CA1123817A - Polymeric isocyanate binder with internal release agent - Google Patents
Polymeric isocyanate binder with internal release agentInfo
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- CA1123817A CA1123817A CA335,406A CA335406A CA1123817A CA 1123817 A CA1123817 A CA 1123817A CA 335406 A CA335406 A CA 335406A CA 1123817 A CA1123817 A CA 1123817A
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- phosphate
- polyisocyanate
- carbon atoms
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Abstract
ABSTRACT OF THE DISCLOSURE
The use of polyisocyanates as binders in the preparation of particle boards is subject to the drawback that the boards exhibit a tendency to adhere to the face of the platens used in their formation.
This problem is minimized by incorporating minor amounts of a mixture of certain mono- and di- (saturated or unsaturated aliphatic or aromatic) acid phosphates or the corresponding pyrophosphates, into the polyisocyanate to be used as binder. The polyisocyanates and the acid phosphates and or pyrophosphates, are applied to the particles separately, or after preblending one with the other. Whether the components are applied separately or in combination one with the other, they can each be applied either neat or in the form of an emulsion or emulsions.
The use of polyisocyanates as binders in the preparation of particle boards is subject to the drawback that the boards exhibit a tendency to adhere to the face of the platens used in their formation.
This problem is minimized by incorporating minor amounts of a mixture of certain mono- and di- (saturated or unsaturated aliphatic or aromatic) acid phosphates or the corresponding pyrophosphates, into the polyisocyanate to be used as binder. The polyisocyanates and the acid phosphates and or pyrophosphates, are applied to the particles separately, or after preblending one with the other. Whether the components are applied separately or in combination one with the other, they can each be applied either neat or in the form of an emulsion or emulsions.
Description
3~1'7 BACKGROUND OF THE INVENTION
1. Field of the Invention This invention relates to particle board binders and is more particularly concerned with the use of organic polyisocyanates as particle board binders, with compositions for said use, and with the particle boards so prepared.
1. Field of the Invention This invention relates to particle board binders and is more particularly concerned with the use of organic polyisocyanates as particle board binders, with compositions for said use, and with the particle boards so prepared.
2. Description of the Prior Art The use is now widely recognized of organic poly-- isocyanates, particularly toluene diisocyanate;
1~ methylenebis(phenyl isocyanate~, and polymethylene polyphenyl polyisocyanates, as binders, or as a component or a binder,for the preparation of particle boards; see, for example, U. S. Patents 3,~28,592; 3,440,189; 3,557,263;
1~ methylenebis(phenyl isocyanate~, and polymethylene polyphenyl polyisocyanates, as binders, or as a component or a binder,for the preparation of particle boards; see, for example, U. S. Patents 3,~28,592; 3,440,189; 3,557,263;
3,~36,199; 3,870,665; 3,919,017 and 3,930,110.
In a typical process the binder resins, optionally in the form of a solution or aqueous suspension or emulsion, are applied to or admixèd with the particles of cellulosic material, or other types of material capable of forming particle boàrds, using a tumbler apparatus or blender or other form of agitator. The mixture of particles and binder is then formed into a mat and subjected to heat and pressure using heated platens.
The process can be carried out in a batch operation or continuously. To avoid adhesion of the board so formed to the heated platens it has hitherto been necessary to interpose a sheet, impermeable to isocyanate, between the surface of the board and the platen during the forming process, or to coat-the surface of the platen, prior to each molding operation, wi~h an appropriate.release agent or to coat the surface of the partisles themselves with a - ~ ~. Z38~7 3698A
material which will not adhere to the ~lat:en. Any of these alternatives, particularly where the process is being operated on a continuous basis, is cumber-some and a drawback to what is otherwise a very satisfactory method of making a particle board with highly attractive structural strength properties.
We have now found that the above drawbacks to the use of organic isocyanates as particle board binders can be minimlzed in a very satisfactory manner by incorporating certain phosphorus-containing compounds as internal release agents in the isocyanate compositions so utilized. We are aware of U. S.
Patent 4,024,088 which describes the incorporation of phosphorus-containing compounds as internal release agents in thè preparation of polyether polyurethanes.
We have found that the phosphorus compounds disclosed in this reference are not suitable for use in the process of the present invention.
SU~RY OF THE INVENTION
This invention comprises an improved process for the preparation of particle board in which particles of organic material capable of being compacted are - contacted with a polyisocyanate and the treated particles are subsequently formed into boàrds by the application of heat and pressure, wherein the improvement comprises contacting said particles, in addition to the treatment with polyisocyanate, with from about 0.1 to 20 parts, per 100 parts by weight of polyisocyanate, of a phosphate selected from the class consisting of ~..238~7 6a) acid phosphates of the formulae O O
1` ~
RO - P - OH and~RO) 2 ~ - OH
OH
tI) ~II) and the ammonium, alkali metal and alkaline earthmetal salts thereof;
(b) pyrophosphates rQpresented by those derived from the acid phosphates (I) and (II) and mixtures of (I) and (II);
(c) The O-monoacyl derivatives of the acid phosphates (I) and (II) having the formulae O O
RO - ~ OCORl and (RO)2~ - OCOR
I
OH
(V) (VI) (d) carbamoyl phosphates having the formula O
R2NHCO - O -~(OR) OH
(VII) and the ammonium, alkali metal and alkaline earth metal salts of the compounds of formula (VII);
(e) branched polyphosphates of the formulae O O O O O
RO -~ - O-~(OR~2 and (RO)2P- O -P- O ~ (OR)2 o -P(OR)2 (VIII) ¦ O (IX) ~ o -~(OR)2 (f) polyphosphates cor~esponding to the general formula ~ Z~8~7 3698A
[ROP - ~n (X) including the cyclometaphosphates tn = 3); and (g) mixtuxas of two or more of said compounds; -wherein, in the various formulae shown above, each R is independently selected from the class consisting of alkyl having from 8 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive and, R'-(O-IH-CH~
wherein R' is alkyl having from 8 to 35 carbon atoms, inclusive, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an averaga valu~
from 1 to 5; Rl is hydrocarbyl from 1 to 12 carbon atoms, inclusive; R2 is selected from the class con-sisting of hydrocarbyl from 1 to 12 carbon atoms and hydrocarbyl substituted by at leas~ one additional --NHCOO -P(OR)~ group wherein R has the significance defined above; and n is~an integer. I
The invention also comprises novel compositions com- I
prising organic polyisocyanates having incorporated therein one or more of the aforesaid compounds. The invention also comprises particle board prepared in accordance with the aforesaid process.
The term "alkyl having from 8 to 35 carbon atoms" means a saturated monovalent aliphatic radical, straight chain or .
~.2~7 3698A
branched chain, which has the stated number of carbon atoms in the molecule. Illustrative of such groups are octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, tetra-decyl, pentadecyl, hexadecyl, heptadecyl, octadecyl, nonadecyl, eicosyl, henei.cosyl, docosyl, tricosyl, pentacosyl, hexacosyl, heptacosyl, octacosyl, nonacosyl, triacontyl, pentatriacontyl, and the like, including isomeric forms thereof.
The term "alkenyl having from 8 to 35 carbon atoms"
means a monovalent straight or branched chain aliphatic radical containing at least one double bond, and having the stated number o~ carbon atoms in the molecule. Illustrative of such groups are octenyl, nonenyl, decenyl, undecenyl, dodecenyl, tridecenyl, tetradecenyl, pentadecenyl, hexadecenyl, heptadecenyl, octadecenyl, nonadecenyl, eicosenyl, heneicosenyl, docosenyl, tricosenyl, pentacosenyl, triacontenyl, pentatria--contenyl, and the like, including isomeric forms thereof.
The term "pyrophosphates ~ derived from the acid phosphates (I) and (II) and mixtures of (I) and (II)" has the following meaning. The acid phosphates (I) and (II) are generally prepared in the form of mixture5 of the monoacid phosphate tII) and the diacid phosphate ~I) which mixtures are produced by reaction of the corresponding alcohol ROH, wherein R is as above defined, with phosphorus pentoxide in accordance with procedures well-known in the art for the preparation of acid phosphates; see, ~or example, Kosolapoff, Organophosphorus Compounds, pp 220-221~ John Wiley and Sons, Inc., New York, 1950. The mixture of the mono- and di-acid phosphates so obtained can be separated, if desired, for example by fractional crystallization of the baxium and like ~ ~ 3698A
38~L~
salts as described in the above cited reference. The individual acid phosphates or mixtures of the two can be used in the process of the invention. The pyrophosphates (III) and ~IV) are readily obtained from the corresponding acid phosphates (II) and (I) respectively, by reaction of the latter with a dehydrating agent such as carbonyl chloride, aryl or alkyl monoisocyanates and polyisocyanates, N,N'-dihydrocarbyl-carbodiimides, and the like in accordance with procedures well-known in the art; see, for example, F. Cramer and M. Winter, Chem. Ber. 94, 989 (1961)i ibid 92, 2761 (1959); M. Smith, J. G.
Moffat and H. G. Khorana, J. Amer. Chem. Soc. 80, 6204 (1958);
F. Ramirez, J. F. Màrecek and I. Ugi, JACS 97, 3809 (1975).
The individual acid phosphates (I) and (II) can be separately converted to the corresponding pyrophosphates or mixtures of the two types of acid phosphate (I) and (II) can be converted to the corresponding mixture of pyrophosphates.
In the case of the acid phosphates having the formula (II) above the corresponding pyrophosphates are those represented by the formula:- !
o o ~ ~
(RO)2P- O -P(OR~2 (III) wherein R has the meaning hereinbefore defined. In the case of the acid phosphates having the formula (I) above the corresponding pyrophosphates are a complex mixture whose average composition is represented by the formula:-HO ~-O ~ - -OH (IV) O x wherein x is a number having an average value of 1 or higher and R has the meaning hereinbefore defined.
~-Z~7 3698A
I
The term "hydrocarbyl from 1 to 12 carbon atoms, inclusive" means the monovaIent radical obtained by removing one hydrogen atom from the parent hydrocarbon having the stated carbon atom content. Illustrative of such groups are alkyl such as methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, decyl, dodecyl and the like including isomeric forms thereof; alkenyl such as vinyl, allyl, butenyl, pentenyl, hexenyl, octenyl, decenyl, dodecenyl and the like, including isomeric forms thereof; aralkyl such as benzyl, phenylpropyl, phenethyl, naphthylmethyl, and the likei aryl such as phenyl, tolyl, xylyl, naphthyl, biphenylyl and the like; cycloalkyl such as cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, and the like, including isomeric forms thereof; and cycloalkenyl such as cyclopentenyl, cyclohexenyl, cycloheptenyl, cyclooctenyl and the like including isomeric forms thereof.
The term "alkali metal" has its well recognized meaning as being inclusive of lithium, sodium, potassium, rubidium and caesium. The term "alkaline earth metal"
also has its well recognized meaning as being inclusive of calcium, strontium, m~agnesium and barium.
DETAILED DESCRIPTION OF THE INVENTION
The process of the invention is carried out substantially in accordance with methods previously described in the art in which an organic polyisocyanate is used as the binder resin, or a component thereof, ~see, for example, German Offenlegungsschrift 2610552 and U. S. 3,428,592) with the chief exception that a ~ 3~1~ 3698A
phosphate as hereinbefore defined is employed in combination with the isocyanate composition which is used to treat the particles which are to be bonded together to form the particle board.
Thus, particle board is produced according to the invention by bonding together particles of wood or other cellulosic or organic material capable of being compacted using heat and pressure in the presence o~ a binder system which comprises a combination of an organic polyisocyanate and a phosphate as herein~efore defined, hereinafter referred to as the "phosphate release agent".
~he polyisocyanate and the phosphate release agent can be brought into contact with the particles as separate, individual components or, in a preferred embodiment, the polyisocyanate and phosphate are brought into contact with the particles either simultaneously or after admixture. Whether the polyisocyanate and phosphate are introduced separately or in admixture, they can be employed neat, i.e. without diluents or solvents or one or other or both can be employed in the form of aqueous dispersions or emulsions.
The polyisocyanate component of the binder system can be any organic polyisocyanate which contains at least two isocyanate groups per molecule. Illustrative of ~5 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 two isomers which are available commercially, triphenylmethane triisocyanates, 4,~'-diisocyanatodiphenyl ether, and polymethylene polyphenyl _g_ 3~saA
3~:L7 polyisocyanates. The latter polyisocyanates are mixtures containing from about 25 to about 90 percent by waight of methylenebis(phenyl isocyanate) the remainder of the mixture being polymethylene polyphenyl polyisocyanates of functionality higher than 2Ø Such polyisocyanates and methods for their preparation are well-known in the art; see, for example, U. S. Patents 2,683,730; 2,950,263; 3,012,008 and 3,097,191. These po~yisocyanates are also available in various modified forms. One such form comprises a poly-methylene polyphenyl polyisocyanate as ahove which has beensubjected to heat treatment, generally at temperatures from about 150C to about 300~, until the viscosity (at 25C) hasbeen increased to a value within the range of about 800 to 1500 centipoises. 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 3,793,362.
The polymethylene polyphenyl polyisocyanates are the pre-ferred polyisocyanates for use in the binder systems of the invention. Particularly preferred polymethylene polyphenyl polyisocyanates are those which contain from about 35 to about 65 percent by weight of methylenebis(phenyl isocyanate).
When the organic polyisocyanate is to be employed as binder system in the form of an aqueous emulsion or dispersion in accordance with the invention, the aqueous emulsion or dispersion can be prepar~d using any of the techni~ues known in the art for the preparation of aqueous emulsions or dis-persions, prior to use of the composition as the binder.
Illustratively, the polyisocyanate is dispersed in water in the presence of an emulsifying agent. The latter can be any of 10-- .
3~:L7 the emulsifying agents known in the art including anionic and nonionic agents. Illustrative of nonionic emulsifying agents are polyoxyethylene and polyoxypropylene alcohols and block copolymers of two or more of ethylene oxide, propylene oxide, butylene oxide, and styrene;
alkoxylated alkylphenols such as nonylphenoxy poly(ethylene~
oxy)ethanols; alkoxylated aliphatic alcohols such as ethoxylated and propoxylated aliphatic alcohols containing from about 4 to 18 carbon atoms; glycerides of saturated and unsaturated fatty acids such as stearic, oleic, and ricinoleic acids and the like; 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 like acidsO A
detailed account of such materials is found in Encyclopedia of Chemical Technology, Second Edition, Vol. 19, pp. 531-554, 1969, Interscience Publishers, New York.
The formation of the emulsion or dispersion can be carried out at any time prior to its use as the binder composition, but, preferably, it is carried out within about 3 hours prior to use. Any of the methods conventional in the art or the preparation of aqueous emulsions can be employed in preparing the aqueous polyisocyanate emulsions employed in the process of the invention. Illustratively, the emulsion is for~ed by bringing the polyisocyanate, emulsifying agent and water together under pressure using a conventional spray gun in which the streams of water and polyisocyanate impinge and are mixed under turbulent conditions in the mixing chamber of the spray gun. The emulsion so formed is discharged in the form of a spray which is applied to the cellulosic .
~ ~. 23~7 3698A
particles to be Eormed into boardstock in the manner discussed below.
As discussed above,the phosphate release agent can be brought into contact with the particles as a separate com-ponent in which case it is employed in neat ~orm, i.e.without diluents,or as an aqueous solution or dispersion.
Preferably the phosphate either neat or in diluted form when used alone i.e. separately from the polyisocyanate,is presented to the particles in the form of a spray. However, in a preferred embo~iment of the invention the phosphate release agent and the polyisocyanate are employed together in a single composition. This can be accomplished in several ways. Thus, when the polyisocyanate is employed as binder resin without diluents such as water, the phosphate release agent can be incorporated in the polyisocyanate by simple admixture. Where the polyisocyanate is employed as binder resin in the form of an aqueous emulsion the phosphate release agent can be added as a separate component during the formation of the emulsion or after its formation or, in a particularly advantageous embodiment, the phosphate is premixed with the organic polyisocyanate prior to emulsification of the latter. Thus, the organic polyisocyanate and the phosphate release agent.can be premixed and stored for any desired period prior to formation of the emulsion. Further, when an emulsifying agent is employed ln preparation of the emulsion said agent can also be incorporated into the mixture of organic polyisocyanate and phosphate release agent to form a storage stable composition which can be converted, at any desired time, to an aqueous emulsion for use as a binder resin by simple admixture with water.
3698~ 1 -~.23~7 When the polyisocyanate is employed as binder in the form of an aqueous emulsionl the proportion of organic polyisocyanate present in the said aqueous emulsion is advantag&ously within .
the range of about 0.1 to abou~ 99 percent by weight and preferably within the ran~e of about 25 to about 75 percent by weight.
Whether the phosphate release agent is introduced as a separate component or in combination with the polyisocyanate, the proportion of phosphate release agent employed is within the range of about 0.1 to about 20 parts by weight, per 100 parts of polyisocyanate and, preferably, is within the range of about 2 to about 10 parts by weight, per 100 parts of poly-isocyanate. The proportion of emulsifying agent required to prepare the aqueous emulsion is not critical and varies lS according to the particular emulsifying agent employed but is generally within the range of about 0.1 to about ~0 percent by weight based on polyisocyanate.
The starting material for the particle board comprises particles of cellulosic and the like material capable of being compacted and bonded into the form of boards. Typical such materials are wood particles derived from lumber manufacturing waste such as planar shavings, veneer chips, and the like.
Particles of other cellulosic material such as shredded paper, pulp or vegetable fibres such as corn stalks, straw, bagasse and the like, and of non-cellulosic materials such as scrap polyurethane, polyisocyanurate and like polymer foams can also be used. The methods for producing suitable particles are well known and conventional. If desired, mixtures of cellulosic particles may be used. Particle board has been successfully produced, for example, from wood particle mixtures containing ~ .3~7 3698A
up to about 30~ bark.
The moiqture content of the particles suitably may range from about 0 to about 24 percent by wei~ht. Typically~ particlcs made from lumber waste materials contain about 10 - 20% moisture, and may be used without first being dried.
Particle board is fabricated by spraying the particles with the components of the binder composition, either separately or in combination, while the particles are tumbled or agitated in a blender or like mixing apparatus. Illustratively, a total of about 2 to 8% by weight of the binder system (excluding any water present therein) is added, based on the "bone dry"
weight of the particles, but higher or lower amounts of binder resin may be used in any given application. If desired, other materials, such as wax sizing agents, fire retardants, pigments and the like, may also be added to the particles during the blending step.
After blending sufficiently to produce a uniform mixture, the coated particles are formed into a loose mat or felt, preferably contalning between about 4~ and about 18~ moisture by weight. The mat is then placed in a heated press between caul plates and compressed to consolidate the particles into a board. Pressing times, temperatures and pressures vary widely depending on the thickness of the board produced, the desired density of the board, the size of the particles used, and other factors well known in the art. By way o example, however, for 1/2" thick particle board of medium density, pressures of about 300 to 700 psi and temperatures of about 325 - 375F are typical. Pressing times are typically about 2 - 5 minutes. Because a portion of the moisture present in the mat reacts with polyisocyanate to form ~`.Z3~7 polyurea, as described earlier, the level of moisture present in the mat is not as critical with isocyanate binders as with other binder systems.
The above-described process can be carried out on a batch basis, i.e. individual sheets of par-ticle board can be molded by treating an appropriate amount of particles with the binder resin combination and heating and pressing the treated material.
Alternatively,the process can be carried out in a continuous manner by feeding treated particles in the form of a continuous web or mat through a heating and pressing zone defined by upper and lower continuous steel belts to which, and through which, the necessary heat and pressure are applied.
Whether the process of the invention is carried out in a batchwise or continuous manner, it is found that the particle board produced using the polyisocyanate and phosphate release agent combination of the invention is released readily from the metal plates of the press used in its formation and shows no tendency to stick or adhere to said plates. This is in direct contrast to previous experience with the use of polyisocyanates alone as binder resins as discussed above~
While any of the phosphate release agents defined hereinbefore can be used,-either alone or in combination, in the process of the invention, it is preferred to use the pyrophosphates (III) and (IV) or mixed pyrophosphates derived from mixtures of the acid phosphates (I) and (II).
Thus, the free hydroxyl groups present in the pyrophosphates, or any free hydroxyl groups present in the form of uncon-verted acid phosphate starting material, are generally sufficiently hindered as to be unreactive at ambient ~.238~7 3698A
temperatures with the polyisocyanate employed in the process of the invention and the pyrophosphates can be stored in combination with said polyisocyanate for prolonged periods wi-thout showing any evidence of deterioration. However, when the mixture of pyrophosphate and polyisocyanate is emulsified and employed in the process of the invention the processing temperature and the steam generated in the formation of the particle board are believed to result in hydrolysis of the pyrophosphate with regeneration of the corresponding acid phosphates which latter then serve to facilitate subse~uent release of the particle board from the plates of the press. It is to be understood that the above theory is presented for purposes of explanation only and is not to be construed as limiting in any way the scope of the present invention.
As set forth above, the monoacid phosphates (II) and the di-acid phosphates ~I) and the salts thereof which are employed in the process of the invention are obtained by conventional procedures such as reaction of the corresponding alcohol ROH, wherein R is as herein-above defined, with phosphorus pentoxide; Kosolapoff, ibid. As will be obvious to one skilled in the art, it is possible by using mixtures of two or more different alcohols in the above reaction to obtain a corresponding mixture of acid phosphates ~I) and or (II) wherein the various components of the mixture have different values of the group R. As also set forth above the mixture of mono- and di-acid phosphates obtained in the above reaction can be separated into its individual ~L~.23~:~7 components by conventional methods, such as fractional crystallization and -the like, and the individual compounds so obtained can be employed in the process of the invention.
Alternatively, and preferably, the mixture of mono- and di-acid phosphates obtained in the above reaction can be employed as sucn, withoutseparation, into its components, in the process of the invention or can be converted to the corresponding mixture of pyrophosphates using the procedures discussed here-inbefore, which latter mixture is then employed in the process of the invention~
Illustrative of the acid phosphates of the formula (I) above which can be employed individually or in combination with other acid phosphates in the process of the invention are:
mono-O-octyl, mono~O-nonyl, mono-O-decyl, mono-O-undecyl, mono-O-dodecyl, mono-O-tridecyl, mono-O-tetradecyl, mono-O-penta~
decyl, mono-O-hexadecyl, mono-O-heptadecyl, mono-O-octadecyl, mono-O-nonadecyl, mono-O-eicosyl, mono-O-heneicosyl, mono-O-docosyl, mono-O-tricosyl, mono-O-pentacosyl, mono-O-hexacosyl, mono-O-heptacosyl, mono-O-octacosyl, mono-O-nonacosyl, mono-O-triacontyl, mono-O-pentatriacontyl, mono-O-dodecenyl, mono-O-tridecenyl, mono-O-tetradecenyl, mono-O-pentadecenyl, mono-O-hexadecenyl, mono-O-heptadecenyl, mono-O-octadecenyl, mono-O-nonadecenyl, mono-O-eicosenyl, mono-O-heneicosenyl, mono-O-docosenyl, mono-O-tricosenyl, mono-O-pentacosenyl, mono-O-triacontenyl and mono-O-pentatriacosenyl di-acid phosphates and the diacid phosphates in which the esterifying radical is that derived from lauryl and like monohydric alcohols which have been capped using from about 1 to 5 moles of ethylene oxide.
Illustrative of the acid phosphates of the ~ormula (II) above which can be employed individually or in combination with ~.23~7 other acid phosphates in the proces3 of the invention are:
O,O-di(octyl), O,O-di(nonyl), O,O-di(d~cyl), O,O-di(undecyl), O,O-di(dodecyl), O,O-di(tridecyl), O,O-di(tetradecyl), O,O-di-- (pentadecyl), O,O-di(hexadecyl), o,O-di(heptadecyl), O,O-di-(octadecyl), O,O-di(nonadecyl), O,O-di(eicosyl), O,O-di(heneicosyl), O,O-di(docosyl), O,O-di(tricosyl), O,O-di(pentacosyl), O,O-di-(hexacosyl), O,O-di(heptacosyl),O,O-di(octacosyl), O~O-di-(nonacosyl), O,O-di(triacontyl), O,O-di(pentatriacontyl), O,O-di-(dodacenyl), O,O-di(tridecenyl), O,O-di(tetradecenyl), O,O-di-(pentadecenyl), O,O-di(hexadecenyl), O,O-di(heptadecenyl), O,O-di(octadecenyl), O,O-di(nonadecenyl), O,O-di(eicosenyl), O,O-di(heneicosenyl), O,O-di(docosenyl), O,O-di(tricosenyl), O,O-di(pentacosenyl), O,O-di(triacontenyl), and O,O-di(penta-triacosenyl) mon~acid phosphates, and the diesterified mono acid phosphates in which the esterifying radical is that derived from lauryl and like monohydric alcohols which have been capped with about 1 to 5 moles of ethylene oxide. Illustrative of the latter typesof phosphate which are available, in admixture with the corresponding diacid phosphates,are the materials marketed under the trade name Tryfac by Emery Industries Inc.
Illustrative of the pyrophosphates of the formula tIII) above which can be employed individually or in combination with other pyropho~phates in the process of the invention are:
tetraoctyl, tetranonyl, tetradecyl, tetraundecyl, tetra-dodecyl, tetra(tridecyl), tetra(tetradecyl), tetra(pentadecyl~,tetxa(hexadecyl), tetra(heptadecyl), tetra(octadecyl), tetra-(nonadecyl), tetra(eicosyl), tetra(heneicosyl), tetra(docosyl), tetra~tricosyl), tetra(pentacosyl), tetra~hexacosyl), tetra-(heptacosyl), tetra(octacosyl), tetra(nonacosyl3, tetra~tria--contyl), tetra~pentatriacontyl), tetra(dod~cenyl~, tetra(tridecenyl), * Trademark ~ 3~7 3698A
tetra(tetradecenyl), tetra(pentadecenyl), tetra(hexadecenyl), tetra(heptadecenyl), tetra(octadecenyl), tetra(nonadecenyl), tetra(eicosenyl), tetra~heneicosenyl), tetra(docosenyl), tetra(tricosenyl~, tetra(pentacosenyl), tetra(triacontenyl), and tetra(pentatriacosenyl)pyrophosphates.
Illustrative of the pyrophosphates of formula (IV) above which can be employed individually or in combination with other pyrophosphates in the process of the invention are di~octyl), di(nonyl), di(decyl), di(undecyl), di(dodecyl), di(tridecyl), di(tetradecyl), di(pentadecyl), di(hexadecyl), di(heptadecyl), di(octadecyl), di(nonadecyl~, di(eicosyl), ;
di(heneicosyl), di(docosyl), di(tricosyl), di~pentacosyl), di(hexacosyl), ditheptacosyl), di(octacosyl), di(nonacosyl), di(triacontyl), di(pentatriacontyl), di(dodecenyl), di(tri-decenyl), di(tetradecenyl), di(pentadecenyl), di(hexadecenyl), di(heptadecenyl), di(octadecenyl), di(nonadecenyl), di(eicosenyl), di(heneicosenyl), di(docosenyl), di(tricosenyl), di(pentaco-senyl), di(triacontenyl) and ~i(pentatriacosenyl)pyrophosphates,.
The O-monoacyl derivatives of the acid phosphates (I) and (II), which can be employed in the process of the invention and which are shown as formulae (V) and (VI) above, are readily prepared by procedures well-known in the art.
Illustratively, the corresponding acid phosphate (I) or (II) in the form of its silver or other metal salt, is reacted with the appropriate acyl halide RlCOHal where Hal represents chlorine or bromine and Rl is as hereinbefore defined, using the procedures described by Kosolapoff, ibid, p. 334. Illustra-tive of the O-monoacyl derivatives of the acid phosphates (I) and ~II) are the O-acetyl, O-propionyl, O-octanoyl, O-decanoyl, O-dodscanoyl, O-benzoyl, O-toluoyl, O-phenacetyl derivatives :~.Z3~317 of the various acid phosphates ~I) and (II) exemplified above.
The carbamoyl phosphates haviny the formula (VII) which are employed in the process of -the invention are readily prepared by reaction of the appropriate acid phosphate (I) or (II) with the appropriate hydrocarbyl mono- or polyisocyanate using, for example, the procedure described by F. Cramer and M. Winter, Chem. Ber~ 92, 2761 tl959). Illustrative of such carbamoyl phosphates are the methylcarbamoyl, ethylcarbamoyl, propylcarbamoyl, hexylcarbamoyl, decylcarbamoyl, dodecylcarbamoyl, allylcarbamoyl, hexenyl-carbamoyl, octenylcarbamoyl, decenylcarbamoyl, dodecenyl-carbamoyl, phenylcarbamoyl, tolylcarbamoyl, diphenylylcarbamoyl, benzylcarbamoyl, phenylpxopylcarbamoyl and like hydrocarbamoyl derivatives of the monoacid phosphates (stabilized in the form of their ammonium or alkali metal salts) as exemplified above. The carbamoyl phosphates (VII) may contain free OH
groups due to incomplete conversion of the acid phosphates in the reaction with the appropriate hydrocarbyl isocyanate because of low order of reactivity of the OH groups in question with the isocyanate. Such compounds containing said free OH groups can be used in the process of the invention without producing undesirable side-e~fects because of the low order of reactivity of the OH groups with isocyanate.
The polyphosphates corresponding to the formula (X), which are employed in the process of the invention, are readily prepared by reaction o~ the appropriate trialkylphosphate (RO)3PO, wherein R is as hereinberore defined, with phosphorus pentoxide using the procedures described by Kosolapoff, i~id, p. 341. The polyphosphates are generally complex mixtures 1~.2 3~7 3698A
whose composition is represented generically by the formula (X), and include cyclic compounds (n = 3) having a six-membered ring composed of alternate phosphorus and oxygen atoms.
The polyphosphates corresponding to the formula (VIII) and (IX), which are employed in the process of the invention, are readily prepared by the reaction of the appropriate di or tr~alkylphosphate and the appropriate halophosphate (RO)2 - Hal where Hal is chlorine or bromine, using, for example, the procedure described by Kosolapoff, ibid, p. 338.
The procedure involves elimination of alkyl halide.
In a further embodiment of the invention it is found that the combination of polyisocyanate and phosphate release agent employed as binder in the process of the invention can be used in conjunction with thermosetting resin binders hitherto employed in the art such as phenol-formaldehyde, resorcinol-formaldehyde, melamine-formaldehyde, urea-formaldehyde,urea-furfural and condensed furfuryl alcohol series. Not only does the use of such a combination avoid the problems of adhesion of the finished particle boards to the platens of the press, which problems were previously encountered with a blend of isocyanate and the above type of thermosetting resin binder, but the physical properties of the particle boards so obtaine~ are markedly impro~ed by the use of the combination.
The following preparations and examples describe the manner and process of making and using the invention and set forth the best mode contemplated by the inventors of carry-ing out the invention but are not to be construed as limiting.
~ 3~7 3698A
Preparation 1 Preparation of pyrophosphate from lauryl acid phosphate.
A mixture of 70 g. lauryl acid phosphate (a mixture of O,O-dilauryl monoacid phosphate and O-lauryl di-acid phosphate;
Hooker Chemical Company) and 60 g. of phenyl isocyanate was charged to a dry flask fitted with stirrer, condenser and drying tube, the flask was immersed in an oil bath preheated to 80C and the contents of the flask were stirred while the temperature of the oil bath was slowly raised to 115C. Carbon dioxide was evolved over a period of about 1 hour. When evolution of carbon dioxide had ceased, the reaction mixtuxe was cooled to room temperature and diluted with 100 ml. of chloro-form. The resulting mixture was filtered and the solid so collected (24.8 g. of N,N'-diphenylurea) was washed with chloroform. The combined filtrate and washings were concentrated on a rotary evaporator at a bath temperature of 50C. When most of the solvent had been evaporated, crystals of N,N',N"-triphenylbiuret separated and the evaporation was interrupted to filter off this solid material (6.6 g.). The filtrate was evaporated to dryness and subjected finally to reduced pressure at 50C to remove excess phenyl isocyanate. The residue (70 g.) was the desired pyrophosphate in the form of a colorless to pale yellow li~uid. The infrared spectrum of the product (in CHCl 3 ) did not show any bands characteristic of P-OH bonds but had a strong band at 940 cm characteristic of P-O-P bonds.
Preparation ?
Prepara~ion of pyrophos~ate from lauryl acid phosphate.
A total of 70 g of lauryl acid phosphate (same starting material as used in Preparation 1) was charged to a flask fitted with stirrer, reflux condenser and gas inlet and was heated under 3698~
-~ ~.23~:1 7 nitrogen at ~S - 75C untiL moltcn. The melt: was stirred while a slow stream of phosgene was passed in for a total of 2.5 hours. The temperature was maintained in the above range throughout the addition.
Evolution of gas from the reaction mixture was vigorous in the first hour of the phosgene addition but gradually subsided and was very slow at the end of the period of addition of phosgene. After the addition was complete, the mixture was purged with nitrogen for 15 hours while maintaining the tem~
perature in the above range. At the end of this time the pressure in the reaction flask was gradually reduced to about 1.0 mm. of mercury to remove gaseous hydrogen chloride and carbon dioxide. The viscous residue so obtained solidified completely on allowing to stand overnight. There was thus obtained 66 g.
of pyrophosphate as a solid which melts gradually at abou~ 60C.
Preparation 3 Preparation of pyrophosphate from oleyl acid phosphate.
A mixture of 200 g. of oleyl acid phosphate (comprised o a mi~ture of O,O-dioleyl acid phosphate and O-monooleyl acid phosphate as supplied by Hooker Chemical Company) was reacted with 160 g. of phenyl isocyanate at a temperature of 85 - 90C for 5.5 hours using the procedure described in Preparation 1.
The N,N'-diphenylurea (6~ g.) was removed by ~iltration after the reaction mixture had been diluted with 200 ml.
of chloroform. The iltrate was concentratad-on a rotary evaporator and the excess unreacted phenyl ~ 8~7 3698A
isocyanate was removed by distillation at reduced pressure. N,N',N"-triphenylbiuret crystallized from the oily residue on standing at room temperature.
Removal of the crystals by filtration yielded 196 g.
of a liquid product, the infrared spectrum of which exhibited a band at 940 cm characteristic of P-O-P
bands but showed no bands characteristic of the P-OH
band.
Preparation 4 Preparation of pyrophosphate from lauryl acid phos~hate.
A solution of 30.4 parts by weight of lauryl acid phosphate (same starting material as in Prepar-ation 1) in 21 parts by weight of toluene was charged to a dry reactor previously purged with nitro-gen. The solution was heated to 40C with agitationat which point a solution of 7.6 parts by weight of polymethylene polyphenyl polyisocyanate [eq. wt. =
133; functionality 2.8; containing circa 50 percent methylenebis~phenyl isocyanate)] in 5 parts by weight of toluene was added. The resulting mixture was stirred while a stream of phosgene was intro-duced (ca. 0.1 parts by weight per minute) and the temperature was slowly raised to 80C. The temperature was maintained at this level, with continuous introduction of phosgene until a total of 20 parts by weight of the latter had been intro-duced. The total time of phosgene addition was 5 hr.
50 mins. The reaction mixture was heated at the same temperature for a further 40 minutes after phosgene addition was complete before being heated ~ ~ 2~8L7 369BA
to 90 to 95C and purged with nitrogen for 2 hours to remove excess phosgene. The pressure in the reactor was then reduced until refluxing of toluene commenced and the purging with nitrogen was continued S for a further 2 hr. The toluene was then removed by distillation under reduced pressure, the last traces being removed in vacuo. The residue was cooled to room temperature, treated with diatomaceous earth tCelite 545) and filtered after agitating for 30 minutes.
There was thus obtained 23.7 parts by weight of a mixture of lauryl pyrophosphate and polymethylene polyphenyl polyisocyanate which was found to contain 6~08% w/w of phosphorus.
Preparation 5 Further preparation of pyrophosphate from lauryl acid phosphate.
Using the procedure described in Preparation ~
but replacing the polymethylene polyphenyl polyiso-cyanate there used by an equivalent amount (6.8 parts by weight) of phenyl isocyanate there was obtained`a further batch of lauryl pyrophosphate.
Example 1 A series of samples of wood particle board was prepared using the following procedure from the compon-ents and quantities of components tall parts by weight)shown in Table 1 below.
~ he wood chips("Turner shavings") were placed in a rotating blender drum and the drum was rotated while the p~rticles were sprayed with an aqueous emulsion of the polyisocyanate, water, phosphate and ~.238:17 emulsifying agent. The emulsion was prepared by blending the ~omponents thereof using a Turrex mixer. The resulting emulsion was sprayed with a paint spray gun on to the wood particles while tumbling for 45 - 120 seconds to achieve homo-geneity. The coated particles were formed into a felted mat on a 12" x 12" cold-rolled steel plate with the aid of a plywood forming frame.
After removal of the forming frame, steel bar~
having a thickness corresponding to the desired thickne~s (1/4 n ) of the final particle board were placed along two opposing edges of the aforesaid steel plate and a second 12" x 12" cold-rolled steel plate was placed on top of the mat. The complete assembly was then placed on the lower platen of a Dake press having a capacity of 100,000 lbs. of ~orce. Both platens of the pre~s were pxeheated to a selected temperature shown in Table 1 below.
Pressure was then applied and the time of molding shown in Table 1 was calculated from the point at which the pressure exer~ed on the mat reached 5Q0 psi. At the e~piry of the molding time shown in Table 1 the pressure was released and the particle board was demolded. In all instances it was found that demolding was accom-plished readily with no tendency o the board to stick to the plates with which it was in contact.
This is in direct contrast to the behaviour of a board prepared under identical conditions but without the presence of the lauryl acid * Trademark " s ~,..
l~.Z3817 3698A
phosphate in the emulsion used as binder in preparing th~ bo~rd.
The various samples of particle board so prepared were then subjected to a series of physical tests and the properties so determined are recorded in Table 1.
These properties demonstrate the excellent structural strength properties of the boards.
Board A B C D
Materials used Wood chips 644 644 644 644 Wt. of water in chips 56 56 56 56 Polyisocyanatel 19.219.2 19.2 19.2 Water in emulsion Sl Sl 51 51 Lauryl acid phosphate 1.9 1.9 1.9 1.9 Emulsifying agent 0.10.1 0.1 0.1 * % w/w polyisocyanate 3.03.0 3.0 3.0 * % w/w water 17 17 17 17 * ~ w/w phosphate 0.30.3 0.3 0. 3 * ~ w/w emulsifier 0.016 0.016 0.016 0.016 Platen temp.F 340 340 340 340 Mold time, minutes 1.52.0 2.5 3.0 Physical Properties Dçnsity, pcf 40 41 41 40 Modulus of rupture:
psi 37103600 43~0 4470 Modulus of elast3icity:
p~i (x 10 ) 502 472 540 5~3 4Dry internal bond: psi 102 104 112 90 sWet internal bond psi ?3 24 24 23 .2~8~
Footnotes to ~A~LE 1 ~: Polymethylene polyphe~yl polyisocyanate: eq.
wt. = 133; functionality 2.8; containing clrca 50 percent methylenebis(phenyl isocyanate1-2: Mixture of lauryl d.iacid phosphate and dilauxylmono acid phosphate: Hooker Chemical Company.
s Ethoxylated propoxylated butanol: Witconol~
APEB: Witco Chemical Company.
In a typical process the binder resins, optionally in the form of a solution or aqueous suspension or emulsion, are applied to or admixèd with the particles of cellulosic material, or other types of material capable of forming particle boàrds, using a tumbler apparatus or blender or other form of agitator. The mixture of particles and binder is then formed into a mat and subjected to heat and pressure using heated platens.
The process can be carried out in a batch operation or continuously. To avoid adhesion of the board so formed to the heated platens it has hitherto been necessary to interpose a sheet, impermeable to isocyanate, between the surface of the board and the platen during the forming process, or to coat-the surface of the platen, prior to each molding operation, wi~h an appropriate.release agent or to coat the surface of the partisles themselves with a - ~ ~. Z38~7 3698A
material which will not adhere to the ~lat:en. Any of these alternatives, particularly where the process is being operated on a continuous basis, is cumber-some and a drawback to what is otherwise a very satisfactory method of making a particle board with highly attractive structural strength properties.
We have now found that the above drawbacks to the use of organic isocyanates as particle board binders can be minimlzed in a very satisfactory manner by incorporating certain phosphorus-containing compounds as internal release agents in the isocyanate compositions so utilized. We are aware of U. S.
Patent 4,024,088 which describes the incorporation of phosphorus-containing compounds as internal release agents in thè preparation of polyether polyurethanes.
We have found that the phosphorus compounds disclosed in this reference are not suitable for use in the process of the present invention.
SU~RY OF THE INVENTION
This invention comprises an improved process for the preparation of particle board in which particles of organic material capable of being compacted are - contacted with a polyisocyanate and the treated particles are subsequently formed into boàrds by the application of heat and pressure, wherein the improvement comprises contacting said particles, in addition to the treatment with polyisocyanate, with from about 0.1 to 20 parts, per 100 parts by weight of polyisocyanate, of a phosphate selected from the class consisting of ~..238~7 6a) acid phosphates of the formulae O O
1` ~
RO - P - OH and~RO) 2 ~ - OH
OH
tI) ~II) and the ammonium, alkali metal and alkaline earthmetal salts thereof;
(b) pyrophosphates rQpresented by those derived from the acid phosphates (I) and (II) and mixtures of (I) and (II);
(c) The O-monoacyl derivatives of the acid phosphates (I) and (II) having the formulae O O
RO - ~ OCORl and (RO)2~ - OCOR
I
OH
(V) (VI) (d) carbamoyl phosphates having the formula O
R2NHCO - O -~(OR) OH
(VII) and the ammonium, alkali metal and alkaline earth metal salts of the compounds of formula (VII);
(e) branched polyphosphates of the formulae O O O O O
RO -~ - O-~(OR~2 and (RO)2P- O -P- O ~ (OR)2 o -P(OR)2 (VIII) ¦ O (IX) ~ o -~(OR)2 (f) polyphosphates cor~esponding to the general formula ~ Z~8~7 3698A
[ROP - ~n (X) including the cyclometaphosphates tn = 3); and (g) mixtuxas of two or more of said compounds; -wherein, in the various formulae shown above, each R is independently selected from the class consisting of alkyl having from 8 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive and, R'-(O-IH-CH~
wherein R' is alkyl having from 8 to 35 carbon atoms, inclusive, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an averaga valu~
from 1 to 5; Rl is hydrocarbyl from 1 to 12 carbon atoms, inclusive; R2 is selected from the class con-sisting of hydrocarbyl from 1 to 12 carbon atoms and hydrocarbyl substituted by at leas~ one additional --NHCOO -P(OR)~ group wherein R has the significance defined above; and n is~an integer. I
The invention also comprises novel compositions com- I
prising organic polyisocyanates having incorporated therein one or more of the aforesaid compounds. The invention also comprises particle board prepared in accordance with the aforesaid process.
The term "alkyl having from 8 to 35 carbon atoms" means a saturated monovalent aliphatic radical, straight chain or .
~.2~7 3698A
branched chain, which has the stated number of carbon atoms in the molecule. Illustrative of such groups are octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, tetra-decyl, pentadecyl, hexadecyl, heptadecyl, octadecyl, nonadecyl, eicosyl, henei.cosyl, docosyl, tricosyl, pentacosyl, hexacosyl, heptacosyl, octacosyl, nonacosyl, triacontyl, pentatriacontyl, and the like, including isomeric forms thereof.
The term "alkenyl having from 8 to 35 carbon atoms"
means a monovalent straight or branched chain aliphatic radical containing at least one double bond, and having the stated number o~ carbon atoms in the molecule. Illustrative of such groups are octenyl, nonenyl, decenyl, undecenyl, dodecenyl, tridecenyl, tetradecenyl, pentadecenyl, hexadecenyl, heptadecenyl, octadecenyl, nonadecenyl, eicosenyl, heneicosenyl, docosenyl, tricosenyl, pentacosenyl, triacontenyl, pentatria--contenyl, and the like, including isomeric forms thereof.
The term "pyrophosphates ~ derived from the acid phosphates (I) and (II) and mixtures of (I) and (II)" has the following meaning. The acid phosphates (I) and (II) are generally prepared in the form of mixture5 of the monoacid phosphate tII) and the diacid phosphate ~I) which mixtures are produced by reaction of the corresponding alcohol ROH, wherein R is as above defined, with phosphorus pentoxide in accordance with procedures well-known in the art for the preparation of acid phosphates; see, ~or example, Kosolapoff, Organophosphorus Compounds, pp 220-221~ John Wiley and Sons, Inc., New York, 1950. The mixture of the mono- and di-acid phosphates so obtained can be separated, if desired, for example by fractional crystallization of the baxium and like ~ ~ 3698A
38~L~
salts as described in the above cited reference. The individual acid phosphates or mixtures of the two can be used in the process of the invention. The pyrophosphates (III) and ~IV) are readily obtained from the corresponding acid phosphates (II) and (I) respectively, by reaction of the latter with a dehydrating agent such as carbonyl chloride, aryl or alkyl monoisocyanates and polyisocyanates, N,N'-dihydrocarbyl-carbodiimides, and the like in accordance with procedures well-known in the art; see, for example, F. Cramer and M. Winter, Chem. Ber. 94, 989 (1961)i ibid 92, 2761 (1959); M. Smith, J. G.
Moffat and H. G. Khorana, J. Amer. Chem. Soc. 80, 6204 (1958);
F. Ramirez, J. F. Màrecek and I. Ugi, JACS 97, 3809 (1975).
The individual acid phosphates (I) and (II) can be separately converted to the corresponding pyrophosphates or mixtures of the two types of acid phosphate (I) and (II) can be converted to the corresponding mixture of pyrophosphates.
In the case of the acid phosphates having the formula (II) above the corresponding pyrophosphates are those represented by the formula:- !
o o ~ ~
(RO)2P- O -P(OR~2 (III) wherein R has the meaning hereinbefore defined. In the case of the acid phosphates having the formula (I) above the corresponding pyrophosphates are a complex mixture whose average composition is represented by the formula:-HO ~-O ~ - -OH (IV) O x wherein x is a number having an average value of 1 or higher and R has the meaning hereinbefore defined.
~-Z~7 3698A
I
The term "hydrocarbyl from 1 to 12 carbon atoms, inclusive" means the monovaIent radical obtained by removing one hydrogen atom from the parent hydrocarbon having the stated carbon atom content. Illustrative of such groups are alkyl such as methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, decyl, dodecyl and the like including isomeric forms thereof; alkenyl such as vinyl, allyl, butenyl, pentenyl, hexenyl, octenyl, decenyl, dodecenyl and the like, including isomeric forms thereof; aralkyl such as benzyl, phenylpropyl, phenethyl, naphthylmethyl, and the likei aryl such as phenyl, tolyl, xylyl, naphthyl, biphenylyl and the like; cycloalkyl such as cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl, cyclooctyl, and the like, including isomeric forms thereof; and cycloalkenyl such as cyclopentenyl, cyclohexenyl, cycloheptenyl, cyclooctenyl and the like including isomeric forms thereof.
The term "alkali metal" has its well recognized meaning as being inclusive of lithium, sodium, potassium, rubidium and caesium. The term "alkaline earth metal"
also has its well recognized meaning as being inclusive of calcium, strontium, m~agnesium and barium.
DETAILED DESCRIPTION OF THE INVENTION
The process of the invention is carried out substantially in accordance with methods previously described in the art in which an organic polyisocyanate is used as the binder resin, or a component thereof, ~see, for example, German Offenlegungsschrift 2610552 and U. S. 3,428,592) with the chief exception that a ~ 3~1~ 3698A
phosphate as hereinbefore defined is employed in combination with the isocyanate composition which is used to treat the particles which are to be bonded together to form the particle board.
Thus, particle board is produced according to the invention by bonding together particles of wood or other cellulosic or organic material capable of being compacted using heat and pressure in the presence o~ a binder system which comprises a combination of an organic polyisocyanate and a phosphate as herein~efore defined, hereinafter referred to as the "phosphate release agent".
~he polyisocyanate and the phosphate release agent can be brought into contact with the particles as separate, individual components or, in a preferred embodiment, the polyisocyanate and phosphate are brought into contact with the particles either simultaneously or after admixture. Whether the polyisocyanate and phosphate are introduced separately or in admixture, they can be employed neat, i.e. without diluents or solvents or one or other or both can be employed in the form of aqueous dispersions or emulsions.
The polyisocyanate component of the binder system can be any organic polyisocyanate which contains at least two isocyanate groups per molecule. Illustrative of ~5 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 two isomers which are available commercially, triphenylmethane triisocyanates, 4,~'-diisocyanatodiphenyl ether, and polymethylene polyphenyl _g_ 3~saA
3~:L7 polyisocyanates. The latter polyisocyanates are mixtures containing from about 25 to about 90 percent by waight of methylenebis(phenyl isocyanate) the remainder of the mixture being polymethylene polyphenyl polyisocyanates of functionality higher than 2Ø Such polyisocyanates and methods for their preparation are well-known in the art; see, for example, U. S. Patents 2,683,730; 2,950,263; 3,012,008 and 3,097,191. These po~yisocyanates are also available in various modified forms. One such form comprises a poly-methylene polyphenyl polyisocyanate as ahove which has beensubjected to heat treatment, generally at temperatures from about 150C to about 300~, until the viscosity (at 25C) hasbeen increased to a value within the range of about 800 to 1500 centipoises. 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 3,793,362.
The polymethylene polyphenyl polyisocyanates are the pre-ferred polyisocyanates for use in the binder systems of the invention. Particularly preferred polymethylene polyphenyl polyisocyanates are those which contain from about 35 to about 65 percent by weight of methylenebis(phenyl isocyanate).
When the organic polyisocyanate is to be employed as binder system in the form of an aqueous emulsion or dispersion in accordance with the invention, the aqueous emulsion or dispersion can be prepar~d using any of the techni~ues known in the art for the preparation of aqueous emulsions or dis-persions, prior to use of the composition as the binder.
Illustratively, the polyisocyanate is dispersed in water in the presence of an emulsifying agent. The latter can be any of 10-- .
3~:L7 the emulsifying agents known in the art including anionic and nonionic agents. Illustrative of nonionic emulsifying agents are polyoxyethylene and polyoxypropylene alcohols and block copolymers of two or more of ethylene oxide, propylene oxide, butylene oxide, and styrene;
alkoxylated alkylphenols such as nonylphenoxy poly(ethylene~
oxy)ethanols; alkoxylated aliphatic alcohols such as ethoxylated and propoxylated aliphatic alcohols containing from about 4 to 18 carbon atoms; glycerides of saturated and unsaturated fatty acids such as stearic, oleic, and ricinoleic acids and the like; 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 like acidsO A
detailed account of such materials is found in Encyclopedia of Chemical Technology, Second Edition, Vol. 19, pp. 531-554, 1969, Interscience Publishers, New York.
The formation of the emulsion or dispersion can be carried out at any time prior to its use as the binder composition, but, preferably, it is carried out within about 3 hours prior to use. Any of the methods conventional in the art or the preparation of aqueous emulsions can be employed in preparing the aqueous polyisocyanate emulsions employed in the process of the invention. Illustratively, the emulsion is for~ed by bringing the polyisocyanate, emulsifying agent and water together under pressure using a conventional spray gun in which the streams of water and polyisocyanate impinge and are mixed under turbulent conditions in the mixing chamber of the spray gun. The emulsion so formed is discharged in the form of a spray which is applied to the cellulosic .
~ ~. 23~7 3698A
particles to be Eormed into boardstock in the manner discussed below.
As discussed above,the phosphate release agent can be brought into contact with the particles as a separate com-ponent in which case it is employed in neat ~orm, i.e.without diluents,or as an aqueous solution or dispersion.
Preferably the phosphate either neat or in diluted form when used alone i.e. separately from the polyisocyanate,is presented to the particles in the form of a spray. However, in a preferred embo~iment of the invention the phosphate release agent and the polyisocyanate are employed together in a single composition. This can be accomplished in several ways. Thus, when the polyisocyanate is employed as binder resin without diluents such as water, the phosphate release agent can be incorporated in the polyisocyanate by simple admixture. Where the polyisocyanate is employed as binder resin in the form of an aqueous emulsion the phosphate release agent can be added as a separate component during the formation of the emulsion or after its formation or, in a particularly advantageous embodiment, the phosphate is premixed with the organic polyisocyanate prior to emulsification of the latter. Thus, the organic polyisocyanate and the phosphate release agent.can be premixed and stored for any desired period prior to formation of the emulsion. Further, when an emulsifying agent is employed ln preparation of the emulsion said agent can also be incorporated into the mixture of organic polyisocyanate and phosphate release agent to form a storage stable composition which can be converted, at any desired time, to an aqueous emulsion for use as a binder resin by simple admixture with water.
3698~ 1 -~.23~7 When the polyisocyanate is employed as binder in the form of an aqueous emulsionl the proportion of organic polyisocyanate present in the said aqueous emulsion is advantag&ously within .
the range of about 0.1 to abou~ 99 percent by weight and preferably within the ran~e of about 25 to about 75 percent by weight.
Whether the phosphate release agent is introduced as a separate component or in combination with the polyisocyanate, the proportion of phosphate release agent employed is within the range of about 0.1 to about 20 parts by weight, per 100 parts of polyisocyanate and, preferably, is within the range of about 2 to about 10 parts by weight, per 100 parts of poly-isocyanate. The proportion of emulsifying agent required to prepare the aqueous emulsion is not critical and varies lS according to the particular emulsifying agent employed but is generally within the range of about 0.1 to about ~0 percent by weight based on polyisocyanate.
The starting material for the particle board comprises particles of cellulosic and the like material capable of being compacted and bonded into the form of boards. Typical such materials are wood particles derived from lumber manufacturing waste such as planar shavings, veneer chips, and the like.
Particles of other cellulosic material such as shredded paper, pulp or vegetable fibres such as corn stalks, straw, bagasse and the like, and of non-cellulosic materials such as scrap polyurethane, polyisocyanurate and like polymer foams can also be used. The methods for producing suitable particles are well known and conventional. If desired, mixtures of cellulosic particles may be used. Particle board has been successfully produced, for example, from wood particle mixtures containing ~ .3~7 3698A
up to about 30~ bark.
The moiqture content of the particles suitably may range from about 0 to about 24 percent by wei~ht. Typically~ particlcs made from lumber waste materials contain about 10 - 20% moisture, and may be used without first being dried.
Particle board is fabricated by spraying the particles with the components of the binder composition, either separately or in combination, while the particles are tumbled or agitated in a blender or like mixing apparatus. Illustratively, a total of about 2 to 8% by weight of the binder system (excluding any water present therein) is added, based on the "bone dry"
weight of the particles, but higher or lower amounts of binder resin may be used in any given application. If desired, other materials, such as wax sizing agents, fire retardants, pigments and the like, may also be added to the particles during the blending step.
After blending sufficiently to produce a uniform mixture, the coated particles are formed into a loose mat or felt, preferably contalning between about 4~ and about 18~ moisture by weight. The mat is then placed in a heated press between caul plates and compressed to consolidate the particles into a board. Pressing times, temperatures and pressures vary widely depending on the thickness of the board produced, the desired density of the board, the size of the particles used, and other factors well known in the art. By way o example, however, for 1/2" thick particle board of medium density, pressures of about 300 to 700 psi and temperatures of about 325 - 375F are typical. Pressing times are typically about 2 - 5 minutes. Because a portion of the moisture present in the mat reacts with polyisocyanate to form ~`.Z3~7 polyurea, as described earlier, the level of moisture present in the mat is not as critical with isocyanate binders as with other binder systems.
The above-described process can be carried out on a batch basis, i.e. individual sheets of par-ticle board can be molded by treating an appropriate amount of particles with the binder resin combination and heating and pressing the treated material.
Alternatively,the process can be carried out in a continuous manner by feeding treated particles in the form of a continuous web or mat through a heating and pressing zone defined by upper and lower continuous steel belts to which, and through which, the necessary heat and pressure are applied.
Whether the process of the invention is carried out in a batchwise or continuous manner, it is found that the particle board produced using the polyisocyanate and phosphate release agent combination of the invention is released readily from the metal plates of the press used in its formation and shows no tendency to stick or adhere to said plates. This is in direct contrast to previous experience with the use of polyisocyanates alone as binder resins as discussed above~
While any of the phosphate release agents defined hereinbefore can be used,-either alone or in combination, in the process of the invention, it is preferred to use the pyrophosphates (III) and (IV) or mixed pyrophosphates derived from mixtures of the acid phosphates (I) and (II).
Thus, the free hydroxyl groups present in the pyrophosphates, or any free hydroxyl groups present in the form of uncon-verted acid phosphate starting material, are generally sufficiently hindered as to be unreactive at ambient ~.238~7 3698A
temperatures with the polyisocyanate employed in the process of the invention and the pyrophosphates can be stored in combination with said polyisocyanate for prolonged periods wi-thout showing any evidence of deterioration. However, when the mixture of pyrophosphate and polyisocyanate is emulsified and employed in the process of the invention the processing temperature and the steam generated in the formation of the particle board are believed to result in hydrolysis of the pyrophosphate with regeneration of the corresponding acid phosphates which latter then serve to facilitate subse~uent release of the particle board from the plates of the press. It is to be understood that the above theory is presented for purposes of explanation only and is not to be construed as limiting in any way the scope of the present invention.
As set forth above, the monoacid phosphates (II) and the di-acid phosphates ~I) and the salts thereof which are employed in the process of the invention are obtained by conventional procedures such as reaction of the corresponding alcohol ROH, wherein R is as herein-above defined, with phosphorus pentoxide; Kosolapoff, ibid. As will be obvious to one skilled in the art, it is possible by using mixtures of two or more different alcohols in the above reaction to obtain a corresponding mixture of acid phosphates ~I) and or (II) wherein the various components of the mixture have different values of the group R. As also set forth above the mixture of mono- and di-acid phosphates obtained in the above reaction can be separated into its individual ~L~.23~:~7 components by conventional methods, such as fractional crystallization and -the like, and the individual compounds so obtained can be employed in the process of the invention.
Alternatively, and preferably, the mixture of mono- and di-acid phosphates obtained in the above reaction can be employed as sucn, withoutseparation, into its components, in the process of the invention or can be converted to the corresponding mixture of pyrophosphates using the procedures discussed here-inbefore, which latter mixture is then employed in the process of the invention~
Illustrative of the acid phosphates of the formula (I) above which can be employed individually or in combination with other acid phosphates in the process of the invention are:
mono-O-octyl, mono~O-nonyl, mono-O-decyl, mono-O-undecyl, mono-O-dodecyl, mono-O-tridecyl, mono-O-tetradecyl, mono-O-penta~
decyl, mono-O-hexadecyl, mono-O-heptadecyl, mono-O-octadecyl, mono-O-nonadecyl, mono-O-eicosyl, mono-O-heneicosyl, mono-O-docosyl, mono-O-tricosyl, mono-O-pentacosyl, mono-O-hexacosyl, mono-O-heptacosyl, mono-O-octacosyl, mono-O-nonacosyl, mono-O-triacontyl, mono-O-pentatriacontyl, mono-O-dodecenyl, mono-O-tridecenyl, mono-O-tetradecenyl, mono-O-pentadecenyl, mono-O-hexadecenyl, mono-O-heptadecenyl, mono-O-octadecenyl, mono-O-nonadecenyl, mono-O-eicosenyl, mono-O-heneicosenyl, mono-O-docosenyl, mono-O-tricosenyl, mono-O-pentacosenyl, mono-O-triacontenyl and mono-O-pentatriacosenyl di-acid phosphates and the diacid phosphates in which the esterifying radical is that derived from lauryl and like monohydric alcohols which have been capped using from about 1 to 5 moles of ethylene oxide.
Illustrative of the acid phosphates of the ~ormula (II) above which can be employed individually or in combination with ~.23~7 other acid phosphates in the proces3 of the invention are:
O,O-di(octyl), O,O-di(nonyl), O,O-di(d~cyl), O,O-di(undecyl), O,O-di(dodecyl), O,O-di(tridecyl), O,O-di(tetradecyl), O,O-di-- (pentadecyl), O,O-di(hexadecyl), o,O-di(heptadecyl), O,O-di-(octadecyl), O,O-di(nonadecyl), O,O-di(eicosyl), O,O-di(heneicosyl), O,O-di(docosyl), O,O-di(tricosyl), O,O-di(pentacosyl), O,O-di-(hexacosyl), O,O-di(heptacosyl),O,O-di(octacosyl), O~O-di-(nonacosyl), O,O-di(triacontyl), O,O-di(pentatriacontyl), O,O-di-(dodacenyl), O,O-di(tridecenyl), O,O-di(tetradecenyl), O,O-di-(pentadecenyl), O,O-di(hexadecenyl), O,O-di(heptadecenyl), O,O-di(octadecenyl), O,O-di(nonadecenyl), O,O-di(eicosenyl), O,O-di(heneicosenyl), O,O-di(docosenyl), O,O-di(tricosenyl), O,O-di(pentacosenyl), O,O-di(triacontenyl), and O,O-di(penta-triacosenyl) mon~acid phosphates, and the diesterified mono acid phosphates in which the esterifying radical is that derived from lauryl and like monohydric alcohols which have been capped with about 1 to 5 moles of ethylene oxide. Illustrative of the latter typesof phosphate which are available, in admixture with the corresponding diacid phosphates,are the materials marketed under the trade name Tryfac by Emery Industries Inc.
Illustrative of the pyrophosphates of the formula tIII) above which can be employed individually or in combination with other pyropho~phates in the process of the invention are:
tetraoctyl, tetranonyl, tetradecyl, tetraundecyl, tetra-dodecyl, tetra(tridecyl), tetra(tetradecyl), tetra(pentadecyl~,tetxa(hexadecyl), tetra(heptadecyl), tetra(octadecyl), tetra-(nonadecyl), tetra(eicosyl), tetra(heneicosyl), tetra(docosyl), tetra~tricosyl), tetra(pentacosyl), tetra~hexacosyl), tetra-(heptacosyl), tetra(octacosyl), tetra(nonacosyl3, tetra~tria--contyl), tetra~pentatriacontyl), tetra(dod~cenyl~, tetra(tridecenyl), * Trademark ~ 3~7 3698A
tetra(tetradecenyl), tetra(pentadecenyl), tetra(hexadecenyl), tetra(heptadecenyl), tetra(octadecenyl), tetra(nonadecenyl), tetra(eicosenyl), tetra~heneicosenyl), tetra(docosenyl), tetra(tricosenyl~, tetra(pentacosenyl), tetra(triacontenyl), and tetra(pentatriacosenyl)pyrophosphates.
Illustrative of the pyrophosphates of formula (IV) above which can be employed individually or in combination with other pyrophosphates in the process of the invention are di~octyl), di(nonyl), di(decyl), di(undecyl), di(dodecyl), di(tridecyl), di(tetradecyl), di(pentadecyl), di(hexadecyl), di(heptadecyl), di(octadecyl), di(nonadecyl~, di(eicosyl), ;
di(heneicosyl), di(docosyl), di(tricosyl), di~pentacosyl), di(hexacosyl), ditheptacosyl), di(octacosyl), di(nonacosyl), di(triacontyl), di(pentatriacontyl), di(dodecenyl), di(tri-decenyl), di(tetradecenyl), di(pentadecenyl), di(hexadecenyl), di(heptadecenyl), di(octadecenyl), di(nonadecenyl), di(eicosenyl), di(heneicosenyl), di(docosenyl), di(tricosenyl), di(pentaco-senyl), di(triacontenyl) and ~i(pentatriacosenyl)pyrophosphates,.
The O-monoacyl derivatives of the acid phosphates (I) and (II), which can be employed in the process of the invention and which are shown as formulae (V) and (VI) above, are readily prepared by procedures well-known in the art.
Illustratively, the corresponding acid phosphate (I) or (II) in the form of its silver or other metal salt, is reacted with the appropriate acyl halide RlCOHal where Hal represents chlorine or bromine and Rl is as hereinbefore defined, using the procedures described by Kosolapoff, ibid, p. 334. Illustra-tive of the O-monoacyl derivatives of the acid phosphates (I) and ~II) are the O-acetyl, O-propionyl, O-octanoyl, O-decanoyl, O-dodscanoyl, O-benzoyl, O-toluoyl, O-phenacetyl derivatives :~.Z3~317 of the various acid phosphates ~I) and (II) exemplified above.
The carbamoyl phosphates haviny the formula (VII) which are employed in the process of -the invention are readily prepared by reaction of the appropriate acid phosphate (I) or (II) with the appropriate hydrocarbyl mono- or polyisocyanate using, for example, the procedure described by F. Cramer and M. Winter, Chem. Ber~ 92, 2761 tl959). Illustrative of such carbamoyl phosphates are the methylcarbamoyl, ethylcarbamoyl, propylcarbamoyl, hexylcarbamoyl, decylcarbamoyl, dodecylcarbamoyl, allylcarbamoyl, hexenyl-carbamoyl, octenylcarbamoyl, decenylcarbamoyl, dodecenyl-carbamoyl, phenylcarbamoyl, tolylcarbamoyl, diphenylylcarbamoyl, benzylcarbamoyl, phenylpxopylcarbamoyl and like hydrocarbamoyl derivatives of the monoacid phosphates (stabilized in the form of their ammonium or alkali metal salts) as exemplified above. The carbamoyl phosphates (VII) may contain free OH
groups due to incomplete conversion of the acid phosphates in the reaction with the appropriate hydrocarbyl isocyanate because of low order of reactivity of the OH groups in question with the isocyanate. Such compounds containing said free OH groups can be used in the process of the invention without producing undesirable side-e~fects because of the low order of reactivity of the OH groups with isocyanate.
The polyphosphates corresponding to the formula (X), which are employed in the process of the invention, are readily prepared by reaction o~ the appropriate trialkylphosphate (RO)3PO, wherein R is as hereinberore defined, with phosphorus pentoxide using the procedures described by Kosolapoff, i~id, p. 341. The polyphosphates are generally complex mixtures 1~.2 3~7 3698A
whose composition is represented generically by the formula (X), and include cyclic compounds (n = 3) having a six-membered ring composed of alternate phosphorus and oxygen atoms.
The polyphosphates corresponding to the formula (VIII) and (IX), which are employed in the process of the invention, are readily prepared by the reaction of the appropriate di or tr~alkylphosphate and the appropriate halophosphate (RO)2 - Hal where Hal is chlorine or bromine, using, for example, the procedure described by Kosolapoff, ibid, p. 338.
The procedure involves elimination of alkyl halide.
In a further embodiment of the invention it is found that the combination of polyisocyanate and phosphate release agent employed as binder in the process of the invention can be used in conjunction with thermosetting resin binders hitherto employed in the art such as phenol-formaldehyde, resorcinol-formaldehyde, melamine-formaldehyde, urea-formaldehyde,urea-furfural and condensed furfuryl alcohol series. Not only does the use of such a combination avoid the problems of adhesion of the finished particle boards to the platens of the press, which problems were previously encountered with a blend of isocyanate and the above type of thermosetting resin binder, but the physical properties of the particle boards so obtaine~ are markedly impro~ed by the use of the combination.
The following preparations and examples describe the manner and process of making and using the invention and set forth the best mode contemplated by the inventors of carry-ing out the invention but are not to be construed as limiting.
~ 3~7 3698A
Preparation 1 Preparation of pyrophosphate from lauryl acid phosphate.
A mixture of 70 g. lauryl acid phosphate (a mixture of O,O-dilauryl monoacid phosphate and O-lauryl di-acid phosphate;
Hooker Chemical Company) and 60 g. of phenyl isocyanate was charged to a dry flask fitted with stirrer, condenser and drying tube, the flask was immersed in an oil bath preheated to 80C and the contents of the flask were stirred while the temperature of the oil bath was slowly raised to 115C. Carbon dioxide was evolved over a period of about 1 hour. When evolution of carbon dioxide had ceased, the reaction mixtuxe was cooled to room temperature and diluted with 100 ml. of chloro-form. The resulting mixture was filtered and the solid so collected (24.8 g. of N,N'-diphenylurea) was washed with chloroform. The combined filtrate and washings were concentrated on a rotary evaporator at a bath temperature of 50C. When most of the solvent had been evaporated, crystals of N,N',N"-triphenylbiuret separated and the evaporation was interrupted to filter off this solid material (6.6 g.). The filtrate was evaporated to dryness and subjected finally to reduced pressure at 50C to remove excess phenyl isocyanate. The residue (70 g.) was the desired pyrophosphate in the form of a colorless to pale yellow li~uid. The infrared spectrum of the product (in CHCl 3 ) did not show any bands characteristic of P-OH bonds but had a strong band at 940 cm characteristic of P-O-P bonds.
Preparation ?
Prepara~ion of pyrophos~ate from lauryl acid phosphate.
A total of 70 g of lauryl acid phosphate (same starting material as used in Preparation 1) was charged to a flask fitted with stirrer, reflux condenser and gas inlet and was heated under 3698~
-~ ~.23~:1 7 nitrogen at ~S - 75C untiL moltcn. The melt: was stirred while a slow stream of phosgene was passed in for a total of 2.5 hours. The temperature was maintained in the above range throughout the addition.
Evolution of gas from the reaction mixture was vigorous in the first hour of the phosgene addition but gradually subsided and was very slow at the end of the period of addition of phosgene. After the addition was complete, the mixture was purged with nitrogen for 15 hours while maintaining the tem~
perature in the above range. At the end of this time the pressure in the reaction flask was gradually reduced to about 1.0 mm. of mercury to remove gaseous hydrogen chloride and carbon dioxide. The viscous residue so obtained solidified completely on allowing to stand overnight. There was thus obtained 66 g.
of pyrophosphate as a solid which melts gradually at abou~ 60C.
Preparation 3 Preparation of pyrophosphate from oleyl acid phosphate.
A mixture of 200 g. of oleyl acid phosphate (comprised o a mi~ture of O,O-dioleyl acid phosphate and O-monooleyl acid phosphate as supplied by Hooker Chemical Company) was reacted with 160 g. of phenyl isocyanate at a temperature of 85 - 90C for 5.5 hours using the procedure described in Preparation 1.
The N,N'-diphenylurea (6~ g.) was removed by ~iltration after the reaction mixture had been diluted with 200 ml.
of chloroform. The iltrate was concentratad-on a rotary evaporator and the excess unreacted phenyl ~ 8~7 3698A
isocyanate was removed by distillation at reduced pressure. N,N',N"-triphenylbiuret crystallized from the oily residue on standing at room temperature.
Removal of the crystals by filtration yielded 196 g.
of a liquid product, the infrared spectrum of which exhibited a band at 940 cm characteristic of P-O-P
bands but showed no bands characteristic of the P-OH
band.
Preparation 4 Preparation of pyrophosphate from lauryl acid phos~hate.
A solution of 30.4 parts by weight of lauryl acid phosphate (same starting material as in Prepar-ation 1) in 21 parts by weight of toluene was charged to a dry reactor previously purged with nitro-gen. The solution was heated to 40C with agitationat which point a solution of 7.6 parts by weight of polymethylene polyphenyl polyisocyanate [eq. wt. =
133; functionality 2.8; containing circa 50 percent methylenebis~phenyl isocyanate)] in 5 parts by weight of toluene was added. The resulting mixture was stirred while a stream of phosgene was intro-duced (ca. 0.1 parts by weight per minute) and the temperature was slowly raised to 80C. The temperature was maintained at this level, with continuous introduction of phosgene until a total of 20 parts by weight of the latter had been intro-duced. The total time of phosgene addition was 5 hr.
50 mins. The reaction mixture was heated at the same temperature for a further 40 minutes after phosgene addition was complete before being heated ~ ~ 2~8L7 369BA
to 90 to 95C and purged with nitrogen for 2 hours to remove excess phosgene. The pressure in the reactor was then reduced until refluxing of toluene commenced and the purging with nitrogen was continued S for a further 2 hr. The toluene was then removed by distillation under reduced pressure, the last traces being removed in vacuo. The residue was cooled to room temperature, treated with diatomaceous earth tCelite 545) and filtered after agitating for 30 minutes.
There was thus obtained 23.7 parts by weight of a mixture of lauryl pyrophosphate and polymethylene polyphenyl polyisocyanate which was found to contain 6~08% w/w of phosphorus.
Preparation 5 Further preparation of pyrophosphate from lauryl acid phosphate.
Using the procedure described in Preparation ~
but replacing the polymethylene polyphenyl polyiso-cyanate there used by an equivalent amount (6.8 parts by weight) of phenyl isocyanate there was obtained`a further batch of lauryl pyrophosphate.
Example 1 A series of samples of wood particle board was prepared using the following procedure from the compon-ents and quantities of components tall parts by weight)shown in Table 1 below.
~ he wood chips("Turner shavings") were placed in a rotating blender drum and the drum was rotated while the p~rticles were sprayed with an aqueous emulsion of the polyisocyanate, water, phosphate and ~.238:17 emulsifying agent. The emulsion was prepared by blending the ~omponents thereof using a Turrex mixer. The resulting emulsion was sprayed with a paint spray gun on to the wood particles while tumbling for 45 - 120 seconds to achieve homo-geneity. The coated particles were formed into a felted mat on a 12" x 12" cold-rolled steel plate with the aid of a plywood forming frame.
After removal of the forming frame, steel bar~
having a thickness corresponding to the desired thickne~s (1/4 n ) of the final particle board were placed along two opposing edges of the aforesaid steel plate and a second 12" x 12" cold-rolled steel plate was placed on top of the mat. The complete assembly was then placed on the lower platen of a Dake press having a capacity of 100,000 lbs. of ~orce. Both platens of the pre~s were pxeheated to a selected temperature shown in Table 1 below.
Pressure was then applied and the time of molding shown in Table 1 was calculated from the point at which the pressure exer~ed on the mat reached 5Q0 psi. At the e~piry of the molding time shown in Table 1 the pressure was released and the particle board was demolded. In all instances it was found that demolding was accom-plished readily with no tendency o the board to stick to the plates with which it was in contact.
This is in direct contrast to the behaviour of a board prepared under identical conditions but without the presence of the lauryl acid * Trademark " s ~,..
l~.Z3817 3698A
phosphate in the emulsion used as binder in preparing th~ bo~rd.
The various samples of particle board so prepared were then subjected to a series of physical tests and the properties so determined are recorded in Table 1.
These properties demonstrate the excellent structural strength properties of the boards.
Board A B C D
Materials used Wood chips 644 644 644 644 Wt. of water in chips 56 56 56 56 Polyisocyanatel 19.219.2 19.2 19.2 Water in emulsion Sl Sl 51 51 Lauryl acid phosphate 1.9 1.9 1.9 1.9 Emulsifying agent 0.10.1 0.1 0.1 * % w/w polyisocyanate 3.03.0 3.0 3.0 * % w/w water 17 17 17 17 * ~ w/w phosphate 0.30.3 0.3 0. 3 * ~ w/w emulsifier 0.016 0.016 0.016 0.016 Platen temp.F 340 340 340 340 Mold time, minutes 1.52.0 2.5 3.0 Physical Properties Dçnsity, pcf 40 41 41 40 Modulus of rupture:
psi 37103600 43~0 4470 Modulus of elast3icity:
p~i (x 10 ) 502 472 540 5~3 4Dry internal bond: psi 102 104 112 90 sWet internal bond psi ?3 24 24 23 .2~8~
Footnotes to ~A~LE 1 ~: Polymethylene polyphe~yl polyisocyanate: eq.
wt. = 133; functionality 2.8; containing clrca 50 percent methylenebis(phenyl isocyanate1-2: Mixture of lauryl d.iacid phosphate and dilauxylmono acid phosphate: Hooker Chemical Company.
s Ethoxylated propoxylated butanol: Witconol~
APEB: Witco Chemical Company.
4: Tests carried out in accordance with ASTM-1037-72.
5: Tests carried out in accordance with German V-100 specifications.
~ Calculated on dry weight of wood particle~.
Example 2 A series of samples of wood particle board was prepared using the procedure described in Example 1 using ~he various components and quantities (all parts by weight) shown in Table 2 below, The mold time shown in the Table for samples E and F is the time for which the mat was maintained under pressure (500 psi) after the internal temperature of the mat (as determined by a thermocouple inserted therein) had reached 130F.
Sample G was a control sample molded as described in Example 1. The physical proper~ies determined for each of the finished particle boards are also shown in Table 2 and demonstrate the excellent structural strength of the various samples. All of the samples demolded readily and showed no sign of adhering to the steel plates used in their preparation.
3~
* Trademark -2~-.
:~.Z3~ .7 3 6 98A
T~ 2 ...
Board E F G
Materials used Wood chips 644 644 644 Wt. of water in chips 56 56 56 Polyisocyanate (same as Ex. 1) 21 42 21 Water in emulsion56 56 5S
Lauryl pyrophosphate 2.1 4.2 2.1 Emulsifying agen~ (same as Ex. 1) 0 .1 0.1 0.1 * % w/w polyisocyanate 3.3 6.6 3.3 * % w/w water 17.4 17.4 17.4 * % w/w pyrophosphate 0.33 0.65 0.33 * ~ w/w emulsifier0.016 0.016 0.016 Platen temp. F 355 355 355 Mold time, minutes2 2.
Physical Properties Density: pcf 41 41 42 Modulus of rupture: psi 5130 5090 5320 Modulus of elasticity: psi (x 10 ) 505 513 521 Dry internal bond: psi 128 141 132 Wet internal bond: psi 32 38 31 Footnotes to TABLE 2 ~: Prepared as described in Preparation 1.
. 2: Tests carried out in accordance with ASTM 1037-72.
3: Tests carried out in accordance with German V-100 qpecifications.
* Calculated on dry weight of wood particles.
Example 3 A serie~ of samples of wood particle board was prepared _~9~
~.
. ;. .~, ~.2 3 ~1 ~ 3698A
using exactly the same reactants and proportions shown in Example 1 and using exactly the procedure described in that Example, save tha~ the platens of the press were preheated to 400F and maintained thereat for S the various molding times shown in T~ble 3 below. The physical properties of the samples so prepared are also recorded in Table 3 and show that these samples all possessed excellent structural strength. None of the samples ~howed any tendency to adhere to the molding plates during demolding.
Board H I J K L
. ... ~
Mold time, minutes 1.0 1.5 2.0 2.5 3.0 Physical Properties Density: pcf 40 40 41 40 40 Modulus of rupture: psi 2760 3530 3150 3210 3370 Modulus of elasticity: ps~ 409 472 441 438 454 (x 10 ) Dry internal bond: psi94 102 88 107 107 Wet internal bond: psi23 24 23 25 24 Footnotes to TABLE 3 I: Tests carried out in accordance with ASTM 1037-72.
2: Tests carried out in accordance with German V-100 specifications.
Example 4 A series of samples of wood particle board was prepared usi~g the procedure described in Example 1 but varying the nature of the polyisocyanate and employing, in place of the lauryl acid phosphate, the pyrophosphate derived from oleyl acid phosphate pr~pared as described in Preparation 3. The various components and the proportions thPreof (all parts by weight) are shown in Table 4 below : , -30-. .; .~, .
~ ~.23~17 3698A
together with the physical properties determined on the ~inished samples. The thickness of the board samples in all cases was 3/8 inch (spacer bars of appropriate thickness were used). None of the samples showed any tendency to stick to the molding plates during demolding. Th~ physical properties of the various samples show that they all have excellent structural strength.
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I h O ~ ~ (D ~ rt ~ O
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Footnotes to T~BLE 4 : Liquid prepolymer of methylenebis(phenyl isocyanate):
Eq. wt. = 181 2 : Polymethylene polyphenyl polyisocyanate containing circa 65 percent methylenebis(phenyl isocyanate): eq. wt. - 133 3 : Polymethylene polyphenyl polyisocyanate containiny circa 45 percent methylenebis(phenyl isocyanate):eq. wt. = 133.5 4 : Liquid methylenebis(phenyl isocyanate) prepared in accordance with U. S. 3,384,653: eq. wt. = 143 5 : Polymethylene polyphenyl polyisocyanate containing circa 35 peroent methylenebis(phenyl isocyanate): eq. wt. 140
~ Calculated on dry weight of wood particle~.
Example 2 A series of samples of wood particle board was prepared using the procedure described in Example 1 using ~he various components and quantities (all parts by weight) shown in Table 2 below, The mold time shown in the Table for samples E and F is the time for which the mat was maintained under pressure (500 psi) after the internal temperature of the mat (as determined by a thermocouple inserted therein) had reached 130F.
Sample G was a control sample molded as described in Example 1. The physical proper~ies determined for each of the finished particle boards are also shown in Table 2 and demonstrate the excellent structural strength of the various samples. All of the samples demolded readily and showed no sign of adhering to the steel plates used in their preparation.
3~
* Trademark -2~-.
:~.Z3~ .7 3 6 98A
T~ 2 ...
Board E F G
Materials used Wood chips 644 644 644 Wt. of water in chips 56 56 56 Polyisocyanate (same as Ex. 1) 21 42 21 Water in emulsion56 56 5S
Lauryl pyrophosphate 2.1 4.2 2.1 Emulsifying agen~ (same as Ex. 1) 0 .1 0.1 0.1 * % w/w polyisocyanate 3.3 6.6 3.3 * % w/w water 17.4 17.4 17.4 * % w/w pyrophosphate 0.33 0.65 0.33 * ~ w/w emulsifier0.016 0.016 0.016 Platen temp. F 355 355 355 Mold time, minutes2 2.
Physical Properties Density: pcf 41 41 42 Modulus of rupture: psi 5130 5090 5320 Modulus of elasticity: psi (x 10 ) 505 513 521 Dry internal bond: psi 128 141 132 Wet internal bond: psi 32 38 31 Footnotes to TABLE 2 ~: Prepared as described in Preparation 1.
. 2: Tests carried out in accordance with ASTM 1037-72.
3: Tests carried out in accordance with German V-100 qpecifications.
* Calculated on dry weight of wood particles.
Example 3 A serie~ of samples of wood particle board was prepared _~9~
~.
. ;. .~, ~.2 3 ~1 ~ 3698A
using exactly the same reactants and proportions shown in Example 1 and using exactly the procedure described in that Example, save tha~ the platens of the press were preheated to 400F and maintained thereat for S the various molding times shown in T~ble 3 below. The physical properties of the samples so prepared are also recorded in Table 3 and show that these samples all possessed excellent structural strength. None of the samples ~howed any tendency to adhere to the molding plates during demolding.
Board H I J K L
. ... ~
Mold time, minutes 1.0 1.5 2.0 2.5 3.0 Physical Properties Density: pcf 40 40 41 40 40 Modulus of rupture: psi 2760 3530 3150 3210 3370 Modulus of elasticity: ps~ 409 472 441 438 454 (x 10 ) Dry internal bond: psi94 102 88 107 107 Wet internal bond: psi23 24 23 25 24 Footnotes to TABLE 3 I: Tests carried out in accordance with ASTM 1037-72.
2: Tests carried out in accordance with German V-100 specifications.
Example 4 A series of samples of wood particle board was prepared usi~g the procedure described in Example 1 but varying the nature of the polyisocyanate and employing, in place of the lauryl acid phosphate, the pyrophosphate derived from oleyl acid phosphate pr~pared as described in Preparation 3. The various components and the proportions thPreof (all parts by weight) are shown in Table 4 below : , -30-. .; .~, .
~ ~.23~17 3698A
together with the physical properties determined on the ~inished samples. The thickness of the board samples in all cases was 3/8 inch (spacer bars of appropriate thickness were used). None of the samples showed any tendency to stick to the molding plates during demolding. Th~ physical properties of the various samples show that they all have excellent structural strength.
- z ~ -O ~ _ 3 ~ ~ o ~t I-- P~ ~ t rt 1-- o It rt ~ ~ t P
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n to ~
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o~ ~ o ~V o ~, ~' _ ~ ~ o \-_ Ul CO ~D a~ ~
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~ ~ ~ o ~ ~ 0 w a~ co o~ ~ ~ o O
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~ ~ ~ O - ~_ ~3 _ _ ~ --_.
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Footnotes to T~BLE 4 : Liquid prepolymer of methylenebis(phenyl isocyanate):
Eq. wt. = 181 2 : Polymethylene polyphenyl polyisocyanate containing circa 65 percent methylenebis(phenyl isocyanate): eq. wt. - 133 3 : Polymethylene polyphenyl polyisocyanate containiny circa 45 percent methylenebis(phenyl isocyanate):eq. wt. = 133.5 4 : Liquid methylenebis(phenyl isocyanate) prepared in accordance with U. S. 3,384,653: eq. wt. = 143 5 : Polymethylene polyphenyl polyisocyanate containing circa 35 peroent methylenebis(phenyl isocyanate): eq. wt. 140
6 : Polymethylene polyphenyl polyisocyanate containing circa 35 percent methylenebis(phenyl isocyanate): eq. wt. 140
7 : Polymethylene polyphenyl polyisocyanate containing circa 70 percent methylenebis(phenyl isocyanate): eq. wt. = 133
8 : Same as Example 1
9 : Toluene diisocyanate : Testscarried out in accordance with ASTM 1037-72 1l , Tests carried out in accordance with German V-100 specifications Example S
This example illustrates the preparation of particle board in accordance with the invention using a binder composition in which no extraneous emulsiying agent is present and the polyisocyanate was applied neat, i.e.
not in the form of an aqueous emulsion.
A series of samples of wood particle board was prepared using the various components and ~uantities (all parts by weight) shown in Table 5 below and using the procedure described in Example 1 with the exception that the wood particles were first sprayed with the stated amount of water and thereafter were sprayed with a mixture of the polyisocyanate and the phcsphate release agent. The 3Q physical properties determined for each of the finished :~.Z38~
particle boards are also shown in Table 5 and demonstrate the excellent structural strength of the various samples. All of the samples demolded readily and showed no sign of adhering to the steel plates used in their preparation.
~oard_ W X Y Z zZ_ Materials Wood chips 644 644 644 644 644 1~ Wt. water in chips 565S 56 56 56 Polyisocyanate 38.638.6 38.6 38.6 38.6 (same as Ex. 1) Water 56 56 56 56 56 Lauryl pyrophosphate 3.9 3.9 3.9 3.9 3.9 ~same as Ex. 2) * % w/w polyisocyanate 6 6 6 6 6 * % w/w water total 17.4 17.4 17.4 17.4 17.4 * % w/w pyrophosphate 0.6 0.6 0.6 0.6 0.6 Mold time (minutes) 2 2.5 3.0 2 2.5 Board thickness (inches) 3/8 3/8 3/8 1/2 1/2 Physical pro~rties Density pcf ~2 41 42 40 41 Modulus of rupture:
psi 5320 5186 5787 4325 4B10 IModulus of elasti3ity:
psi (x 10 ) 501 510 564 377 365 lDry internal bond: psi 135 133 141 lB3 178 2Wet internal bond: psi 43 42 46 50 4 Footnotes to TABLE 5 * Calculated on dry weight of wood particles I Testscarried out in accordance with ASTM 1037-72 2 Testscarried out in accordancP with German V-100 specifications ~3.~3~:~7 Example 6 This example illustrates the preparation of three particle boards in accordance with the process o~ the invention from "wafer" chips having varying dimensions as large as 2" x 2" x 1/32" and supplied by Weldwood of Canada, Ltd. No extraneous water or emulsifying agent was used and the polyisocyanate and phosphate release agent were applied neat.
A series of samples of particle board from the wafer chips was prepared using the various components and quantities (all parts by weight) shown in Table 6 below and using the procedure described in Example 1 with the exception that the wood wafers were sprayed with a mixture of the polyisocyanate and the phosphate release agent and not with an aqueous emulsion as in Example 1 and that aluminum molding plates were used.
All of the samples demolded readily and showed no sign of adhering to the aluminum plates used in their prepar-ation. The excellent structural strength properties of the resulting particle boards, as evidenced by the high modulus of rupture shown in Table 6, compare very favorably with the low value of this parameter (2500 psi) determined in a board available commercially and prepared from the same type of wafer chips using a phenol-formaldehyde resin binder.
~.2~ 7 Board AA BB CC
Wafer chips 955 955 955 Polyisocyanate 19.1 50 50 Lauryl pyrophosphate (same as Ex. 2) 2.5 6.5 6.5 * % w/w polyisocyanate 2 5.2 5.2 * % w/w total water 4.7 4.7 4.7 * ~ w/w pyrophosphate 0.260.68 0.68 Mold time (mins.) 4.5 4 4.5 Board.thickness ~in.) l/2 l/2 1/2 Density, pcf 46 43 45 Modulus of rupture:psi 7317 7946 10,860 * Calcd. on dry weight of wood wafers Polymethylene polyphenyl polyisocyanate: eq. wt. - 139:
functionality 3Ø Viscosity at 25C = 700 cps: contain-ing circa 35 percent methylenebis(phenyl isocyanate).
Example 7 This example illustrates the preparation of a series of particle boards using polyisocyanate binders in com-bination with various commercially available phosphates in amounts corresponding to approximately 0.7 percent w/w phosphorus in the binder resin combination.
The various samples were prepared using the various components and guantities (all parts by weight) shown in Table 7 and using the procedure described in Example 1 with the exception that no emulsifying agent was employed, and the wat~r was sprayed onto the chips first, followed by the isocyanate mixed with the release agent. A11 of the samples demolded readily and showed no sign of adhering 3~
to the steel plates used in their preparation. In contrast, a control board, prepared in exactly the same manner but omitting the use of a phosphate release agent adhered to the steel plates used in the preparation and could not be demolded without damage to the surface of the board.
~.23~ 7 O O U~ O ~ ~D
~D CO ~ ~1 :~
~ ~r O O ~D O U~ ~ ~ ~r _ _ _ U~
~ r~
o o ~ o u~ lO ~ ~r H ~ ~ CO t~
i-l ~
_ _ . _ _ _ _ . _ _ . _ _ . . _ _ _ _ . _ _ _ _ _ C~:>
O O ~D O 1` ~ N ~ N
3: .. _ ._ ____ _ . ... , _ .. _ _ . __ ...... _.. __ . _._ _.. ___ ~O
O~
O O ~ O ~
~) ~
_ O O U~ O 0 ~ r N
~D CO t~ ~1 r~ ~ ~ _l ,1 ~ _ ___ ... _. _ , .... . . .. _.
.
O O ~D O ~i ~9 ~ ~ ~
~1 _~
~ .
O O ~D O CO ~D N ~ ~I
a ~
~ ~o a o . ,a m x ~ .c ~ $
U
J~ 'd N S 0 3 Q. ~ U ~ r) ~ Q O E3 9C h U U U U V h O ~ Q ~a ~1 0 h ~1 ~ 0 5 ~ 1~5 . Q O h #
-~ -- 3q-;
~.23~:L~
Footnotes to TABLE 7 -Alkyl acid phosphate derived from lauryl alcohol prereacted with 3 molar proportions of ethylene oxide;
Textilana Division of ~enkel Inc., Hawthorne, CaliEornia.
2 Lauryl acid phosphate; Emery Industries Inc., Mauldin, South Carolina.
3 Alkyl acid phosphate derived from ethoxylated lauryl alcohol; Emery Industries Inc.
Alkyl acid phosphate derived from ethoxylated mid-chain branched aliphatic alcohol; Emery Industries, Inc.
5 Alkyl acid phosphate derived from n-octyl alcohol;
Textilana, ibid.
' 10 6 Alkyl acid phosphate derived from ethoxylated lauryl alcohol; Emery Industries Inc.
7 Prepared as described in Preparation 5.
* Calcd. on dry weight of wood wafers.
Example 8 A further series of particle board samples was prepared using the same phosphate release agents and procedure employed in Example 7 but at iower levels of concentration in the binder resin combination. The various components and the proportions thereof ~all parts by weight) are shown in Table 8 below together with the physical properties determined on certain of the samples. All the samples could be demolded without damage to the board or signi~icant adhesion to the mold plates. The samples prepared using the higher concentrations of phosphate release agent slid out from between the mold plates when demolded whereas some of those prepared using the lower concentrations of phosphate release agent (OO, QQ, and UU) required assistance, e.e. tapping of the mold plates, in order to eff2ct releaseO
All the samples had a thickness of 1/2" in the final board.
æ
0 ~ O O ~ O r~ O ~
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I I I I i ~ D
~ l l l ~ l co co ~ o o~ t co o ~ ~
~ I I I I I ~ co al o o~
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, ~ 3 ~o . . .
cr~ ~
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a~ ~I o o~
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Z Z ~ ~:
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~ P
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O O
_ æ æ z z Example 9 This example illustrates the use of a binder re~in combination in accordance with the invention in association with a phenol-formaldehyde resin binder of the prior art.
All of the samples (1/2" thickness) were prepared using the procedure described in Example 1, with the exceptions detailed below, and using the reactants and proportions (all parts by weight) set forth in Table 9. In the case of Boards YY and ZZ the phenol-formaldehyde resin was incorporated in the emulsion of the isocyanate whereas, in the case of Board AAA, the chips were sprayed firstly with the indicated amount of added water, then with the phenol-formaldehyde resin and finally with the polyisocyanate. In the case of control Board BBB the chips were sprayed with water and then with phenol-formaldehyde resin. The Boards XX
and ZZ showed no significant adhesion to the mold plates after molding whereas serious adhesion problems were encountered in the case of Boards YY, AAA, and BBB. The physical properties of the various boards are also shown in Table 9, from which it will be seen that the properties of Boards XX and ZZ, bo,th within the scope of this invention, are clearly superior to those of Boards YY, AAA and BBB all of which are outside the scope of the invention.
I
1~.23~7 TABLE_9 Boards XX YY ZZ AAA BBB
Materials Wood chips 1920 19201920 1920 1920 Wt. water in chips80 80 80 80 80 Phenol-formaldehyde resin -- 96 96 96 192 Polyisocyanate (same as E~. 1) 96 48 48 48 --Added w~ter 208160 160160 112 2 Emulsifying agent ~.42.4 2.4 -- --
This example illustrates the preparation of particle board in accordance with the invention using a binder composition in which no extraneous emulsiying agent is present and the polyisocyanate was applied neat, i.e.
not in the form of an aqueous emulsion.
A series of samples of wood particle board was prepared using the various components and ~uantities (all parts by weight) shown in Table 5 below and using the procedure described in Example 1 with the exception that the wood particles were first sprayed with the stated amount of water and thereafter were sprayed with a mixture of the polyisocyanate and the phcsphate release agent. The 3Q physical properties determined for each of the finished :~.Z38~
particle boards are also shown in Table 5 and demonstrate the excellent structural strength of the various samples. All of the samples demolded readily and showed no sign of adhering to the steel plates used in their preparation.
~oard_ W X Y Z zZ_ Materials Wood chips 644 644 644 644 644 1~ Wt. water in chips 565S 56 56 56 Polyisocyanate 38.638.6 38.6 38.6 38.6 (same as Ex. 1) Water 56 56 56 56 56 Lauryl pyrophosphate 3.9 3.9 3.9 3.9 3.9 ~same as Ex. 2) * % w/w polyisocyanate 6 6 6 6 6 * % w/w water total 17.4 17.4 17.4 17.4 17.4 * % w/w pyrophosphate 0.6 0.6 0.6 0.6 0.6 Mold time (minutes) 2 2.5 3.0 2 2.5 Board thickness (inches) 3/8 3/8 3/8 1/2 1/2 Physical pro~rties Density pcf ~2 41 42 40 41 Modulus of rupture:
psi 5320 5186 5787 4325 4B10 IModulus of elasti3ity:
psi (x 10 ) 501 510 564 377 365 lDry internal bond: psi 135 133 141 lB3 178 2Wet internal bond: psi 43 42 46 50 4 Footnotes to TABLE 5 * Calculated on dry weight of wood particles I Testscarried out in accordance with ASTM 1037-72 2 Testscarried out in accordancP with German V-100 specifications ~3.~3~:~7 Example 6 This example illustrates the preparation of three particle boards in accordance with the process o~ the invention from "wafer" chips having varying dimensions as large as 2" x 2" x 1/32" and supplied by Weldwood of Canada, Ltd. No extraneous water or emulsifying agent was used and the polyisocyanate and phosphate release agent were applied neat.
A series of samples of particle board from the wafer chips was prepared using the various components and quantities (all parts by weight) shown in Table 6 below and using the procedure described in Example 1 with the exception that the wood wafers were sprayed with a mixture of the polyisocyanate and the phosphate release agent and not with an aqueous emulsion as in Example 1 and that aluminum molding plates were used.
All of the samples demolded readily and showed no sign of adhering to the aluminum plates used in their prepar-ation. The excellent structural strength properties of the resulting particle boards, as evidenced by the high modulus of rupture shown in Table 6, compare very favorably with the low value of this parameter (2500 psi) determined in a board available commercially and prepared from the same type of wafer chips using a phenol-formaldehyde resin binder.
~.2~ 7 Board AA BB CC
Wafer chips 955 955 955 Polyisocyanate 19.1 50 50 Lauryl pyrophosphate (same as Ex. 2) 2.5 6.5 6.5 * % w/w polyisocyanate 2 5.2 5.2 * % w/w total water 4.7 4.7 4.7 * ~ w/w pyrophosphate 0.260.68 0.68 Mold time (mins.) 4.5 4 4.5 Board.thickness ~in.) l/2 l/2 1/2 Density, pcf 46 43 45 Modulus of rupture:psi 7317 7946 10,860 * Calcd. on dry weight of wood wafers Polymethylene polyphenyl polyisocyanate: eq. wt. - 139:
functionality 3Ø Viscosity at 25C = 700 cps: contain-ing circa 35 percent methylenebis(phenyl isocyanate).
Example 7 This example illustrates the preparation of a series of particle boards using polyisocyanate binders in com-bination with various commercially available phosphates in amounts corresponding to approximately 0.7 percent w/w phosphorus in the binder resin combination.
The various samples were prepared using the various components and guantities (all parts by weight) shown in Table 7 and using the procedure described in Example 1 with the exception that no emulsifying agent was employed, and the wat~r was sprayed onto the chips first, followed by the isocyanate mixed with the release agent. A11 of the samples demolded readily and showed no sign of adhering 3~
to the steel plates used in their preparation. In contrast, a control board, prepared in exactly the same manner but omitting the use of a phosphate release agent adhered to the steel plates used in the preparation and could not be demolded without damage to the surface of the board.
~.23~ 7 O O U~ O ~ ~D
~D CO ~ ~1 :~
~ ~r O O ~D O U~ ~ ~ ~r _ _ _ U~
~ r~
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i-l ~
_ _ . _ _ _ _ . _ _ . _ _ . . _ _ _ _ . _ _ _ _ _ C~:>
O O ~D O 1` ~ N ~ N
3: .. _ ._ ____ _ . ... , _ .. _ _ . __ ...... _.. __ . _._ _.. ___ ~O
O~
O O ~ O ~
~) ~
_ O O U~ O 0 ~ r N
~D CO t~ ~1 r~ ~ ~ _l ,1 ~ _ ___ ... _. _ , .... . . .. _.
.
O O ~D O ~i ~9 ~ ~ ~
~1 _~
~ .
O O ~D O CO ~D N ~ ~I
a ~
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U
J~ 'd N S 0 3 Q. ~ U ~ r) ~ Q O E3 9C h U U U U V h O ~ Q ~a ~1 0 h ~1 ~ 0 5 ~ 1~5 . Q O h #
-~ -- 3q-;
~.23~:L~
Footnotes to TABLE 7 -Alkyl acid phosphate derived from lauryl alcohol prereacted with 3 molar proportions of ethylene oxide;
Textilana Division of ~enkel Inc., Hawthorne, CaliEornia.
2 Lauryl acid phosphate; Emery Industries Inc., Mauldin, South Carolina.
3 Alkyl acid phosphate derived from ethoxylated lauryl alcohol; Emery Industries Inc.
Alkyl acid phosphate derived from ethoxylated mid-chain branched aliphatic alcohol; Emery Industries, Inc.
5 Alkyl acid phosphate derived from n-octyl alcohol;
Textilana, ibid.
' 10 6 Alkyl acid phosphate derived from ethoxylated lauryl alcohol; Emery Industries Inc.
7 Prepared as described in Preparation 5.
* Calcd. on dry weight of wood wafers.
Example 8 A further series of particle board samples was prepared using the same phosphate release agents and procedure employed in Example 7 but at iower levels of concentration in the binder resin combination. The various components and the proportions thereof ~all parts by weight) are shown in Table 8 below together with the physical properties determined on certain of the samples. All the samples could be demolded without damage to the board or signi~icant adhesion to the mold plates. The samples prepared using the higher concentrations of phosphate release agent slid out from between the mold plates when demolded whereas some of those prepared using the lower concentrations of phosphate release agent (OO, QQ, and UU) required assistance, e.e. tapping of the mold plates, in order to eff2ct releaseO
All the samples had a thickness of 1/2" in the final board.
æ
0 ~ O O ~ O r~ O ~
~h o ~ ~ ~h ~ rt~ rt tg ~h ~D 3 ~ ~ (D
1~-x P) rr~ rDX P~ x SDX rD x ~ - n ~ It :~ n ~ n ~ n ~n ~ PJ O ~-P~ o 1~- ~ ~ P~
~:~ O ~ ~ ~ ~X ~ ~- ~
3 rD ~ ~ u~ b:
tJ- ~S :q O ~ 1--r~ tD O
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_ _ _ . . .... .. .
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~ I I I ~ I I a~ a~ o o --o ~
oo ~ o o O O ~D
~ ~o : oo co - - -~
I I I I i ~ D
~ l l l ~ l co co ~ o o~ t co o ~ ~
~ I I I I I ~ co al o o~
~ - - --o ~ ~o ~ ~ l l l l l ~ ~ o o ~
- -o l- ~
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o ~ I
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t ~ O ~ ~0 . IJ. 1.. ~ P~ X ~ U~ ~h ~ O
,: 3 o ~ t~ ~ '.. ~
1~ W t a~ ~ o ~o ~ ~7 ~ O
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o . . . . ~2 g ~ .
~ _. _ 5~ 1'- N ~ ~9Cl~ ~Z
~- ~a O ,_ ~ æ
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Z Z ~ ~:
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_ æ æ z z Example 9 This example illustrates the use of a binder re~in combination in accordance with the invention in association with a phenol-formaldehyde resin binder of the prior art.
All of the samples (1/2" thickness) were prepared using the procedure described in Example 1, with the exceptions detailed below, and using the reactants and proportions (all parts by weight) set forth in Table 9. In the case of Boards YY and ZZ the phenol-formaldehyde resin was incorporated in the emulsion of the isocyanate whereas, in the case of Board AAA, the chips were sprayed firstly with the indicated amount of added water, then with the phenol-formaldehyde resin and finally with the polyisocyanate. In the case of control Board BBB the chips were sprayed with water and then with phenol-formaldehyde resin. The Boards XX
and ZZ showed no significant adhesion to the mold plates after molding whereas serious adhesion problems were encountered in the case of Boards YY, AAA, and BBB. The physical properties of the various boards are also shown in Table 9, from which it will be seen that the properties of Boards XX and ZZ, bo,th within the scope of this invention, are clearly superior to those of Boards YY, AAA and BBB all of which are outside the scope of the invention.
I
1~.23~7 TABLE_9 Boards XX YY ZZ AAA BBB
Materials Wood chips 1920 19201920 1920 1920 Wt. water in chips80 80 80 80 80 Phenol-formaldehyde resin -- 96 96 96 192 Polyisocyanate (same as E~. 1) 96 48 48 48 --Added w~ter 208160 160160 112 2 Emulsifying agent ~.42.4 2.4 -- --
10 3 Lauryl pyrophosphate9.~ -~4.8 -- __ * % w/w resin 5 5 5 5 5 * % w/w water 15 15 15 15 15 * ~ w/w phosphate 0.5 --0.25 -- --Platen temp. F350350 350350350 Mold time (minutes)5.S5.5 5.55.5 5.5 Physical Properties Density pcf 41~742.8 44.644.541.4 4 Modulus of Rupture:psi3650 300033203250 2770 20 4 Modulus of elasticity ps 3 310 300 355 319 301 4 Dry internal bond:psi 170 158152 168 100 5 Wet internal bond:psi 78 64 61 50 22 1 PB-65: Borden; aqueous suspension, 50% solids.
2 Aqueous solution: sodium salt of styrene-maleic anhydride copolymer; 30% solids: Monsanto.
3 Prepared as described in Preparation 4.
4 Tests carried out in accordance with ASTM-1037-7~.
5 Test carried out in accordance with German V-100 specifications.
* Calcd. on dry weight of wood particles.
. . .
SUPPLEMENTARY DISCLOSURE
In addition to the phosphate species set out in the original disclosure, certain further phosphate species have now been found to be useful in particle board binders.
Hence binders containing these phosphates and the process of making such binders constitute further embodiments of the invention.
Thus, the present invention provides a process for the preparation of particle board wherein particles of organic material capable of being compacted are contacted with a polyisocyanate composition and the treated particles are subsequently formed into boards by the application of heat and pressure, the improvement comprising contacting said particles, in addition to the treatment with said polyisocyanate composition, with from about 0.1 to about 20 parts, per 100 parts by weight of said polyisocyanate, of a phosphate selected from the class consisting of (a) acid phosphates of the formulae - O O
RO P - OH and (RO)2~ OH
2n OH
~I) (II) and the ammonium, alkali metal and alkaline earth metal salts thereof;
(b) pyrophosphates represented by those derived from the acid phosphates (I) and (II) and mixtures of (I) and (II);
(c) The O-monoacyl derivatives of the acid phosphates (I~ and (II~ havina the formulae O O.
3P RO P OCORl and ~RO)2P OCOR~ ;
OH
(~) (VI) (d) carbamoyl phosphates having the formula , . .
3~ 7 I
R2 NHCO--O p ( OR) OH
(VII) and the ammonium, alkali metal and alkaline earth metal salts of the compounds of formula (VII);
(e) branched polyphosphates of the formulae O O O O O
RO -P - O -~(OR) 2 and (RO~ 2~ - O ~- o - ~(OR)2 1 r (OR)2 (VIII) ¦ (IX);
~ o -~(OR)2 (f) polyphosphates corresponding to the general formula . ~
[ROP - ]n (X~
including the cyclometaphosphates (n = 3); and (g) mixtures of two or more of said compounds;
wherein, in the various formulae shown above, each R
is independently selected from the class consisting of alkyl having from 3 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive, aryl, and R'- (O-CH-lH~
wherein R' is alkyl having from L to 35 carbon atoms, inclusive, and aryl, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an average value from 1 to 25; provided that when one of the Rs in ~ormula (II) is alkyl having from 3 to 35 carbon atoms, inclusive, th~ other R
can be selected from methyl and ethyl; Rl is hyclrocarbyl from 1 to 12 carbon atoms, inclusive; R2 is selected from the class consisting of hydrocarbyl from 1 to 12 carbon atoms and hydrocarbylOsubstituted by at least one additional ~r - NHCOO - P(OR)2 group wAerein R has the signi~icance defined above; and n is an integer.
The invention also comprises novel compositions comprising organic polyisocyanates having incorporated therein one or more of the aforementioned compounds.
The following preparation and examples describe the manner and process of making and using the new phosphate compounds and binder compositions. The preparation and examples are intended only to illustrate the invention ~ithout limiting the scope thereof.
Preparation 6 A series of acid phosphates (mixtures o mono- and di-acid phosphates) was prepared by reaction of the corresponding alcohol with phosphorus pentoxide using the following standard procedure which is illustrated for the preparation of the mixture of the corresponding ~ono- and di-(hexyloxyethyleneoxyethyl)phosphate by reaction of hexyl carbitol (hexyl ether of diethylene glycol) with phosphorus pentoxide.
A total of 9.97 g. (0.07 mole) of phosphorus pentoxide was charged, under nitrogen and in the absence of ~oisture, to 50 g. of freshly distilled methylene chloride. To the resulting I ~fE3 ~ ~ 3698AA
3~7 mixture was added, with rapid stirring, a total of 41.4 g.
(0.218 mole) oE hexyl carbitol at such a rate as to maintain a steady rate of reflux of solvent. When the addition was complete, the solvent was permitted to distil slowly from the reaction mixture while the pot temperature was not permitted to rise above about 80C. The last traces of solvent were removed in vacuo on a rotary film evaporator for 15-30 minutes at 85 - 90C. There was thus obtained a mixture of the mono- and di-(hexyloxyethyleneoxyethyl) acid phosphates.
Using the above procedure but replacin~ the hexyl carbitol there used by an equivalent amount of the ollowing alcohols:-propyloxypropanol butyloxypropanol phenoxypropanvl phenoxyethanol nonylphenoxyethanol butyl carhitol tridecyl~henoxyethyleneoxYethanol[cl3H2 7 ~0 ( CH2)20-(CH2)2 OH]
butyl ether o~ tri(ethylene glycol)~C4HgO(CH2)20(CH2)20(CH2)20H]
tridecyl ether of nona(ethylene glycol)[C~3H2~0(CH2C~20)9H]
methyl ether of dodeca(ethylene glycol)~CH30(CH2CH20)12H]
dodecyl ether of dodeca(ethylene glycol)[C~2H2sO(CH2CH20)l2H]
methyl ether of heptadeca(ethylene glycol)~CH30(CH2CH20)l~H]
phenol mixture of methanol and dodecanol n-propanol n-butanol heptanol and tridecyl alcohol;
~, .. ~
~.Z3~
there were obtained the corresponding mixtures of the mono- and di-acid phosphates.
All the above acid phosphates were employed as release agents in combination with a polyisocyanate binder in the preparation of particle boards in accordance with the invention.
Example 10 A series of samples of wood particle board was prepared using a combination of a polymethylene polyphenyl polyiso-cyanate and an acid phosphate as the binder. The polyisocyanate used in all cases was a polymethylene polyphenyl polyisocyanate containing approximately 48 percent by weight of methylenebis-(phenyl isocyanate) and having an isocyanate equivalent of 134.5 and a viscosity at 25C of 173 cps. A different acid phosphate was used in each instance but all the acid phosphates were mixtures of di-acid phosphates of formula RO-~(OH) 2 and mono-acid phosphates ~RO) 2 (OH) where R had the value shown in Table 10 below, said mixture of acid phosphates having been prepared as described in Preparation 6 above unless otherwise stated.
The method of preparation of the particle board sample in all instances was as follows:-A batch of ~00 a. of ~ouglas fir wood chips W25 sprayedwith 112 g. of the polyisocyanate using the procedure and apparatus described in E~ample 1. When the spraying and tumbling with polyisocyanate was complete, the treated chips were then spraved using the same procedure and apparatus with an amount of the mixture of acid phosphates such that the total amount o~
phosphorus present in the combination of acid phosphate and pol isocyanate ~;as apprcximately 1 percent by weight. The e~act amount of the acid phosphate used in each instance is recorded in T3ble 10 belo~ he mi~ re of acid phos-ha-es W25 dil~_^d - SD'9 -~.23~7 with 40 - 50 g. of Freon Rll (trichlorofluoromethane) or water (diluent indicated in each case in Table lO) to facilitate spraying. An aliquot ~2156 ~.) of the treated chips was then utilized to prepare a particle board having a thickness of 3/8"
using the procedure described in Example l but using cold-rolled steel plates having a dimension of 24" x 36" and a forming frame with inside dimensions of 18.5" x 3~". A sheet of aluminum foil was inserted ~etween each steel plate and the abutting surface of the particle board mat. The platen temperature was 350~F, and the press time was 2.5 minutes at about 500 psi minimum, in all cases. After the particle board, with aluminum sheets in contact therewith, was removed from - the platens of the press, the relative ease with which the aluminum foil separated from the particle board was rated as "excellent" (no resistance to removal), "good" (no resistancb to peeling of foil) or "fair" (some resistance bu~ could be peeled off without tearing or other damage to the foil). It ~as apparent that all the acid phosphates used ga~e significant release properties. The data relating to ~he sam~les is sh~wr in Table 10.
- ~r50 -* Trademark % w/w acid Diluent R in acid ~ w/w P in phosph~te for Ease of phosphate binderl in binderl phosphate release ___ . _ C3H 7 O-C 3H6- 1.18.6 FreonGood C4HgO~C~H6~ 1.08.7 FreonExcellent C6HsO~C3H6~ 1.09.7 FreonFair 2C4HgO~CH2CH2~ 1.012.4 WaterGood nonylphenyl-O-CH2CH2- 914.4 Freon Excellent C4Hg-(OCH2CH2t~r 1.010.2 FreonExcellent C6Hi~OCH2CH2~ 1.011.9 FreonExcellent tridecylphenyl-(OCH2CH2t 20 . 8 16.8 Freon Excellent C4H9-(oc~2cH23-3 1 O12 .1 FreonExcellent *3di(nonyl)phenyl-(OCH2CH~t~0.8 28~9 Freon Excellent * Cl3H27(oCH2CH239 0.825.1 FreonExcellent - 15 4nonylphenyl-(OCH2CH~t~ 0.830.1 FreonExcellent * CH3-(OCH2CH2~ 1.224.3 FreonExcellent * Cl2H2s-(OCH2CH2)12 0.829.4 FreonExcellent * CH3-(OCH2CH2~ 17 1.230.0 I FreonExcellent C,2H25(0C}12CH2-t~ 0~742.2 FreonFair C4Hg- 1.06.2 ~ FreonFair C6H5- 1.5j 10 ' FreonFair Mixture of CH3-and Cl2l~2s0 9 , 7.1, Freon Excellent nonylphenyl 0.6! 7.4 I Freonxcellent Footnotes to TABLE 10:
1: binder = polyisocyanate + acid phosphate 2: As diethylamine salt: Virco Pet 30~ Mobil Corporation 3- Tryfac 5555: Emery Industries 4: Tryfac 5556: Emery Industries *: Each of these acid phosphates in admixture with the isocyanate form~d a good emulsion when shaken with water.
* Trademark .;~. , .
` 369aAA
Example lL
Using the procedure described in Example 10, but replacing the mixture of acid phosphates by bis-2-ethylhexyl-pyrophosphoric acid (Mobil Corporation) and by dibut~lpyrophosphoric acid (~obil Corporation) in amounts representing 12~ by weight based on total weight of pyrophosphoric acid and polyisocyanate there were obtained particle boards with ease of release rated as "excellent" for the former and "fair" for the latter.
Example 12 A further series of wood particle boards was prepared using exactly the same procedure as that described in E~ample 10 wlth the sole exception that the mixture of acid phosphates was blended with the polyisocyanate and the blend was diluted with 40 - 50 g. of Freon Rll before being sprayed on to the wood chips. The polyisocyanate employed throughout the series was the same as that employed in Example 10. A different acid phosphate was used in each instance but all the acid phosphates were mixtures of di-acid phosphates of formula RO-~(OH) 2 and mono-acid phosphates (RO)2~(OH) where R had the value shown in Table 11 below, said mixture of acid phosphates having been prepared as described in Preparation 6 above unless otherwise stated. The ease of release of the particle boards from the aluminum foil were rated on the basis set forth in Example 10.
The results are recorded in Table 11.
~= . . .
3~ 7 TABLE ll % w/w acid R in acid % w/w P inphosphate Ease of phosphate binderlin binderl release *2C12H2s(OCH2CH2t~ 0.6 9.7 Excellent 53Cl2H2s(OCH2CH2~ 3O. 6 10.6 Excellent 4CI2H25(OCH2CH2~s 0.6 13.6 Excellent *5CI3H27(OCH~CH2~6 0.6 14.3 Excellent C3H7 l.0 5.0 Fair C4Hg 1.7 10.0 Excellent lOC7HIs 1.3 lO.0 Excellent CBH~7 0.5 4.6 Excellent 62-ethylhexyl- 1.2 lO Good 7tridecyl 0.8 10 Excellent Footnotes to TABLE 11 . _ _ 5 *: Each of these acid phosphates in admixture with the isocyanate formed an emulsion on shaking with water.
1: binder~= polyisocyanate + acid phosphate 2: Fosterge A25?3: Textilana 3: Tryfac 325A: Emery Industries 4: Tryfac 525A: Emery Industries 5: Tryfac 610~: Emery Industries 6: Mobil Corporation 7: Mobil Corporation As noted in the above Example and in Example 10, a number of the acid phosphates there used possess "self-emulsifying"
properties, i.e. form emulsions when shaken or otherwise agitated with water in the absence of an additional surfactant. This rinding is particularly advantageous where the poiyisocyanate binder containing the acid phosphate release agent is employed in the form of an aqueous emulsion, since, in the case of ~he . 3698AA
~1~.2~B~7 above acid phosphates there is no need to employ an additional emulsifying agent -- the acid phosphate serves both as release agent and emulsifying agent. It has been found that such "self-emulsifying" properties are found in the case of those - 5 acid phosphates of the formula (I) and (II) wherein R represents R'- (O-fH-~H~ wherein R', A and B have the significance A
hereinbefore defined and m has an average value from 3 to 30.
2 Aqueous solution: sodium salt of styrene-maleic anhydride copolymer; 30% solids: Monsanto.
3 Prepared as described in Preparation 4.
4 Tests carried out in accordance with ASTM-1037-7~.
5 Test carried out in accordance with German V-100 specifications.
* Calcd. on dry weight of wood particles.
. . .
SUPPLEMENTARY DISCLOSURE
In addition to the phosphate species set out in the original disclosure, certain further phosphate species have now been found to be useful in particle board binders.
Hence binders containing these phosphates and the process of making such binders constitute further embodiments of the invention.
Thus, the present invention provides a process for the preparation of particle board wherein particles of organic material capable of being compacted are contacted with a polyisocyanate composition and the treated particles are subsequently formed into boards by the application of heat and pressure, the improvement comprising contacting said particles, in addition to the treatment with said polyisocyanate composition, with from about 0.1 to about 20 parts, per 100 parts by weight of said polyisocyanate, of a phosphate selected from the class consisting of (a) acid phosphates of the formulae - O O
RO P - OH and (RO)2~ OH
2n OH
~I) (II) and the ammonium, alkali metal and alkaline earth metal salts thereof;
(b) pyrophosphates represented by those derived from the acid phosphates (I) and (II) and mixtures of (I) and (II);
(c) The O-monoacyl derivatives of the acid phosphates (I~ and (II~ havina the formulae O O.
3P RO P OCORl and ~RO)2P OCOR~ ;
OH
(~) (VI) (d) carbamoyl phosphates having the formula , . .
3~ 7 I
R2 NHCO--O p ( OR) OH
(VII) and the ammonium, alkali metal and alkaline earth metal salts of the compounds of formula (VII);
(e) branched polyphosphates of the formulae O O O O O
RO -P - O -~(OR) 2 and (RO~ 2~ - O ~- o - ~(OR)2 1 r (OR)2 (VIII) ¦ (IX);
~ o -~(OR)2 (f) polyphosphates corresponding to the general formula . ~
[ROP - ]n (X~
including the cyclometaphosphates (n = 3); and (g) mixtures of two or more of said compounds;
wherein, in the various formulae shown above, each R
is independently selected from the class consisting of alkyl having from 3 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive, aryl, and R'- (O-CH-lH~
wherein R' is alkyl having from L to 35 carbon atoms, inclusive, and aryl, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an average value from 1 to 25; provided that when one of the Rs in ~ormula (II) is alkyl having from 3 to 35 carbon atoms, inclusive, th~ other R
can be selected from methyl and ethyl; Rl is hyclrocarbyl from 1 to 12 carbon atoms, inclusive; R2 is selected from the class consisting of hydrocarbyl from 1 to 12 carbon atoms and hydrocarbylOsubstituted by at least one additional ~r - NHCOO - P(OR)2 group wAerein R has the signi~icance defined above; and n is an integer.
The invention also comprises novel compositions comprising organic polyisocyanates having incorporated therein one or more of the aforementioned compounds.
The following preparation and examples describe the manner and process of making and using the new phosphate compounds and binder compositions. The preparation and examples are intended only to illustrate the invention ~ithout limiting the scope thereof.
Preparation 6 A series of acid phosphates (mixtures o mono- and di-acid phosphates) was prepared by reaction of the corresponding alcohol with phosphorus pentoxide using the following standard procedure which is illustrated for the preparation of the mixture of the corresponding ~ono- and di-(hexyloxyethyleneoxyethyl)phosphate by reaction of hexyl carbitol (hexyl ether of diethylene glycol) with phosphorus pentoxide.
A total of 9.97 g. (0.07 mole) of phosphorus pentoxide was charged, under nitrogen and in the absence of ~oisture, to 50 g. of freshly distilled methylene chloride. To the resulting I ~fE3 ~ ~ 3698AA
3~7 mixture was added, with rapid stirring, a total of 41.4 g.
(0.218 mole) oE hexyl carbitol at such a rate as to maintain a steady rate of reflux of solvent. When the addition was complete, the solvent was permitted to distil slowly from the reaction mixture while the pot temperature was not permitted to rise above about 80C. The last traces of solvent were removed in vacuo on a rotary film evaporator for 15-30 minutes at 85 - 90C. There was thus obtained a mixture of the mono- and di-(hexyloxyethyleneoxyethyl) acid phosphates.
Using the above procedure but replacin~ the hexyl carbitol there used by an equivalent amount of the ollowing alcohols:-propyloxypropanol butyloxypropanol phenoxypropanvl phenoxyethanol nonylphenoxyethanol butyl carhitol tridecyl~henoxyethyleneoxYethanol[cl3H2 7 ~0 ( CH2)20-(CH2)2 OH]
butyl ether o~ tri(ethylene glycol)~C4HgO(CH2)20(CH2)20(CH2)20H]
tridecyl ether of nona(ethylene glycol)[C~3H2~0(CH2C~20)9H]
methyl ether of dodeca(ethylene glycol)~CH30(CH2CH20)12H]
dodecyl ether of dodeca(ethylene glycol)[C~2H2sO(CH2CH20)l2H]
methyl ether of heptadeca(ethylene glycol)~CH30(CH2CH20)l~H]
phenol mixture of methanol and dodecanol n-propanol n-butanol heptanol and tridecyl alcohol;
~, .. ~
~.Z3~
there were obtained the corresponding mixtures of the mono- and di-acid phosphates.
All the above acid phosphates were employed as release agents in combination with a polyisocyanate binder in the preparation of particle boards in accordance with the invention.
Example 10 A series of samples of wood particle board was prepared using a combination of a polymethylene polyphenyl polyiso-cyanate and an acid phosphate as the binder. The polyisocyanate used in all cases was a polymethylene polyphenyl polyisocyanate containing approximately 48 percent by weight of methylenebis-(phenyl isocyanate) and having an isocyanate equivalent of 134.5 and a viscosity at 25C of 173 cps. A different acid phosphate was used in each instance but all the acid phosphates were mixtures of di-acid phosphates of formula RO-~(OH) 2 and mono-acid phosphates ~RO) 2 (OH) where R had the value shown in Table 10 below, said mixture of acid phosphates having been prepared as described in Preparation 6 above unless otherwise stated.
The method of preparation of the particle board sample in all instances was as follows:-A batch of ~00 a. of ~ouglas fir wood chips W25 sprayedwith 112 g. of the polyisocyanate using the procedure and apparatus described in E~ample 1. When the spraying and tumbling with polyisocyanate was complete, the treated chips were then spraved using the same procedure and apparatus with an amount of the mixture of acid phosphates such that the total amount o~
phosphorus present in the combination of acid phosphate and pol isocyanate ~;as apprcximately 1 percent by weight. The e~act amount of the acid phosphate used in each instance is recorded in T3ble 10 belo~ he mi~ re of acid phos-ha-es W25 dil~_^d - SD'9 -~.23~7 with 40 - 50 g. of Freon Rll (trichlorofluoromethane) or water (diluent indicated in each case in Table lO) to facilitate spraying. An aliquot ~2156 ~.) of the treated chips was then utilized to prepare a particle board having a thickness of 3/8"
using the procedure described in Example l but using cold-rolled steel plates having a dimension of 24" x 36" and a forming frame with inside dimensions of 18.5" x 3~". A sheet of aluminum foil was inserted ~etween each steel plate and the abutting surface of the particle board mat. The platen temperature was 350~F, and the press time was 2.5 minutes at about 500 psi minimum, in all cases. After the particle board, with aluminum sheets in contact therewith, was removed from - the platens of the press, the relative ease with which the aluminum foil separated from the particle board was rated as "excellent" (no resistance to removal), "good" (no resistancb to peeling of foil) or "fair" (some resistance bu~ could be peeled off without tearing or other damage to the foil). It ~as apparent that all the acid phosphates used ga~e significant release properties. The data relating to ~he sam~les is sh~wr in Table 10.
- ~r50 -* Trademark % w/w acid Diluent R in acid ~ w/w P in phosph~te for Ease of phosphate binderl in binderl phosphate release ___ . _ C3H 7 O-C 3H6- 1.18.6 FreonGood C4HgO~C~H6~ 1.08.7 FreonExcellent C6HsO~C3H6~ 1.09.7 FreonFair 2C4HgO~CH2CH2~ 1.012.4 WaterGood nonylphenyl-O-CH2CH2- 914.4 Freon Excellent C4Hg-(OCH2CH2t~r 1.010.2 FreonExcellent C6Hi~OCH2CH2~ 1.011.9 FreonExcellent tridecylphenyl-(OCH2CH2t 20 . 8 16.8 Freon Excellent C4H9-(oc~2cH23-3 1 O12 .1 FreonExcellent *3di(nonyl)phenyl-(OCH2CH~t~0.8 28~9 Freon Excellent * Cl3H27(oCH2CH239 0.825.1 FreonExcellent - 15 4nonylphenyl-(OCH2CH~t~ 0.830.1 FreonExcellent * CH3-(OCH2CH2~ 1.224.3 FreonExcellent * Cl2H2s-(OCH2CH2)12 0.829.4 FreonExcellent * CH3-(OCH2CH2~ 17 1.230.0 I FreonExcellent C,2H25(0C}12CH2-t~ 0~742.2 FreonFair C4Hg- 1.06.2 ~ FreonFair C6H5- 1.5j 10 ' FreonFair Mixture of CH3-and Cl2l~2s0 9 , 7.1, Freon Excellent nonylphenyl 0.6! 7.4 I Freonxcellent Footnotes to TABLE 10:
1: binder = polyisocyanate + acid phosphate 2: As diethylamine salt: Virco Pet 30~ Mobil Corporation 3- Tryfac 5555: Emery Industries 4: Tryfac 5556: Emery Industries *: Each of these acid phosphates in admixture with the isocyanate form~d a good emulsion when shaken with water.
* Trademark .;~. , .
` 369aAA
Example lL
Using the procedure described in Example 10, but replacing the mixture of acid phosphates by bis-2-ethylhexyl-pyrophosphoric acid (Mobil Corporation) and by dibut~lpyrophosphoric acid (~obil Corporation) in amounts representing 12~ by weight based on total weight of pyrophosphoric acid and polyisocyanate there were obtained particle boards with ease of release rated as "excellent" for the former and "fair" for the latter.
Example 12 A further series of wood particle boards was prepared using exactly the same procedure as that described in E~ample 10 wlth the sole exception that the mixture of acid phosphates was blended with the polyisocyanate and the blend was diluted with 40 - 50 g. of Freon Rll before being sprayed on to the wood chips. The polyisocyanate employed throughout the series was the same as that employed in Example 10. A different acid phosphate was used in each instance but all the acid phosphates were mixtures of di-acid phosphates of formula RO-~(OH) 2 and mono-acid phosphates (RO)2~(OH) where R had the value shown in Table 11 below, said mixture of acid phosphates having been prepared as described in Preparation 6 above unless otherwise stated. The ease of release of the particle boards from the aluminum foil were rated on the basis set forth in Example 10.
The results are recorded in Table 11.
~= . . .
3~ 7 TABLE ll % w/w acid R in acid % w/w P inphosphate Ease of phosphate binderlin binderl release *2C12H2s(OCH2CH2t~ 0.6 9.7 Excellent 53Cl2H2s(OCH2CH2~ 3O. 6 10.6 Excellent 4CI2H25(OCH2CH2~s 0.6 13.6 Excellent *5CI3H27(OCH~CH2~6 0.6 14.3 Excellent C3H7 l.0 5.0 Fair C4Hg 1.7 10.0 Excellent lOC7HIs 1.3 lO.0 Excellent CBH~7 0.5 4.6 Excellent 62-ethylhexyl- 1.2 lO Good 7tridecyl 0.8 10 Excellent Footnotes to TABLE 11 . _ _ 5 *: Each of these acid phosphates in admixture with the isocyanate formed an emulsion on shaking with water.
1: binder~= polyisocyanate + acid phosphate 2: Fosterge A25?3: Textilana 3: Tryfac 325A: Emery Industries 4: Tryfac 525A: Emery Industries 5: Tryfac 610~: Emery Industries 6: Mobil Corporation 7: Mobil Corporation As noted in the above Example and in Example 10, a number of the acid phosphates there used possess "self-emulsifying"
properties, i.e. form emulsions when shaken or otherwise agitated with water in the absence of an additional surfactant. This rinding is particularly advantageous where the poiyisocyanate binder containing the acid phosphate release agent is employed in the form of an aqueous emulsion, since, in the case of ~he . 3698AA
~1~.2~B~7 above acid phosphates there is no need to employ an additional emulsifying agent -- the acid phosphate serves both as release agent and emulsifying agent. It has been found that such "self-emulsifying" properties are found in the case of those - 5 acid phosphates of the formula (I) and (II) wherein R represents R'- (O-fH-~H~ wherein R', A and B have the significance A
hereinbefore defined and m has an average value from 3 to 30.
Claims
(b) pyrophosphates represented by those derived from the acid phosphates (I) and (II) and mixtures of (I) and (II);
(c) The O-monoacyl derivatives of the acid phosphates (I) and (II) having the formulae and ;
(V) (VI) (d) carbamoyl phosphates having the formula (VII) and the ammonium, alkali metal and alkaline earth metal salts of the compounds of formula (VII);
(e) branched polyphosphates of the formulae and (VIII) (IX);
(f) polyphosphates corresponding to the general formula (X) including the cyclometaphosphates (n = 3); and (g) mixtures of two or more of said compounds;
wherein, in the various formulae shown above, each R
is independently selected from the class consisting of alkyl having from 8 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive and wherein R' is alkyl having from 8 to 35 carbon atoms, inclusive, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an average value from to 5; R1 is hydrocarbyl from 1 to 12 carbon atoms, inclusive;
R2 is selected from the class consisting of hydrocarbyl from 1 to 12 carbon atoms and hydrocarbyl substituted by at least one additional group wherein R has the significance defined above; and n is an integer.
The process of Claim 1 wherein said polyisocyanate is a polymethylene polyphenyl polyisocyanate containing from about 25 to about 90 percent by weight of methylene-bis(phenyl isocyanate), the remainder of said mixture being oligomeric polymethylene polyphenyl polyisocyanates of functionality greater than 2.
The process of Claim 2 wherein the polymethylene polyphenyl polyisocyanate contains from about 35 to about 65 percent by weight of methylenebis(phenyl isocyanate).
The process of Claim 1 wherein said phosphate is a mixture of lauryl diacid phosphate and dilauryl monoacid phosphate.
The process of Claim 1 wherein said phosphate is a pyrophosphate derived by removal of water of condensation from a mixture of lauryl,diacid phosphate and dilauryl monoacid phosphate.
The process of Claim 1 wherein said phosphate is a mixture of oleyl diacid phosphate and dioleyl monoacid phosphate.
The process of Claim 1 wherein said phosphate is a pyrophosphate derived by removal of water of condensation from a mixture of oleyl diacid phosphate and dioleyl monoacid phosphate.
The process of Claim 1 wherein the particles employed in the preparation of said particle board are wood chips.
The process of Claim 1 wherein said polyisocyanate and said phosphate are applied simultaneously to said particles in the form of an aqueous emulsion.
The process of Claim 9 wherein said aqueous emulsion of polyisocyanate also comprises an emulsifying agent.
The process of Claim 1 wherein said particles are contacted separately with said polyisocyanate and said phosphate.
The process of Claim 11 wherein said polyisocyanate and said phosphate are each employed in the form of an aqueous dispersion.
The process of Claim 11 wherein said particles are contacted with water prior to being contacted with said polyisocyanate and said phosphate.
A storage stable composition comprising a mixture of (a) a polymethylene polyphenyl polyisocyanate containing from about 25 to about 90 percent by weight of methylenebis(phenyl isocyanate) the remainder of said mixture being oligomeric polymethylene polyphenyl polyisocyanates having a functionality higher than 2.0; and (b) from about 0.1 parts by weight to about 20 parts by weight, per 100 parts by weight of said polyisocyanate, of a pyrophosphate derived by removal of water of condensation from at least one acid phosphate selected from acid phosphates of the formulae:
and wherein each R is independently selected from the class consisting of alkyl having from 8 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive and wherein R' is alkyl having from 8 to 35 carbon atoms, inclusive, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an average value from 1 to 5, and mixtures of two or more of said acid phosphates.
A composition according to Claim 14 wherein the pyrophosphate is derived from a mixture of lauryl diacid phosphate and dilauryl monoacid phosphate.
A composition according to Claim 14 wherein the pyrophosphate is derived from a mixture of oleyl diacid phosphate and di monoacid phosphate.
A composition according to Claim 14 which also comprises an emulsifying agent.
Page 50 of 50 Pages CLAIMS SUPPORTED BY SUPPLEMENTARY DISCLOSURE
In a process for the preparation of particle board wherein particles of organic material capable of being compacted are contacted with a polyisocyanate composition and the treated particles are subsequently formed into boards by the application of heat and pressure, the improvement which comprises contacting said particles, in addition to the treatment with said polyisocyanate composition, with from about 0.1 to about 20 parts, per 100 parts by weight of said polyisocyanate, of a phosphate selected from the class consisting of (a) acid phosphates of the formulae and (I) (II) and the ammonium, alkali metal and alkaline earth metal salts thereof;
(b) pyrophosphates represented by those derived from the acid phosphates (I) and (II) and mixtures of (I) and (II);
(c) The O-monoacyl derivatives of the acid phosphates (I) and (II) having the formulae and ;
(V) (VI) (d) carbamoyl phosphates having the formula (VII) and the ammonium, alkali metal and alkaline earth metal salts of the compounds of formula (VII);
(e) branched polyphosphates of the formulae and (VIII) (IX);
(f) polyphosphates corresponding to the general formula (X) including the cyclometaphosphates (n = 3); and (g) mixtures of two or more of said compounds;
wherein, in the various formulae shown above, each R
is independently selected from the class consisting of alkyl having from 3 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive, aryl , and wherein R' is alkyl having from 1 to 35 carbon atoms, inclusive, and aryl, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an average value from 1 to 25; provided that when one of the Rs in formula (II) is alkyl having from 3 to 35 carbon atoms, inclusive, the other R can be selected from methyl and ethyl;
R1 is hydrocarbyl from 1 to 12 carbon atoms, inclusive;
R2 is selected from the class consisting of hydrocarbyl from 1 to 12 carbon atoms and hydrocarbyl substituted by at least one additional group wherein R has the significance defined above; and n is an integer.
The process of Claim 18 wherein said polyisocyanate is a polymethylene polyphenyl polyisocyanate containing from about 25 to about 90 percent by weight of methylene-bis(phenyl isocyanate), the remainder of said mixture being oligomeric polymethylene polyphenyl polyisocyanates of functionality greater than 2.
The process of Claim 19 wherein the polymethylene polyphenyl polyisocyanate contains from about 35 to about 65 percent by weight of methylenebis(phenyl isocyanate).
The process of Claim 18 wherein the particles employed in the preparation of said particle board are wood chips.
The process of Claim 18 wherein said polyisocyanate and said phosphate are applied simultaneously to said particles in the form of an aqueous emulsion.
The process of Claim 22 wherein said aqueous emulsion of polyisocyanate also comprises an emulsifying agent.
The process of Claim 18 wherein said particles are contacted separately with said polyisocyanate and said phosphate.
The process of Claim 24 wherein said polyisocyanate and said phosphate are each employed in the form of an aqueous dispersion.
The process of Claim 24 wherein said particles are contacted with water prior to being contacted with said polyisocyanate and said phosphate.
A storage stable composition comprising a mixture of (a) a polymethylene polyphenyl polyisocyanate containing from about 25 to about 90 percent by weight of methylenebis(phenyl isocyanate) the remainder of said mixture being oligomeric polymethylene polyphenyl polyisocyanates having a functionality higher than 2.0; and (b) from about 0.1 parts by weight to about 20 parts by weight, per 100 parts by weight of said polyisocyanate, of a pyrophosphate derived by removal of water of condensation from at least one acid phosphate selected from acid phosphates of the formulae:
and (I) (II) wherein each R is independently selected from the class consisting of alkyl having from 3 to 35 carbon atoms, inclusive, alkenyl having from 8 to 35 carbon atoms, inclusive, aryl, and wherein R' is alkyl having from 1 to 35 carbon atoms, inclusive, and aryl, one of A and B represents hydrogen and the other is selected from the class consisting of hydrogen and methyl, and n is a number having an average value from
1 to 25; provided that when one of the Rs in formula (II) is alkyl having from 3 to 35 carbon atoms, inclusive, the other R can be selected from methyl and ethyl; and mixtures of two or more or said acid phosphates.
A composition according to Claim 27 which also comprises an emulsifying agent.
A composition according to Claim 27 which also comprises an emulsifying agent.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US94720978A | 1978-09-29 | 1978-09-29 | |
| US947,209 | 1978-09-29 | ||
| US3564779A | 1979-05-03 | 1979-05-03 | |
| US35,647 | 1979-05-03 | ||
| US06/134,315 US4257995A (en) | 1979-05-03 | 1980-03-26 | Process for preparing particle board and polyisocyanate-phosphorus compound release agent composition therefor |
| US134,315 | 1980-03-26 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1123817A true CA1123817A (en) | 1982-05-18 |
Family
ID=27364880
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA335,406A Expired CA1123817A (en) | 1978-09-29 | 1979-09-11 | Polymeric isocyanate binder with internal release agent |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1123817A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10787593B2 (en) | 2015-05-15 | 2020-09-29 | Wanhua Chemical Group Co., Ltd. | Emulsifiable isocyanate composition and preparation method and use thereof |
-
1979
- 1979-09-11 CA CA335,406A patent/CA1123817A/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10787593B2 (en) | 2015-05-15 | 2020-09-29 | Wanhua Chemical Group Co., Ltd. | Emulsifiable isocyanate composition and preparation method and use thereof |
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| MKEX | Expiry |