Production of foamed polymer structures

Abstract: Described are ways of improving the yields of specification grade polyimide foam on a consistent basis from one run to the next, by use of improved microwave-­ based foaming processes. In one such process, during the application of the microwave radiation, the body of polyimide precursor and of the foam structure as it is developing therefrom are maintained under a substantially vapor-impermeable microwave-compatible shroud that does not substantially restrict or impede development of the foam structure; and the microwave radiation is directed upon the top, sides and ends of the body of polyimide precursor and of the foam structure as it is developing, but the extent to which such radiation impinges upwardly into the bottom of said body and said foam structure is curtailed, preferably by means of a metallic shield located below the precursor and developing foam struc­ ture. Mechanisms by which the shields and shrouds function to provide the improvements of the process are discussed, and methods based thereon are set forth.

Description: This invention relates to the production of cellular polymeric structures, and more particularly to improvements in the manufacture of polyimide foams. Over the years, considerable effort has been devoted to the development of technology for producing polyimide foams. Such materials are generally produced by forming a polyimide precursor, usually an essentially equimolar mixture of a lower alkyl ester of a tetracarboxylic acid and one or more primary diamines, and subjecting a bed or body of this polyimide precursor mixture to a temperature sufficient to cause the development of a foamed polymer structure through the generation and evolution of gaseous material within the body of the precursor. See for example U. S. Pat. Nos. 4,153,783, 4,296,208, 4,305,796, 4,439,381 and Re.30,213. Although the foaming operation may be performed in thermal ovens or by use of dielectric heating, to date use of microwaving as described in U. S. Pat. Nos. 4,305,796 and 4,439,381 has proven most successful. Despite the intensity and magnitude of the efforts to improve upon the technology of polyimide foam production, a number of difficulties have defied solution. Chief among these has been the inability to achieve consistently high yields of usable foam from the polyimide precursor. As formed, the polyimide leaves the oven in the form of a "bun" which has a crust over its outer surface which must be cut away in order to expose the interior cellular mass of cured polyimide foam. Unfortunately, blow holes, striations and other physical defects are often encountered in the buns, which means that the defective zones within the bun must be trimmed away and discarded, often with a considerable loss of raw materials and plant throughput. Complicating the problem has been the erratic nature of these events -- only after the bun had been made and trimmed can it be determined whether the production run has been successful or not. Moreover, successive runs conducted under apparently the same conditions may give rise to vastly different results. In one case the yield of specification grade foam may be reasonably good, yet in the very next run it may be unacceptably low. The document US-A 4,439,381 discloses a method for producing polyimide foams wherein the polyimide precursor is foamed alternatively in an open or a closed mold. The mold material is described to have sufficient flexible strength to withstand the pressure of the expanding foam. It is clear from reading said description that there is no concept of having a substantially vapor-impermeable microwave-compatible shroud that does not substantially restrict or impede development of the foam and, in addition, that prevents the surface of the foam from drying as it would if left exposed to the microwave radiation. The document US-A 4,305,796 is directed to a process for preparing polyimides by exposing a precursor to microwave radiation for a sufficient period of time to develop a cellular physical structure. The precursor is spread over a glass cloth which is placed on a sheet of aluminum foil. However, the assembly is first dried in a microwave oven in order to remove the solvent. The aluminum foil is then removed, and the sample is placed between two sheets of Teflon-coated glass. At that point, the dried panel is further processed by foaming and curing, whereby the foaming is carried out in a microwave oven without the aluminum foil. A most worthwhile contribution to the art would thus be the discovery of a way of improving the yields of specification grade polyimide foam on a consistent basis from one run to the next. This invention is believed to fulfill this need. Provided by this invention are improvements in microwave-based foaming processes carried out in a microwave cavity wherein a polyimide precursor is exposed to microwave radiation of intensity sufficient to cause the development of a foamed polymer through the generation and evolution of gaseous material within the precursor as it foams. In accordance with one embodiment of this invention during the application of the microwave radiation, the body of polyimide precursor and of the foam structure as it is developing therefrom are maintained under a substantially vapor-impermeable microwave-compatible shroud that does not substantially restrict or impede development of the foam structure and prevents the surface of the foam from drying out as it would if left exposed; and the microwave radiation is directed upon the top, sides and ends of the body of polyimide precursor and of the foam structure as it is developing therefrom, but the extent to which such radiation impinges upwardly into the bottom of said body and said foam structure as it is developing therefrom is curtailed by maintaining a microwave radiation-curtailing shield between said precursor and foam and a source of microwave radiation therebelow. One way of accomplishing this radiation curtailment is to design the microwave cavity so that the radiation is not directed upwardly into the precursor or developing foam. However the method of the invention for accomplishing this curtailment consists of maintaining a microwave radiation-curtailing shield between the precursor body and a source of microwave radiation therebelow. Not only does this avoid the difficulty and expense of redesigning and producing specially made microwave cavities, but it enables certain other operational advantages (described below) to be achieved when employing and properly positioning certain types of shields in the microwave cavity. While various microwave-blocking materials may be used, the shield is preferably a metallic shield, and most preferably a shield composed of a metal or metallic alloy having a heat capacity similar to that of aluminum. In addition, the metal preferably does not conduct heat substantially more rapidly than aluminum. Suitable metals include aluminum, aluminum-silicon alloys, ferroalloys, copper, titanium, stainless steel, gold, silver, whereby a shield composed primarily or exclusively of aluminum is preferred. When using a metal shield it is particularly desirable to maintain the shield at a suitable temperature in the range of 50 to 300°C and at least the bottom portion of the precursor should be maintained at a suitable temperature in the range of 50 to 200°C before the time of foaming. Aluminum is particularly well suited for use as a shield since its heat capacity and thermal conductivity enable it to be preheated to the desired temperature within this range and be positioned in close proximity to the bottom of the bed, and thus suitably control the temperature of the precursor before and during the actual generation of the foamed mass. Another advantage of employing a metal shield composed of aluminum or having thermal properties comparable to aluminum is that upon the completion of one microwaving operation, the foamed mass can be removed from the microwave cavity for thermal curing in a thermal oven, and another batch of precursor promptly put in place for the next run. The metal shield will retain enough heat from the prior run to heat up the lower portion of the incoming precursor to a temperature in or close to the desired temperature range by the time the application of the microwave radiation is begun. Thus the metallic shield conserves thermal energy for effective use in the process and in so doing, enables plant throughput to be increased. The polyimide precursor, when in the form of a powder, is preferably placed on a heat stable cloth which in turn is positioned on or a suitable distance above the metallic shield. Among the materials from which such cloths may be fabricated are glass coated with a Teflon resin or other high temperature resin, glass cloth, ceramic cloth, fiberglass cloth, quartz cloth. In accordance with, and as an outgrowth of, the use of a shield, another embodiment of this invention provides a method of producing a foamed polymer structure which comprises: (i) raising the temperature of at least the lower portion of a body of polyimide precursor to a suitable temperature in the range of 50 to 200°C, (preferably in the range of 60 to 130°C); (ii) while at least said lower portion is at said temperature, commencing the exposure of the body of polyimide precursor to microwave radiation, in particular radiation of intensity sufficient to cause the development of a foamed polymer structure by generation and evolution of gaseous material within the body of the precursor; and (iii) maintaining the body of polyimide precursor and of the foam structure as it is developing therefrom under a substantially vapor-impermeable microwave-compatible shroud that does not substantially restrict or impede development of the foam structure. The operation of (i) hereof may be effected simply by use of a metallic or other shield having a suitably high heat capacity, heated from a prior run, as the source of heat for heating up the precursor to the desired temperature. Alternatively, contact or radiant heaters may be positioned in the microwave cavity below the bed of precursor and above the microwave shield (if used) so that the temperature of the precursor or at least the lower portion thereof can be elevated to the desired temperature just prior to initiating the flow of microwave radiation into the precursor. Other ways of preheating the precursor prior to the onset of the microwave radiation may also be used. In the various embodiments of this invention described above, before and during the time the body of polyimide precursor is exposed to microwave radiation, outer surfaces of the body of polyimide precursor and of the foam structure as it is developing therefrom are kept under a substantially vapor-impermeable microwave-compatible shroud that does not substantially restrict or impede development of the foam structure. For this purpose use may be made of a shroud composed of a polymer film, such as polyvinyl chloride (PVC), polyvinylidene chloride, polyethylene, polypropylene, nylon, polyethylene terephthalate, PVC being preferred. The suitability of any given polymer film can readily be determined by simply running a few preliminary small scale foaming experiments using various candidate films to see which ones result in the formation of desirable foam structures during the microwaving step. In practice suitably-sized sheets or strips of the film are placed over the top and around the sides and ends of the body of polyimide precursor before the microwave radiation is applied. The film should not be applied so that it excessively constricts the expansion of the developing film structure. Films having stretch characteristics are useful in this regard, provided of course that they are made of materials that can withstand the temperatures that are developed in the microwaving operation. Several beneficial mechanisms are believed to occur because of the use of a shroud. In the first place, polyimide precursors, especially when in powder form, are very hygroscopic. Thus the film is believed to prevent the precursor from picking up too much moisture from the atmosphere before the microwave radiation is applied. Secondly, when a body of polyimide precursor is exposed to the microwave radiation, the development of a foamed polymer structure is caused by the generation and evolution of gaseous material within the body of the precursor. This gaseous material initially is predominantly vaporous alcohol (e.g., methanol or ethanol) being liberated from the ester component in the precursor, along with some water vapor which is also liberated in the reactions taking place within the precursor mixture. In the absence of the vapor-impermeable microwave-compatible shroud this gaseous material leaves the surface of the developing foam and allows the surface to dry out and become hard and crusty, which in turn impedes proper development of additional foam within the interior of the bun, and provides areas for excessive heat build up with consequent adverse effects on foam quality. Careful observation of the surface of buns developing when encased by a shroud pursuant to this invention indicates that the surface does not dry out as it would if left exposed, and in fact in some cases the surface appears to have become wet with condensed vapor from the alcohol and/or water enriched atmosphere which the shroud maintains around the developing foam. It will be understood and appreciated, of course that this invention is not to be limited by any particular theory or to any particular mechanism of operation. The foregoing explanation conforms to the observations made to date and is believed to be a rational explanation of why the shroud performs so successfully. However this invention is not intended to be, nor should it be, limited by theoretical considerations -- the invention works, and it works well, irrespective of exactly how it works. Another way of adapting the concept of the shroud to the microwaving operation is to maintain a suitable quantity of the precursor, whether in powder or liquid form, encased in a sealed bag or pouch of vapor-impermeable, microwave-compatible material, such as a plastics bag or pouch, from around the time it is formed and to use the bag or pouch of precursor in the microwaving step. In this way all of the foregoing benefits of the shroud are achieved and additionally, handling, storage and transport of the precursor are facilitated. In accordance with, and as an outgrowth of, the use of a shroud, another embodiment of this invention provides a method of producing a foamed polymer structure which comprises: (i) raising the temperature of at least the lower portion of a body of polyimide precursor to a suitable temperature in the range of 50 to 200°C, (preferably in the range of 60 to 130°C); (ii) while at least said lower portion is at said temperature, commencing the exposure of the body of polyimide precursor to microwave radiation of intensity sufficient to cause the development of a foamed polymer structure by generation and evolution of gaseous material within the body of the precursor, and (iii) concurrently maintaining the precursor and the foam structure developing therefrom under an atmosphere enriched in vapors of a lower alcohol. The operation of (i) hereof may be effected simply by use of a metallic or other shield having a suitably high heat capacity, heated from a prior run, as the source of heat for heating up the precursor to the desired temperature. Alternatively, contact or radiant heaters may be positioned in the microwave cavity below the bed of precursor and above the microwave shield (if used) so that the temperature of the precursor or at least the lower portion thereof can be elevated to the desired temperature just prior to initiating the flow of microwave radiation into the precursor. Other ways of preheating the precursor prior to the onset of the microwave radiation may also be used. The operation of (iii) hereof may be effected simply by use of the shroud in the manner described hereinabove. Alternatively, the foaming step may be conducted in an enclosed chamber through which an atmosphere enriched in vaporous lower alcohol (e.g., a C₁-C₄ alcohol) is circulated so that the developing foam structure is itself encased in this enriched vaporous atmosphere. Use of a very fine spray or mist of alcohol in a suitably-designed microwave chamber is also possible. Preferred precursors for use in the embodiments of the immediately preceding paragraph are comprised of a lower alkyl ester of an aromatic tetracarboxylic acid and at least one aromatic or heterocyclic primary diamine. It is also preferable to employ in those embodiments a precursor that is initially in powder form. The polyimide precursors used in the practice of this invention can vary widely in composition. In general, they are composed of a mixture comprising at least (i) one or more organic tetracarboxylic acids or derivatives thereof, and (ii) one or more organic diamines co-reactive therewith, preferably an aromatic or heterocyclic or primary diamine. Components (i) and (ii) are usually present in the mixture in essentially stoichiometric quantities. The organic tetracarboxylic acids or derivatives thereof are preferably based on aromatic tetracarboxylic acids having the general formula: wherein A is a tetravalent organic group. The tetravalent organic group A is preferably one having one of the following structures: wherein X is one or more of the following: -O-; -S; -SO₂-; -CH₂-; -CH₂CH₂-; Preferred among the tetracarboxylic acid esters are the alkyl esters of 3,3',4,4'-benzophenone tetracarboxylic acid, most preferably the lower alkyl diesters thereof. Mixtures of two or more aromatic esters, most preferably predominating in diesters, may be employed, if desired. It is also possible, in accordance with this invention, that the tetracarboxylic acid derivative employed in the manufacture of the polyimide foams be a caprolactam as taught by U. S. 4,161,477, 4,183,838 and 4,183,839. As described in those patents, bis-imide is formed by reaction of a tetracarboxylic acid dianhydride with an oxoimine such as caprolactam and then reacted with the diamine or diamines to produce the desired polyimides. The caprolaotam is displaced during the reaction, in much the same way as is the ester portion of the tetracarboxylic acid ester. The tetracarboxylic acid derivative used in the manufacture of the polyimide foams pursuant to this invention may also be an N-substituted imido acid ester of the tetracarboxylic acid as taught by U. S. 4,647,597 and 4,656,198. As described in those patents, the N-substituted imido acid ester may be formed by reacting an aromatic tetracarboxylic acid dianhydride with an amino acid and an alcohol or mixture of alcohols. As further taught in those patents, on reaction of the imido acid ester with the diamine or diamines, the acid ester group bonded to the nitrogen atom of the N-substituted imido acid ester is displaced so that the desired polyimide is formed. The organic diamines with which the foregoing mixture of tetracarboxylic acids or derivatives is employed may be represented by the formula: H₂N-R'-NH₂ wherein R' is an aromatic group containing 5 to 16 carbon atoms and containing up to one hetero atom in the ring, the hetero atom being nitrogen, oxygen or sulfur. Also included are aromatic groups such as: Representatives of such diamines include: 2,6-diaminopyridine; 3,5-diaminopyridine; 3,3'-diaminodiphenylsulfone; 4,4'-diaminodiphenylsulfone; 4,4'-diaminodiphenylsulfide; 3,3'-diaminodiphenylether; 4,4'-diaminodiphenylether; meta-phenylenediamine; para-phenylenediamine; 4,4'-methylene dianiline; 2,6-diamino toluene; and 2,4-diamino toluene; It is also possible and sometimes desirable in the preparation of the polyimide precursors of this invention, to include in the reaction mixture one or more aliphatic diamines. Such aliphatic diamines are preferably alpha-omega diaminoalkanes having the formula: H₂N-(CH₂) n -NH₂ (I) wherein n is an integer from 2 to 16. Representatives of such diamines include 1,3-diaminopropane, 1,4-diaminobutane, 1,5-di-aminopentane, or 1,6-diaminohexane. In place of or in addition to the foregoing aliphatic amines, use can be made of aliphatic etherified polyamines of the type polyoxypropylene amines having the formula: H₂N-CH(CH₃)CH₂-[OCH₂CH(CH₃)] x -NH₂ (II) wherein x varies from 1 to 5 carbon atoms. Other useful primary diamines which may be included in the products of this invention include amino-terminated butadienenitrile copolymers having the general formula: wherein R is either a phenylene group or an alkylene group, R₁ is hydrogen or methyl, and x and y or each independently integers ranging from 1 to 25 and n is an integer, preferably below 20. In these copolymers it is preferred that butadiene constitute at least 50% by weight of the butadiene and nitrile monomer. The nitrile monomer copolymerized with the butadiene can either be acrylonitrile or methacrylonitrile. Such copolymers generally have low molecular weights, preferably less than 3,000, to insure that they are sufficiently fluid to react in the formation of the polyimide as well as sufficiently fluid so as to be capable of foaming. Still another type of primary diamines which may be included in the products of this invention is the aromatic amino-terminated silicones, such as those having the general formula: wherein R is a C₂ to C₆ alkylene group, R₁ and R₂ are each independently lower alkyl containing 1 to 3 carbon atoms and n is an integer from 1 to 4. Another preferred category of diamines which may be utilized in forming the foams of this invention are the diesters of an amino-substituted aromatic carboxylic acid and a polymethylene glycol. Such diesters may be represented by the general formula: H₂N-ArCOO-R-OOCAr-NH₂ (V) wherein R is an alkylene group (which may be branched or straight chain) and which preferably contains from 3 to 8 carbon atoms, most preferably trimethylene; and Ar is an aromatic group which may be composed of one or more fused or non-fused benzene rings which in turn may carry suitable substituents (e.g., nitro or alkoxy) in addition to the primary amino groups. A few exemplary diesters of this type include: ethylene glycol-4-aminobenzoic acid diester; ethylene glycol-3-aminobenzoic acid diester; ethylene glycol-2-aminobenzoic acid diester; trimethylene glycol-3-aminobenzoic acid diester; trimethylene glycol-2-aminobenzoic acid diester; trimethylene glycol-3-amino-2-nitrobenzoic acid diester; tetramethylene glycol-3-amino-4-nitrobenzoic acid diester; tetramethylene glycol-3-amino-5-nitrobenzoic acid diester; tetramethylene glycol-4-amino-2-nitrobenzoic acid diester; 1,5-pentanediol-4-amino-3-nitrobenzoic acid diester; 1,6-hexanediol-5-amino-2-nitrobenzoic acid diester; neopentyl glycol-4-amino-2-methylbenzoic acid diester; 1,8-octanediol-4-amino-2-propylbenzoic acid diester; 1,9-nonanediol-3-amino-4-methylbenzoic acid diester; and 1,10-decanediol-4-(4-aminophenyl)benzoic acid diester. Mixtures of such diesters may be employed. A particularly preferred diester of this type is the diester of trimethylene glycol (1,3-propanediol) and 4-aminobenzoic acid. In the practice of this invention the organic tetracarboxylic acid preferably in the form of its diester, most preferably from methanol or ethanol, is reacted with the above-referred-to amine(s) to form a prepolymer in the form of a consolidated, fragile foam structure, which is then subjected to additional heating in order to effect imide formation and thereby cure the polymer. When using the tetracarboxylic acid ester this operation can be conducted either in the presence or absence of an added blowing agent to provide the desired polyimide foam. The relative proportions used in the preparation of the precursors and polymers of this invention can be varied. In general, it is preferred to employ essentially stoichiometric proportions as between the mixture of tetracarboxylic acids or derivatives thereof and the primary diamine(s). However, non-stoichiometric mixtures can be used although the excess of the reactant present in excess usually does not participate in the reaction. As noted above, 1 to 40 mol percent (preferably 10 to 30 mol percent, most preferably about 20 mol percent) of the combination of tetracarboxylic acids or derivatives thereof employed is composed of one or more dicarboxycyclohexenyl succinic acids or their derivatives. The balance of the combination is preferably composed of one or more aromatic or heterocyclic diamines with or without the addition of still other diamines, for example diamines of the type referred to hereinabove in Formulas I, II, III, IV and V, or any mixture thereof. Usually the overall combination of amines will contain no more than about 10 mol percent of the diamines of Formulas I, II, III and IV. In the case of diamines of Formula V, these may comprise up to about 40 mol percent of the mixture of diamines used. In accordance with one preferred form of the invention, use is made of a combination of aromatic amines, one of which is a nitrogen heterocyclic diamine, preferably 2,6-diaminopyridine and/or 3,5-diaminopyridine, while the other is a diamine containing two benzene rings, preferably 4,4'-methylenedianiline and/or 4,4'-oxydianiline. When using a combination of aromatic amines in accordance with this concept, the mol ratio of the non-heterocyclic diamine to the nitrogen-containing heterocyclic diamine is within the range of 1.0 to 3.0, and preferably 1.5 to 2.8. When using a lower alkyl ester of the tetracarboxylic acid, the resulting alcohol produced in the reaction as well as the water released during the reaction can be used as the blowing agent during polymerization to form the desired polyimide foams. Alternatively, use can be made of any of a variety of organic or inorganic blowing agents. By use of a solid blowing agent such as Celogen R TSH, Celogen R OT, Celogen R AZ 130, Celogen R RA, Celogen R HT 500 Celogen R HT 550, sodium bicarbonate, benzenesulfonyl hydrazide, boric acid, benzoic acid, and Expandex R 5 PT of controlled particle size, the homogeneity of the cellular structure of the resulting polyimide foam can be more accurately controlled. Preferred for such use are solid blowing agents which have been subjected to ball milling or other grinding so that the blowing agent is less than 200 µm (microns) in diameter, with 98 percent of the blowing agent particle sized being less than 150 µm (microns) in diameter. The chemical compositions of the blowing agents identified by trade name above follow: Blowing Agent Chemical Composition Celogen R TSH toluenesulfonyl hydrazide Celogen R OT p,p'-oxybis(benzenesulfonyl hydrazide) Celogen R AZ 130 azodicarbonamide Celogen R RA p-toluenesulfonyl semicarbazide Celogen R HT 500 a modified hydrazine derivative Celogen R HT 550 hydrazol dicarboxylate Expandex R 5 PT 5-phenyltetrazole Variations in the concentration of the blowing agent can be used to achieve specific densities and ILD values. Concentrations of up to 10 percent based on the weight of the polyimide precursor, and preferably 1 to 5 percent, can be employed. A concentration of about 2.5 weight percent is particularly preferred. Hydrated organic compounds of the type referred to in U. S. 4,621,015 may also be used as blowing agents in the process. In the practice of this invention, it is possible to include in the reaction mixture various filler and/or reinforcing materials. For example, graphite, glass and other synthetic fibers can be added to the composition to produce a fiberreinforced product. Microballons may be added for density adjustment, if desired. It is frequently desirable to employ a surfactant thereby increasing cellular structure stability and uniformity, and increase fatigue resistance and make the foam more flexible and resilient. The nature of such surfactants for this use is well known and reported in the patent literature. Although not necessary, for some applications it is desirable to add a suitable quantity of a flame retardant material to the formulation in order to still further increase the flame resistance of the resultant foam. In preparing the precursors of this invention, it is preferred to employ the procedures and spray drying techniques described in U. S. 4,296,208. The temperatures at which the precursor is converted to the polyimide foam are generally those temperatures used in the preparation of other polyimide polymers. As a general rule temperatures ranging from 200 to 400°C can be used, with heating times from 5 to 60 minutes or longer. As those skilled in the art will appreciate, the time for carrying out the reaction is somewhat dependent upon the reaction temperature, higher temperatures enabling the use of shorter reaction times. It is also possible to heat to a lower temperature in the first stage of the reaction and then to higher temperatures in the later stages. Heating can be carried out in a conventional oven if desired. Alternatively, the foaming and curing of the precursor into a foamed polyimide polymer can be effected by means of microwave heating. In this technique, the precursor is exposed for 1 to 120 minutes to radio frequencies within the range of 915 to 2450 MHz, with the power output ranging from 1 to 100 kW. The power output to prepolymer weight ratio generally falls within the range of 0.1 to 10 kW per kg. Having described the basic concepts of the invention, reference is now made to the following example which is provided by way of illustration, but not by way of limitation of the practice of the invention. EXAMPLE A series of runs were conducted using 55 to 70 kg of a polyimide precursor powder in a microwave transparent mold using a microwave power input of 30 kW. The well-mixed powder was composed of 4,4'-methylenedianiline (MDA), 2,6-diaminopyridine (DAP) and benzophenone tetracarboxylic acid dimethyl ester (DTDE) in the mol ratio of approximately 0.7 MDA : 0.3 DAP : 1.0 BTDE. The powder was covered with a layer of polyvinyl chloride film, and an aluminum microwave shield 0,32 or 0,64 cm (1/8 or 1/4 inch) thick was positioned directly below the powder bed. The shield was covered by a temperature resistant cloth, and rested upon a layer of polyimide foam thermal insulation. The artifacts were formed in microwave-transparent molds, and were removed therefrom and cured in a thermal oven at 260°C to 288°C (500-550°F) for 30 minutes. In each case the yield of specification grade foam was significantly higher than a control run in which no shroud or shield was used.

Claims: Method of producing a foamed polymer structure in a microwave cavity in which a polyimide precursor is exposed to microwave radiation of intensity sufficient to cause the development of a foamed polymer through the generation and evolution of gaseous material within the precursor as it foams, which process comprises (a) maintaining the polyimide precursor and the foam as it is developing therefrom under a substantially vapor-impermeable microwave-compatible shroud that does not substantially restrict or impede development of the foam and prevents the surface of the foam from drying out as it would if left exposed; and (b) directing the microwave radiation upon the top, sides and ends of said polyimide precursor and of the foam as it is developing therefrom, but curtailing the extent to which such radiation impinges upwardly into the bottom of said precursor and said foam as it is developing therefrom by maintaining a microwave radiation-curtailing shield between said precursor and foam and a source of microwave radiation therebelow. Method according to claim 1 wherein the shield is a metallic shield. Method according to any of the claims 1 or 2 wherein the shield is composed primarily or exclusively of aluminum. Method according to any of the claims 1 to 3 wherein said shroud is a polymer film. Method according to claim 4 wherein said polymer film is a polyvinyl chloride film. Method according to any of the claims 1 to 5 additionally comprising the steps of raising the temperature of at least the lower portion of the polyimide precursor to a temperature in the range of 50 to 200 °C; and while at least the lower portion of said polyimide precursor is at said temperature, commencing the exposure of the polyimide precursor to microwave radiation. Method according to claim 6 wherein the temperature is in the range of 60 to 130 °C. Method according to any of the claims 1 to 7 additionally comprising the step of maintaining the precursor and the foam as it is developing therefrom, concurrently with exposing it to microwave radiation, under an atmosphere enriched in vapors of a lower alcohol. Method according to any of the claims 1 to 8 additionally comprising the step of curing the developed foam structure into a polyimide foam. A bun of cured polyimide foam produced by the method of any of the claims 1 to 9.

Inventors: BROEMMELSIEK HENRY EUGENE, LANIER CAROLL WENDELL, LEE RAYMOND, BROEMMELSIEK, HENRY EUGENE, LANIER, CAROLL WENDELL, LEE, RAYMOND
Applicants: ALBEMARLE CORP, ALBEMARLE CORPORATION
Application year: 1989
Main classification: C08J9
IPC codes: C08J9, B29C44, B29C35, B29C33, B01J19