Download PDFInfo
- Publication number
- WO1996033231A1 WO1996033231A1 PCT/US1996/004120 US9604120W WO9633231A1 WO 1996033231 A1 WO1996033231 A1 WO 1996033231A1 US 9604120 W US9604120 W US 9604120W WO 9633231 A1 WO9633231 A1 WO 9633231A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- polyisocyanate
- mixture
- group
- dissolved gases
- acid phosphate
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/77—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur
- C08G18/776—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur phosphorus
-
- 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
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
-
- 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
- C08G18/30—Low-molecular-weight compounds
- C08G18/38—Low-molecular-weight compounds having heteroatoms other than oxygen
- C08G18/3878—Low-molecular-weight compounds having heteroatoms other than oxygen having phosphorus
- C08G18/3882—Low-molecular-weight compounds having heteroatoms other than oxygen having phosphorus having phosphorus bound to oxygen only
- C08G18/3885—Phosphate 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
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/77—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur
Definitions
- This invention relates to the field of polyisocyanates and, more particularly, to the field of storage-stable polyisocyanate/phosphate mixtures.
- mixtures of polyisocyanates and phosphates are useful for various purposes.
- such can be used as binder resins having releasing properties for wood composite materials.
- These polyisocyanate compositions are particularly useful as binders in the preparation of particle boards and similar materials. See, for example, U.S. Patents 3,428,592; 3,440,189; 3,557,263; 3,636,199; 3,870,665; 3,919,017; and 3,930,1 10. While some of these mixtures can be made relatively storage-stable in that they do not deposit solids or separate into two liquid phases during relatively short-term storage (see, for example, U.S Patent 4,258,169, Re.
- the present invention solves the problem of pressurization of containers. It is an improvement in a process for producing a storage-stable mixture of a polyisocyanate and an acid phosphate, wherein dissolved gases are present, comprising subjecting the mixture to a negative pressure for a time sufficient to remove at least a portion of the dissolved gases therefrom. Preferably the amount of dissolved gases is reduced by at least 10 percent by weight. It has been found that this evacuation, which is preferably carried out at a vacuum pressure of less than 50 mm Hg (2 inches Hg), for a time sufficient to remove at least 90 percent of the dissolved gases in the mixture, more preferably at least 99 percent, results in a mixture which, thereafter, shows markedly decreased gas production.
- the invention therefore reduces or eliminates problems associated with pressurization of smaller containers used to ship or store the mixture.
- the polyisocyanate/phosphorus-containing compound mixtures which are treated in the present invention can be prepared from a variety of materials and via a variety of routes.
- the starting material includes one or more phosphorus-containing compounds formed in situ, which function as a release agent when the material is used in formulations which contact certain types of metal surfaces. It is prepared starting with a polyisocyanate and an acid phosphate. This is preferably a mixture of an organic polyisocyanate and from 1 to 20 parts, per 100 parts by weight of the polyisocyanate, of an acid phosphate selected from the group consisting of acid phosphates having the formula:
- each R is independently selected from the group consisting of alkyl having at least 3 carbon atoms, alkenyl having at least 3 carbon atoms, aryl, aryl substituted by at least one alkyl group, alkyl substituted by at least one acyloxy group, wherein the acyl group is the residue of an aliphatic monocarboxylic acid having at least 2 carbon atoms, and
- Ri is selected from the group consisting of alkyl, aryl, and aryl substituted by at least one alkyl
- one of A and B represents hydrogen and the other is selected from the group consisting of hydrogen, methyl, chloromethyl and 2,2,2-trichloroethyl
- X is chalcogen selected from the group consisting of oxygen and sulfur
- m is a number having an average value of 1 to 25.
- alkyl having at least 3 carbon atoms means a saturated monovalent aliphatic radical, straight chain or branched chain, which has the stated minimum number of carbon atoms in the molecule.
- Illustrative of such groups are propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, and tridecyl, as well as those having many more carbon atoms such astriacontyl, pentatriacontyl, including isomeric forms thereof.
- alkyl when used without the above carbon atom limitation is also inclusive of methyl and ethyl.
- alkenyl having at least 3 carbon atoms means a monovalent straight or branched chain aliphatic radical containing at least one double bond, and having the stated minimum number of carbon atoms in the molecule.
- Illustrative of such groups are allyl, butenyl, pentenyl, hexenyl, heptenyl, octenyl, nonenyl, decenyl, undecenyl, dodecenyl, tridecenyl, tetradecenyl, pentadecenyl, hexadecenyl, heptadecenyl, octadecenyl, nonadecenyl, eicosenyl, heneicosenyl, docosenyl, tricosenyl, pentacosenyl. triacontenyl, pentatria-contenyl, including isomeric forms thereof.
- aryl means the monovalent radical obtained by removing one nuclear hydrogen atom from an aromatic hydrocarbon.
- aryl phenyl, naphthyl, biphenyl, triphenyl.
- aryl substituted by at least one alkyl means an aryl radical, as above defined, carrying at least one alkyl (as above defined) substituent.
- alkyl as above defined
- aliphatic monocarboxylic acid having at least 2 carbon atoms is inclusive of any alkanoic or alkenoic acid having the stated minimum number of carbon atoms.
- Illustrative of such acids are acetic, propionic, butyric, hexanoic, octanoic, lauric, stearic, oleic, undecylenic, dodecylenic, isocrotonic, palmitic.
- Each of the groups R and Ri in the formulae (I) and (II) set forth above can optionally be substituted by one or more inert substituents, i.e., substituents which do not contain active hydrogen atoms and which are therefore unreactive in the presence of the ° polyisocyanate.
- inert substituents are alkoxy, dialkylmercapto, alkenyloxy, dialkenylmercapto, chloro, bromo, iodo, fluoro, cyano.
- the acid phosphates of the formulae (I) and (II) are, for the most part, well-known in the art, and can be prepared by methods well-known in the art.
- the acid phosphates (I) and (II) are obtained by reaction of the corresponding alcohol or thiol R-XH, 5 wherein R and X are as hereinbefore defined, with phosphorus pentoxide or phosphorus oxysulfide using the procedures described by Kosolapof, Organophosphorus Compounds, John Wiley and Sons, Inc (New York, 1950), pp. 220-221.
- This reaction gives rise to a mixture of the mono- and di-acid phosphates, which mixture can be separated, if desired, for example by fractional crystallization of the barium and like salts as described in the above cited reference.
- the individual acid phosphates in the mixture of the mono- and di-acid phosphates obtained in accordance with the above reaction can be employed as starting materials in the process of the invention.
- acid phosphates having the formula (I) and (II) above, to a product containing the corresponding pyrophosphates and their sulfur-containing analogues, 5 such as thiophosphates and pyrophosphothiolates, by heating the acid phosphates in the presence of an organic polyisocyanate, with or without any other reactant such as phosphorus oxychloride, phosgene and the like. If the conditions of heating are carefully controlled as described herein, the resulting product is a homogeneous liquid which can be stored for prolonged periods without any tendency to undergo phase separation.
- the reaction would be expected to result in the formation of the desired pyrophosphate in association with some polyphosphate (if a mono-ester is present).
- the reaction also would be expected to give rise to the intermediate formation of the amine (IV) corresponding to the starting isocyanate.
- the amine (I ) would be expected to react immediately with additional isocyanate to form a urea. If a polyisocyanate were used a poly urea would be expected to form, and such should normally be insoluble in the reaction product and separate as a solid either immediately or on standing.
- reaction temperature is not the only important factor. It is found that the time for which heating is carried out is important and, in general, the higher the reaction temperature, the shorter the period for which the heating can be carried out without consequences which are fatal to the improvement of phase stability in the reaction product. Illustratively, even when the reaction temperature is as low as 60°C, it is found that there is a limited time beyond which further heating causes transformation of the pyrophosphates into what are believed to be higher polyphosphates. When the proportion of the latter in the reaction product reaches a sufficiently high level it is found that on subsequent cooling of the reaction product, the polyphosphates separate generally as a liquid layer immiscible with the polyisocyanate. Further, the higher the reaction temperature, the shorter the period for which the reaction of acid phosphate and polyisocyanate can be allowed to continue without the onset of the above described transformation of the pyrophosphates.
- the time and the temperature for which the process described hereinabove can be carried out can vary according to the particular acid phosphate and polyisocyanate, as well as the concentration of the acid phosphate, which are employed.
- the appropriate time in any given instance can be determined readily by a process of trial and error.
- the reaction times which can be employed vary from several hours at 60°C down to a minute or less at the higher end of the temperature range (190 ⁇ Q. As set forth above, the higher the temperature employed, the shorter the reaction time which can be employed without deleterious results.
- the manner in which the acid phosphate and the organic polyisocyanate are brought together can also, in certain cases, affect the ability to produce a phase-stable composition in accordance with the invention. It is possible in many instances to bring the two reactants together, in any conventional manner, at ambient temperature, and then to heat the resulting mixture at a temperature within the range set forth for a time which has been determined to give the desired result at the particular reaction temperature chosen. However, it is preferred to preheat the polyisocyanate to the selected reaction temperature and then to add the acid phosphate to the preheated polyisocyanate. When operating a batch type procedure, the addition can be carried out in a single charge or can be carried out slowly over a period of time.
- the process of the invention can also be carried out in a continuous manner in which the mixture of polyisocyanate (preferably preheated) and acid phosphate is passed through a heating zone maintained at a temperature within the range set forth above.
- the rate of flow of mixture through the heating zone is adjusted so that the residence time in the mixing zone corresponds to the selected reaction time.
- a wide variety of conventional equipment can be employed for this purpose.
- a particularly useful apparatus is that of the type in which the mixture to be heated is spread in the form of a thin film over the walls of the heating vessel.
- Atypical example of such apparatus is that set forth in U.S. Pat. No. 2,927,634.
- the polyisocyanate (preferably preheated) and the acid phosphate are charged continuously, in the appropriate proportions, to a stirred reactor in which the reactants are maintained at the desired temperature.
- the reaction mixture is withdrawn from the reactor at the same rate as the fresh reactants are added and the rate of addition and withdrawal are such that the residence time of the mixture in the reactor corresponds to the
- the reaction be carried out in the absence of oxygen and moisture, i.e., in the presence of an inert gas such as nitrogen in accordance with the usual practice of handling polyisocyanates.
- an inert gas such as nitrogen in accordance with the usual practice of handling polyisocyanates.
- an inert gas such as nitrogen in accordance with the usual practice of handling polyisocyanates.
- nitrogen such as nitrogen
- the final mixture is saturated with dissolved gases which include primarily carbon dioxide as evolved, and this is the case whether the reaction is carried out under a nitrogen blanket or under air.
- the mixture will contain primarily nitrogen, since the nitrogen forces out the carbon dioxide being evolved by the reaction between the polyisocyanate and the acid phosphate. Minor proportions of other gases may also be present in some embodiments.
- the proportions in which the polyisocyanate and the acid phosphates (I) and or (II) are employed in the process of the invention can vary over a wide range but advantageously the acid phosphate is employed in an amount corresponding from 1 to 20 parts by weight per 100 parts by weight of polyisocyanate.
- the amount of acid phosphate employed is such that the polyisocyanate compositions produced in accordance with the invention contain from 0.1 , preferably from 3, to 15, preferably to 10, most preferably to 8, percent by weight of the acid phosphate.
- the polyisocyanate employed in the process of the invention can be any organic polyisocyanate which contains at least two isocyanate groups per molecule.
- organic polyisocyanates are diphenylmethane diisocyanate, m- and p-phenylene diisocyanates, chlorophenylene diisocyanate, ⁇ , ⁇ '-xylylene diisocyanate, 2,4- and 2,6-toluene diisocyanate and the mixtures of these latter two isomers which are available commercially, including triphenylmethane triisocyanates, 4,4-diisocyanatodiphenyl ether, and polymethylene polyphenyl polyisocyanates.
- polyisocyanates are mixtures containing from 25 to 90 percent by weight of methylenebis(phenyl isocyanate) the remainder of the mixture being polymethylene polyphenyl polyisocyanates of functionality higher than 2.0.
- Such polyisocyanates and methods for their preparation are well-known in the art; see, for example, U.S. Patent Nos. 2,683,730; 2,950,263; 3,12,008 and 3,097,191.
- polyisocyanates are also available in various modified forms.
- One such form comprises a polymethylene polyphenyl polyisocyanate which has been subjected to heat treatment, generally at temperatures from 150°C to 300 ⁇ C until the viscosity (at 25°C) has been increased to a value within the range of 800 to 1500 centipoise (cps).
- Another modified polymethylene polyphenyl polyisocyanate is one which has been treated with minor amounts of an epoxide to reduce the acidity thereof in accordance with U.S. Patent No. 3,793,362.
- polymethylene polyphenyl polyisocyanates can also be employed in the form of prepolymers and quasi-prepolymers, i.e., the products obtained by reacting the polyisocyanate with a minor amount of a polyol, as well as in the form of polyisocyanates which have been partially blocked by reaction with a monohydric alcohol using procedures well-known in the art.
- Carbodiimide- modified methane diphenyl diisocyanates can also be used.
- polymethylene polyphenyl polyisocyanates are the preferred polyisocyanates for use in the process of the invention.
- Particularly preferred polymethylene polyphenyl polyisocyanates are those which contain from 35 to 65 percent by weight of methylenebis(phenyl isocyanate).
- Also preferred are those polyisocyanates having viscosities of less than 500 centipoise (cps), more preferably less than 300 cps, and most preferably less than 200 cps.
- acid phosphates of formulae (I) and (II) can be employed in the process of the invention, those acid phosphates wherein R represents alkyl or alkenyl and X represents O, and more particularly, those acid phosphates wherein R represents alkyl or alkenyl having from 8 to 18 carbon atoms and X represents O, exhibit advantages because of ready availability and low cost.
- the increased stability as to carbon dioxide generation is effected particularly by the second step of the present invention, which involves subjecting the mixture to a negative pressure sufficient to remove at least a portion of the dissolved gases therefrom.
- the negative pressure is a vacuum sufficient to remove at least 10 percent of the dissolved gases, more preferably at least 95 percent, and most preferably at least 99 percent.
- the negative pressurization evacuated be to less than 50 mm Hg (2 inches Hg), and more preferably to less than 10 mm Hg (0.4 inch Hg).
- the effective time of the evacuation varies, depending on the negative pressure employed as well as the concentration of the acid phosphate in the polyisocyanate.
- the negative pressurization is held for at least 15 minutes, and more preferably at least 30 minutes, and most preferably from 1 to 3 hours. In a preferred embodiment this most preferred period of evacuation is applied while maintaining a pressure reading of less than 10 mm Hg (0.4 inch Hg).
- Equipment useful for the negative pressurization includes vacuum pumps, jets, aspirators or other conventional equipment.
- liquid, storage-stable polyisocyanate compositions prepared in accordance with the process of this invention are particularly useful as binder resins for use in the preparation of particle boards in accordance with methods well-known in the art, as described in the "Background” section references cited hereinabove.
- the compositions useful in the process of this invention possess the advantage of preventing adherence of the particle board to metal surfaces such as caul plates and press plate platens used in the preparation of such a board.
- the polyisocyanate compositions of the invention have a viscosity in the range of from 100 to 3000 centipoise (cps) to facilitate ease of handling in the equipment currently employed in the manufacture of particle board. Viscosities in the above range can be attained readily when employing polymethylene polyphenyl polyisocyanates having an initial viscosity of the order of 25 cps to 1000 cps and subjecting these polyisocyanates to the process of the invention. This represents an additional reason for employing such polyisocyanates in a preferred embodiment of the invention.
- the polyisocyanate composition can be applied to the particle board chips, prior to heating and pressing of the latter, in the form of an aqueous emulsion or dispersion.
- an emulsifying or dispersing agent it is desirable to employ an emulsifying or dispersing agent.
- the agent can be incorporated into the polyisocyanate compositions of the invention so as to enable the particle board manufacturer to prepare the required emulsion or dispersion without the need to employ additional agents.
- the agent can be any of those known in the art including anionic and nonionic emulsifying and dispersing agents.
- agents include, for example, polyoxyethylene and polyoxypropylene alcohols and block copolymers of two or more of ethylene oxide, propylene oxide, butylene oxide, and styrene; alkoxylated alkylphenols such as nonylphenoxypoly-(ethyleneoxy)ethanols; alkoxylated aliphatic alcohols such as ethoxylated and propoxylated aliphatic alcohols containing from 4 to 18 carbon atoms; glycerides of saturated and unsaturated fatty acids such as stearic, oleic, and ricinoleic acids; polyoxyalkylene esters of fatty acids such as stearic, lauric, oleic and like acids; fatty acid amides such as the dialkanolamides of fatty acids such as stearic, lauric, oleic and similar acids; and
- a non-active hydrogen containing solvent or diluent can be employed.
- such non-active hydrogen containing materials include esterified polyols and monols.
- a reaction was carried out using as the acid phosphate a mixture of mono- and di- lauryl acid phosphate (TRYFAC* 5573, commercially available from Henkel Industries) and, as the polyisocyanate, a polymethylene polyphenyl polyisocyanate containing approximately 46.5 percent by weight of methylenebis(phenyl isocyanate) and having an isocyanate equivalent of 134.5 and a viscosity of 25°C of 173 cps (PAPI* 27, commercially available from The Dow
- the polyisocyanate starting amount was 900 pounds, and was charged to a stainless steel reaction vessel equipped with an agitator and nitrogen sparge. It was heated to 80°C with stirring and 32.6 pounds of TRYFAC* 5573 were added over a 5-10 minute interval to control foaming resulting from carbon dioxide evolution. Upon completion of the TRYFAC* addition, the reaction was stirred at 80°C for two hours. Foaming of the reaction mixture was observed to continue. At the end of the reaction the nitrogen flow was shut off, full vacuum was applied (0-50 mm Hg, 0-2 inches Hg) while the temperature was maintained at 80°C, and the product was then cooled to ambient temperature. The vacuum was then discontinued and the product was drummed off. It was stored in an oven at 43-49°C and pressurization recorded as shown in Table 1. The NCO content of the final product was 30.1 percent by weight.
- a reaction was carried out to illustrate the difference in the rate of drum pressurization between the Example 1 sample and a sample prepared using a similar preparation method but without the step of being subjected to a negative pressure
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP96911430A EP0821706A1 (en) | 1995-04-17 | 1996-03-26 | Process for preparing a storage-stable mixture of polyisocyanate and phosphate |
MX9707969A MX9707969A (en) | 1995-04-17 | 1996-03-26 | Process for preparing a storage-stable mixture of polyisocyanate and phosphate. |
BR9608163A BR9608163A (en) | 1995-04-17 | 1996-03-26 | Process for preparing a liquid polyisocyanate composition and organic polyisocyanate mixture |
JP8531745A JPH11503786A (en) | 1995-04-17 | 1996-03-26 | Process for producing a storage-stable mixture of polyisocyanate and phosphate |
AU54319/96A AU5431996A (en) | 1995-04-17 | 1996-03-26 | Process for preparing a storage-stable mixture of polyisocyanate and phosphate |
NO974785A NO974785D0 (en) | 1995-04-17 | 1997-10-16 | Process for preparing a storage stable mixture of polyisocyanate and phosphate |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US42306095A | 1995-04-17 | 1995-04-17 | |
US08/423,060 | 1995-04-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996033231A1 true WO1996033231A1 (en) | 1996-10-24 |
Family
ID=23677523
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1996/004120 WO1996033231A1 (en) | 1995-04-17 | 1996-03-26 | Process for preparing a storage-stable mixture of polyisocyanate and phosphate |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP0821706A1 (en) |
JP (1) | JPH11503786A (en) |
KR (1) | KR19990007809A (en) |
CN (1) | CN1181765A (en) |
AU (1) | AU5431996A (en) |
BR (1) | BR9608163A (en) |
CA (1) | CA2218254A1 (en) |
CO (1) | CO4410409A1 (en) |
MX (1) | MX9707969A (en) |
NO (1) | NO974785D0 (en) |
WO (1) | WO1996033231A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002024612A1 (en) * | 2000-09-20 | 2002-03-28 | Basf Aktiengesellschaft | Method for removing dissolved metals from organic fluids and cleaning agent suited therefor |
EP2825544B1 (en) * | 2012-03-15 | 2018-08-08 | Basf Se | Modified isocyanate compositions and methods of preparing the same |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006052987A1 (en) * | 2006-11-10 | 2008-05-15 | Bayer Materialscience Ag | Plastic composite elements and a method for their production |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2382468A1 (en) * | 1977-03-01 | 1978-09-29 | Asahi Chemical Ind | PROCESS FOR PREPARING AN ORGANIC POLYISOCYANATE |
US4258169A (en) * | 1980-03-26 | 1981-03-24 | The Upjohn Company | Polyisocyanate compositions containing in-situ formed pyrophosphate mold release agent and process of making |
US4257995A (en) * | 1979-05-03 | 1981-03-24 | The Upjohn Company | Process for preparing particle board and polyisocyanate-phosphorus compound release agent composition therefor |
US4382108A (en) * | 1981-12-21 | 1983-05-03 | The Upjohn Company | Novel compositions and process |
-
1995
- 1995-06-23 CO CO95027884A patent/CO4410409A1/en unknown
-
1996
- 1996-03-26 CN CN96193363A patent/CN1181765A/en active Pending
- 1996-03-26 KR KR1019970707332A patent/KR19990007809A/en not_active Application Discontinuation
- 1996-03-26 JP JP8531745A patent/JPH11503786A/en active Pending
- 1996-03-26 WO PCT/US1996/004120 patent/WO1996033231A1/en not_active Application Discontinuation
- 1996-03-26 AU AU54319/96A patent/AU5431996A/en not_active Abandoned
- 1996-03-26 EP EP96911430A patent/EP0821706A1/en not_active Withdrawn
- 1996-03-26 BR BR9608163A patent/BR9608163A/en not_active Application Discontinuation
- 1996-03-26 MX MX9707969A patent/MX9707969A/en unknown
- 1996-03-26 CA CA002218254A patent/CA2218254A1/en not_active Abandoned
-
1997
- 1997-10-16 NO NO974785A patent/NO974785D0/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2382468A1 (en) * | 1977-03-01 | 1978-09-29 | Asahi Chemical Ind | PROCESS FOR PREPARING AN ORGANIC POLYISOCYANATE |
US4257995A (en) * | 1979-05-03 | 1981-03-24 | The Upjohn Company | Process for preparing particle board and polyisocyanate-phosphorus compound release agent composition therefor |
US4258169A (en) * | 1980-03-26 | 1981-03-24 | The Upjohn Company | Polyisocyanate compositions containing in-situ formed pyrophosphate mold release agent and process of making |
US4382108A (en) * | 1981-12-21 | 1983-05-03 | The Upjohn Company | Novel compositions and process |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002024612A1 (en) * | 2000-09-20 | 2002-03-28 | Basf Aktiengesellschaft | Method for removing dissolved metals from organic fluids and cleaning agent suited therefor |
EP2825544B1 (en) * | 2012-03-15 | 2018-08-08 | Basf Se | Modified isocyanate compositions and methods of preparing the same |
Also Published As
Publication number | Publication date |
---|---|
CO4410409A1 (en) | 1997-01-09 |
NO974785L (en) | 1997-10-16 |
KR19990007809A (en) | 1999-01-25 |
CA2218254A1 (en) | 1996-10-24 |
NO974785D0 (en) | 1997-10-16 |
AU5431996A (en) | 1996-11-07 |
JPH11503786A (en) | 1999-03-30 |
EP0821706A1 (en) | 1998-02-04 |
BR9608163A (en) | 1999-02-09 |
MX9707969A (en) | 1997-12-31 |
CN1181765A (en) | 1998-05-13 |
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