Foaming compositions and methods for making and using the composition

Abstract

A low-temperature foam compositions and that are produced from an epoxy compound and an acid source can be substantially free of polyurethane or isocyanate chemistry. The disclosed compositions and precursors thereof reduce, if not eliminate, the presence of conventional undesirable compounds and by-products thereof.

Description

FIELD OF THE INVENTION

The invention relates to foam compositions, precursors thereof and methods for making foam compositions and foam containing articles.

BACKGROUND OF THE INVENTION

Foams are employed in a wide range of commercial applications including applications requiring thermal and sound insulation such as automotive and construction environments, among others. In the automotive industry, foams are typically formed in situ, and can be used to fill cavities such as pillars and rocker panels, and to dampen sound transmission. In situ foam formation has typically been accomplished by using a polyurethane foam based on isocyanate chemistry. Certain polyurethane foam components and by-products thereof are believed to have an undesirable environmental impact. Consequently, there is a need in this art for a low-temperature foam which is cost-effective and substantially free of undesirable materials.

SUMMARY OF THE INVENTION

The invention is capable of solving problems associated with conventional foam formulations by providing foam compositions and precursors thereto which do not require the use of isocyanates. The inventive compositions and precursors can thereof reduce, if not eliminate, the presence of conventional undesirable compounds and by-products thereof while providing benefits associated with conventional foams, e.g, sound/vibration dampening, thermal insulation, structure reinforcement, floatation, energy dissipation, among other benefits. In addition, the inventive foam has a reduced cured and tack time in comparison to conventional polyurethane foams. These properties in turn improve the efficiency of manufacturing processes that employ foam.

One aspect of the invention relates to a method of reacting an epoxy compound and a hydrogen donor or acid compound at ambient conditions to produce a foam. This reaction can produce a relatively large exotherm. The heat released by the exothermic reaction can be sufficient to drive an endothermic blowing agent, thus creating a foam virtually instantaneously. In fact, the exothermic reaction can be sufficiently large to cause a blowing agent entrapped within, for example, thermoplastic powders to expand thereby forming a foam.

Another aspect of the invention relates to a method of containing the foam during expansion by expanding the foam within a containment or control means. The control means confines the expanding foam and determines the direction of expansion. While any suitable control means can be employed, a polymeric bag or sack is desirable. If desired, the polymer bag comprises an adhesive material, e.g., the bag adhesive is activated by the exothermic foam reaction and affixes the resultant foam to a substrate. The polymeric bag can be fabricated from a virtually unlimited array of materials and configured into any desirable shape, e.g., a honeycomb structure, replicating an automotive cavity, etc.

The inventive foam can be employed in a wide array of end-uses. Examples of such uses include thermal insulation such as appliances, e.g., refrigerators, hot water heaters, etc; aircraft; commercial or residential construction such as spray or rigid insulation for walls, doors, cavity/widow sealant, acoustical control, etc.; packing material, e.g., foam-in-place; marine foams; environmental control, e.g., spill containment; footware; furniture; toy and consumer goods; protective equipment such as pads, helmets, etc.; fluid filtration; transportation industry uses, e.g., sound dampeners, structural supporting material, etc. for cars, trucks and heavy duty vehicles; vehicle repair; gasketing material; medical uses such as casts, emergency immobilization, etc.; artistic medium such as decorative brick/block, figures, etc.; among others.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a graphical representation of the foam reaction rate and temperature as a function of percent acid.

FIGS. 2A and 2B are a schematic drawings of assemblies that can be employed for dispensing the inventive foam within a defined cavity or area.

DETAILED DESCRIPTION

The invention is based, at least in part, on the surprising discovery that superior foam compositions can be produced from epoxy compounds and acids or hydrogen donor compounds, and in particular, a reaction of the epoxy compounds with the acid source.

Moreover, the inventive compositions can be polyurethane and/or isocyanate free. By “free” it is meant that the inventive compositions before or after foaming contain less than about 10 wt. % polyurethane and/or isocyanurates, isocyanate, and in most cases 0 wt. %. While the presence of such compounds does not adversely affect the reaction described below in greater detail, these materials can be obviated by employing the inventive formulations. The instant invention, therefore, provides a foam which can be used with or instead of urethane/isocyanate based foams and foaming systems.

The inventive foam composition is typically obtained from the reaction of one or more foam precursors. The precursor(s) comprise (i) at least one epoxy compound, and (ii) at least one acid source, i.e., a hydrogen donor or an acid, e.g., phosphoric acid, or a compound such as a photoinitiator which can upon activation provide a hydrogen donor or an acid, and (iii) at least one expansion or blowing agent, among other components. An exothermic reaction between the epoxy and hydrogen donor or acid can activate the expansion or blowing agent thereby producing a foam.

The foam precursor(s) can comprise a single phase system that is activated in response to a source of energy, e.g., heat, UV or electron beam or laser radiation, among other energy sources, or a two component system (an A side precursor and a B side precursor) that are contacted together to produce a foam. When a two component system is employed the epoxy and acid source are provided in separate “side” components.

Alternatively, the foam precursor(s) can comprise a two component system that is activated in response to a source of, e.g., heat, UV or electron beam or laser radiation, among other energy sources. The two component system can include an acid source as well as a photoinitiator.

The first component of the precursor(s), an epoxy compound, comprises about 10 to about 80 wt % of the precursor(s). Examples of suitable epoxy compounds include bis-phenol A epoxy, bis-F epoxy, epoxy-modified elastomers, epoxy-modified polybutene, epoxy-modified polybutadiene, epoxy-modified ethylene-propylene-diene rubber (EPDM), cycloaliphatic epoxy, novolac compounds, and mixtures thereof, among others. When a two component system is employed, the epoxy is located on the A-side, or otherwise prevented from prematurely reacting with the acid or other precursors.

The first component of the precursor can be tailored by adding one or more modifiers. For best results, the modifier is solublized by the epoxy or miscible with the epoxy. Examples of suitable modifiers can comprise at least one member selected from the group consisting of styrene and co-polymers thereof, vinyls and co-polymers thereof, elastomers such as nitrile. ethylene acrylic rubber, mixtures thereof, among others compounds that do not adversely impact the exothermic reaction. Some commercially available materials that can be employed as a modifier comprise Kraton® (Shell Chemical), Vamac® (DuPont), Piccolastic® (Hercules), Phenoxy® (Paphen), SAA® (styrene-allyl-alcohol copolymer (ARCO), G-Cryl® (Henkel), Rohagum® (Rhomtech), acrylate modified acidic adhesion promoting agent (acid functional oligomer, RadCure®), mixtures thereof, among others. Normally, the epoxy modifier comprises about 2 to about 50 wt. % of the composition prior to foaming.

A second component of the precursor(s) is the acid source. When a two component precursor system is employed, the acid source is present in the “B side” of the foam precursors. The hydrogen donor or acid usually comprises about 1% to about 30 wt. % of the precursor, and in particular, about 3% to about 15% of precursor B-side precursors. Examples of suitable acid sources include Lewis acids such as sulfonic acids, phosphoric acid, citric acid, carboxylic acid, glycolic, tannic, 1,2,4,5-Benzenenetracarboxylic acid, citraconic acid, L-(+)-Citrulline, fumaric, maleic, azelaic, oxalic acids, and mixtures thereof, among others. Particularly desirable results have been achieved by employing at least one of sulfonic, phosphoric acids and other acid functional compounds, e.g., acid functional acrylics. Depending upon the desired reaction rate and resultant foam characteristics, a relatively concentrated acid can be employed. An example of such a concentrated acid comprises a phosphoric acid that is substantially free of water. By “substantially free” it is meant that the acid contains less than about 10 wt. % and normally less than about 5 wt. % water. Substantially water free acid can be obtained by distilling commercially available acids, e.g., 75% phosphoric acid can be concentrated by distillation. In the case of phosphoric acid, concentration by distillation permits obtaining at least one of meta, ortho and pyro-phosphoric acids. At least one of ortho or pyro-phosphoric acid and mixtures thereof are effective as an acid source when a relatively strong and rigid foam is desired, e.g., an acid source comprising about 50 to greater than 90 wt. % ortho-phosphoric acid. If desired, the acid can comprise an acid functionally equivalent to the hydrogen donor released by a UV photoinitiator, e.g., replace a portion of the photoinitiator with its corresponding acid.

In one aspect of the invention, an acid substantially free of water is employed to obtain a foam precursor that generates foam having improved structural properties, e.g., foam having a flexural strength about 20 to 100% greater than many conventional materials such as wooden particle board. By employing a substantially water free acid as a foam precursor, the resultant foam has a lower expansion and water absorption, and greater structural strength and adhesion, e.g., to a painted or primed metal surface, wood, particle board, corrugated paper such as honeycomb, ABS, Formica®, Masonite®, thermoplastics such as polystyrene, among other surfaces. Substantially water free acids can also permit using a wider range of precursors, e.g., non-polyol carriers.

The adhesion of the foam to certain substrates, e.g., ABS, can be improved by pre-treating or priming the substrate surface. An example of a suitable primer comprises applying a silane coating (e.g., Z6040 supplied by Dow Chemical) onto the surface. The silane forms a coating to which the foam can adhere. Adhesion can also be improved by embossing or roughening the surface of the substrate.

A mechanical fastener can be attached to or incorporated within the substrate such that the foam embeds the fastener. The fastener can comprise a plurality of protrusions, studs or mechanical fastening means having any desirable shape can be located within a cavity to be filled with foam and/or attached to the substrate that contacts the foam. When studs are employed, the studs can be welded, e.g., sonically welded to a thermoplastic, within a cavity to be filled with foam. Protrusions can also be affixed within the cavity or upon the surface by a suitable adhesive, or by mechanical attachment. The height and specific configuration of the protrusions depends upon the application. These protrusions can be fabricated from any suitable material such as thermoplastics such as nylon, metal, among other materials. When introduced into the cavity, the inventive foam composition or precursors thereof embeds the protrusions, fills the cavity and embeds the protrusions thereby affixing the foam within the cavity or onto a substrate.

In another aspect of the invention, the hydrogen donor comprises a photo-initiator that becomes active when exposed to a source of energy. While any photoinitiator capable of becoming a hydrogen donor upon activation can be employed, specific examples of a suitable photoinitiators include a UV catalyst such as UVI 6974 (Union Carbide) that is described in greater detail in the aforementioned copending and commonly assigned U.S. non-provisional patent application Ser. Nos. 09/081,966, filed on May 20, 1998 and Ser. No. 09/197,107, filed Nov. 20, 1999, both filed in the name of Jeffrey Pachl et al., and entitled “Curable Sealant Composition”. Alternatively, free radical photoinitiators can be employed. An example of a free radical photo-iniator comprises 2-hydroxy-2-methyl-1-phenyl-propan-1-one, e.g., DAROCUR® 1173 (Ciba-Giegy). Free radical photoinitiators can be employed in systems comprising at least one of monomers and oligomers such as acrylated oligomers, urethane acrylates, acrylated epoxies, acrylated acrylics, acrylated polyesters, acrylated polybutadiene, methacrylated counterparts thereof, among others. When such initiators are employed, the foam precursors can be utilized in a single or multi-phase system.

For example, such a single phase system can be dispensed, exposed to a UV light source or other suitable source of energy that causes the UV catalyst to generate an acid thereby permitting the epoxy or free-radical reaction to occur. The heat released by the exothermic reaction in turn activates an expansion or blowing agent, e.g., a hydrocarbon encapsulated within a thermoplastic, thereby producing a foam. While any suitable single or two phase system can be employed, normally a single phase system produces a foam that is thin relative to a two phase system. Similar to other foam precursors, the radiation activated precursors can be modified for controlling the properties of the precursors or resultant foam, e.g., about 1 to about 20 wt. % polystyrene is added to the epoxy component.

The blowing agent can comprise one or more of the blowing agents recognized in the foam-forming field. Example of suitable blowing agents include water, hydrazide, diphenyloxide-4,4-disulphohydrazide, carbonamide, azocarbonamide, hexamethylene diamine carbamate, sodium bicarbonate, dimethyl ether, methylene chloride, carbon dioxide, fluorocarbons such as difluoroethane, tetrafluoroethane, HFC-4310, azeotropes and isomers thereof, among others; and hydrocarbons such as isobutane, butane, propane, pentane, isopentane, alcohol, isomers thereof; mixtures thereof, among other known blowing agents. Normally, the expansion or blowing agent comprises about 1 to about 40 wt. % of the foam precursor(s). The blowing agent can be present in either the A or B side of a two component system, although the B-side precursor is preferred.

The foam precursor(s) can also include at least one carrier component, e.g., a polyol, and optional components such as thermoplastics. A carrier usually comprises about 1 to about 40 wt. % of the precursor, e.g., preferably about 10-30 wt. %. The carrier typically serves to deliver a component, e.g., an acid, expanding agent, catalyst, mixtures thereof, among others for contact with the epoxy. Examples of suitable carriers comprise at least one member selected from the group of polyols including polyester, polyether, polycarbonate and caprolactone; alcohol, polyvinyl alcohol, synthetic or natural oils such as castor, soy, linseed, glycerin and glycols; water, among other carriers that are preferably miscible with the epoxy and mixtures thereof. When a two component precursor system is employed, these carrier materials are typically added to the acid side or “B side” component of the foam precursors

In addition to the aforementioned epoxy modifiers, the components of the precursor can be tailored by adding one or more modifiers in order to control viscosity, improve stability, physical properties, reaction rates, color, odor, among other characteristics. For best results, the modifier is solublized by the carrier or miscible with a carrier. Examples of suitable modifiers can comprise at least one member selected from the group consisting of natural and synthetic oils such as at least one of castor, soy, canola, linseed, polybutene, epoxidized counterparts thereof, among other oils. Epoxized natural oils such as epoxized castor oil can be employed as a Part A component. The addition of castor oil can also produce a foam having an exterior glaze or skin. Normally, the carrier modifier is used about 2 wt. % to about 50 wt. % of the composition prior to foaming.

Moreover, the density, moisture and temperature resistance among other physical properties of the final foam product can be modified or tailored by adding a thermoplastic, theromset, plastic or resinous material to the epoxy-containing precursor. While any suitable modifying material can be employed, examples of such modifying materials include dicyandiamide (Dicy (Amicure CG 1400)), ethylene vinyl acetate, polypropylene, polyethylene, rubber, phenoxy resin, phenolics, powdered wax, solid epoxy such as bis-A epoxy or modified epoxy, novalac compound, mixtures thereof, among others. For example, depending upon the relative concentration of the components of the precursor, polyvinyl alcohol, hydroscopic polyolefin such as modified polypropylene (as well as other suitable materials) can be employed as modifiers and for absorbing steam or water generated by or during the exothermic reaction. About 1 to about 60 wt. % of modifying material can be added relative to the epoxy, e.g., about 2 wt. % of the precursor(s). The modifying material will normally comprise a powder having a particle size less than about 20 microns and a melting point from about 150 to about 400 F. The modifying material will become fluid and normally melt when exposed to the exothermic reaction temperature. When a two component precursor system is employed, these materials are normally, but not necessarily, combined with the epoxy or “A side”.

The foam precursors can also include a thermoplastic component that can function to modify the properties of the resultant foam, reduce material cost, increase precursor shelf life, among other desirable results. The thermoplastic component of the foam precursor(s) can comprise at least one member selected from the group consisting of acrylonitrile, polyethylene, phenolic, wax, EVA, polypropylene, GMA, acid modified polyethylene, polybutadiene, modified polyethylene blend (such as Bynel® supplied by DuPont Company), SIS or SBS or SEBS blocked copolymers (such Kraton® supplied by Shell Chemical), oligomers, polyolefin, hydroxyl or epoxy functional compounds, among other thermoplastic materials that can be dispersed in a foam precursor and have a melting point less than about the aforementioned exothermic reaction and mixtures thereof. Normally, the thermoplastic component of the precursor will comprise about 1% to about 60 wt. % of the precursor. The thermoplastic component can possess any desirable configuration or particle size. In some cases, the thermoplastic component can form a film or skin upon an exterior surface of the foam thereby improving the resistance of the foam to fluids, e.g., water, gasoline, among other fluids.

In an aspect of the invention, the flame resistance of the foam can be improved by adding an effective amount of at least one member selected from the group consisting of halogenated epoxy as a component of the epoxy (brominated epoxy Erisys® GE-29), aluminum trihydrates, zinc borate, among other commercially available flame retardants. If desired, a halogenated epoxy can replace a portion of the Part A epoxy. Normally, the flame retardant comprises about 0.5 to about 15 wt. % of the unexpanded foam composition.

In one particularly useful aspect of the invention, a liquid or gaseous blowing agent is combined with or encapsulated within a thermoplastic particle or powder, e.g., a hydrocarbon encapsulated within an acrylonitrile shell as in Expancel® that is supplied by Expancel Inc., a division of Akzo Nobel Industries. When a two component precursor system is employed, the shells are normally combined on the B side along with the carrier. These shells can, however, be combined with the A side or in a single phase system so long as the composition of the shells is not substantially affected by the epoxy, e.g, the acrylonitrile or vinylidene chloride shells may be soluble within the epoxy. For example, the shells can be fabricated from polyolefins such polyethylene and polypropylene; vinyls, EVA, nylon, acrylics, among other materials not soluble in the epoxy component, and mixtures thereof could be present in the epoxy component of a two phase precursor system. The shells are selected to melt, soften, expand, rupture or retain their physical configuration depending upon whether or not an open or closed cell foam is desired. The shells can also comprise a distribution of differing particle sizes, composition and activation temperatures, e.g., a foam precursor comprising at least two different particle sizes and activation temperatures. A foam comprising particles having a range of sizes and compositions is especially desirable when producing an acoustical foam. The acoustical properties of a foam can also be improved by employing particles encapsulating blowing agents of more than one composition, e.g., employing shells encapsulating differing blowing agents. Specific examples of suitable encapsulated blowing agents comprise at least one member selected from the group of hydrocarbons such as isobutane and isopentane; fluorocarbons such as 1-1dichloroethene, HFC-134a, HFC-152a; and nitrogen releasing chemical blowing agents such as those supplied as Celogen® by UniRoyal that are encapsulated within any suitable thermoplastic, e.g., 2-methyl 2-propenioc acid methyl ester polymer with 2-propenenitrile and vinylidene chloride polymer and polyvinylidene fluoride. These materials are supplied commercially by Expancel, Inc., a division of Akzo Nobel as Expancels® 051WU, 051DU, 091DU80, 820WU, 820DU, 642WU, 551WU, 551WU80, 461DU or Micropearl® F30D supplied by Pierce and Stevens. These materials can be supplied in either dry or wet form. These materials can also be coated with any suitable material for controlling the activation temperature of the encapsulated blowing agents. An example of a coating comprises an acrylated materials, waxes, among other materials. When the A and B sides are contacted (or in the case of a single phase system exposed to an energy source), the epoxy reacts with the hydrogen or acid thereby releasing heat and causing the expansion agent within the shells to foam. The foam can be characterized by a composite wherein the epoxy reaction product (including of the aforementioned modifying materials) forms a matrix that embeds the expanded shells. Depending upon the physical characteristics desired in the foam, the shells can be open or closed cells.

In a further aspect of the invention, the encapsulated foam precursor can comprise at least one member selected from the group consisting of an acid source, a curing agent, surfactants, epoxy accelerators, among other foam precursors. By curing agent it is intended to mean one or more compositions, other than an acid source, that causes an epoxy functional material to react, exotherm, and cross-link. Examples of curing agents comprise at least one member selected from the group consisting of imidazoles, amines, amides, derivatives thereof, among others. If desired an encapsulated or unencapsulated acid source can be employed in conjunction with an encapsulated curing agent. An example of an encapsulated or polymer bound curing agent comprises those supplied by Landec as Intelimer® 7001, 7002, 7004, 7024 and mixtures thereof. By employing one or more encapsulated or polymer bound foam precursors, it is possible to produce a foam by a multiple stage reaction method wherein the resultant foam has enhanced physical properties, e.g., density, water absorption, hardness and strength.

The foam characteristics can also be modified by adding one or more filler materials to the precursor(s). Conventionally used filler materials comprise at least one of talc, mica, magnesium silicate, oxidized polyethylene, sodium silicate, alcohols, petroleum jelly, aromatic acid methacrylate-mixed half esters, methacrylated polybutadiene, concrete mix (supplied commercially as Quickrete®), arylalkoxy silane, hollow ceramic spheres, inorganic microspheres, dispersants, conventional blowing/expansion agents, flame retardants such as phosphates, borates and halogenated compounds; plasticizers, diluents, pigments, colorants, metal or ceramic powders, soybean hulls, pecan hulls, rice hull, antimicrobial agents such as fungicides, fumed silica, abrasive materials, magnetic materials, anti-static or conductive materials, mixtures thereof, among others. If desired calcium carbonate can be added to the foam precursor for increasing the hardness and density of the resultant foam. When included the filler comprises about 1 to about 60 wt. % of the foam precursors.

The inventive foam can be matrix that embeds or contacts other materials in order to obtain a composite structure. The compositing materials can comprise the aforementioned filler materials, previously formed preform or structures, e.g., honeycomb, fibrous mat, shaped particulate member, honeycomb structures, syntactic materials such as described in U.S. Pat. No. 4,568,603 hereby incorporated by reference; among others. The compositing material can be added to a foam precursor and/or introduced when foaming the precursors. In one aspect, the compositing material comprises styrene pellets, e.g., recycled packaging material, that is ground and added to the previously described carrier. These pellets function to reduce weight and cost of the resultant foam. In another aspect, the compositing material comprises a material for improving the compressive strength of the foam and/or spacers for limiting the degree to which the foam can be compressed, e.g., nylon, polyolefins, polyethylene, among other materials. The compressive strength improving materials can be of any suitable form such as cubes, beads, mixtures thereof, among other shapes.

In one aspect of the invention, one or more foam precursors interact to form an intermediate foam precursor. The intermediate foam precursor can correspond to a Part A and/or Part B. The intermediate foam precursor can be contacted with another precursor or another intermediate foam precursor in order to obtain a foam. A carrier such as a polyol, e.g., a polyester polyol, can interact with at least one member selected from the group of an acid source, e.g, phosphoric acid; a modifier, e.g., styrene; among other precursor components. An epoxy can interact with at least one member selected from the group of an acid source, e.g., phosphoric acid; a modifier, e.g., styrene; among other precursors that are miscible with the epoxy. If desired the aforementioned carrier containing intermediate product is contacted with the aforementioned epoxy containing intermediate product to obtain a foam. The intermediate precursor can be self-supporting. The combined intermediate products can produce a gel-like product that in turn is converted to a foam, e.g, the intermediate product can comprise a gel that can be shaped prior to onset of foam formation.

The precursor(s) and/or intermediate products thereof can be pre-blended and stored in separate containers prior to use. To this end, an A-side or first precursor mixture is typically obtained by combining the epoxy and modifying material, e.g, polyvinyl alcohol and polypropylene, and a B-side or second precursor mixture can be obtained by combining the carrier, e.g., a polyol, hydrogen donor/acid and thermoplastic, e.g., encapsulated blowing agent.

The precursor(s) can be produced using any suitable apparatus that imparts an amount of shear sufficient to obtain a substantially homogenous precursor. Examples of suitable apparatus comprise hand mixing, static tube mixtures, the structures described illustrated by FIGS. 2A and 2B (described below in greater detail), impingement spraying precursors, extrusion, e.g., a twin screw extruder, among other conventional apparatus. Normally, the samples are mixed for about 1 to about 40 seconds depending upon the composition and mixing environment, e.g., a 1:1 A:B composition can be mixed for about 1 to about 10 seconds in a static tube mixer.

The inventive method involves contacting the epoxy compound and acid or hydrogen donor under conditions effective to provide an exothermic reaction. The heat produced from the reaction can then cause the blowing agent(s) to expand in forming the desired foam. For example, where two precursors, A and B are employed, the two compositions can be combined—to obtain a foam by using conventional foam manufacturing equipment. For example, A-side and B-side can be contacted as two high pressure streams within a mixing chamber of an external mix-head. While heat can be added to the precursors, the reaction between “A” and “B” can occur at ambient conditions, e.g., to control viscosity, adjust reaction rate, etc. The ratio of A-side to B-side normally ranges from about 1:1 to about 10:1 or 1:10.

An example of a combined A and B side precursor composition is set forth in the following Table.

TABLE
Chemical Name	Trade Name	Supplier	Wt. %	Equivalent
Cycloaliphatic	Uvacure 1500	UCB	1-80	Sartomer-
Epoxy		Radcure		SARCAT ®
				K126
Caparolactone	Tone 0301	Union	0-70	—
		Carbide
Phosphoric Acid	Phos. Acid	J. T.	1-20	commodity
		Baker
Themoplastic	Expancel	Nobel	1-50	Pierce &
		Industries		Stevens-
				Micropearls ®

The pH of the A-side component (containing the epoxy compound(s)) is normally about 6 to at least about 8. The pH of the B side of the foam precursor comprising an acid and a carrier is normally about 0.5 to about 4, e.g., the pH of phosphoric acid when mixed with polyol. Normally, the pH prior to reaction with A-side precursors is about 1.6. The composition and concentration of the foam precursors can be modified to achieve a predetermined reaction rate e.g., by tailoring the concentration of the acid. The affects of the pH or acid concentration of the B side are better understood by reference to FIG. 1 which illustrates the affects upon the composition demonstrated in Example 9.

Referring now to FIG. 1 , FIG. 1 is a graphical representation of % acid in the precursor versus foam reaction time and temperature. FIG. 1 illustrates that as the acid concentration increases the reaction temperature increases and the reaction time decreases. FIG. 1 also illustrates that the precursor can be selected to a predetermined reaction time/temperature. For example, by selecting a higher reaction temperature (higher acid concentration) a wider range of modifying materials can be employed whereas by selecting a slower reaction time (lower acid concentration) the foam has easier handling characteristics.

The viscosity of a foam precursor can be tailored to enhance the resultant foam characteristics. The viscosity of the “A-side” or epoxy component of the foam precursor is normally controlled, for example, so that a modifying material, e.g., a plastic powder, becomes or remains dispersed within the “A-side” precursor. While any suitable viscosity control agent can be employed desirable results can be achieved by using a solid polymer (in particulate form) to produce a foam precursor gel.

Examples of suitable solid polymers comprise at least one member selected from the group consisting of waxes, polyethylene, EVOH, PVOH, fluoropolymers and dispersions thereof such as polytetrafluoroethylene (supplied as Teflon® by the DuPont Company), among others. The viscosity control agent can range in particle size of about 20 to 50 microns, e.g,. less than 325 mesh. An example of a controlled viscosity composition comprises about 5 to about 10 wt. % solid epoxy, about 5 to about 15 wt. %, powdered polyethylene and about 25 to about 30 wt. % blowing agent. In addition to viscosity, the characteristics of the foam can be tailored by varying the temperature, pressure, foam pH, foam density, among other parameters known to those skilled in this art. Also, the “A-side” of the system can be thickened into a gel by the addition of a surfactant such as any commercially available liquid detergent or titanate such as Kenrich KRTTS, e.g., about 0.1 to about 10 wt. % surfactant. This enables a more complete Theological control, included insuring the homogeneity of the system.

As discussed above, the foam can be produced from a single-phase system, e.g., only an “A-side” mixture. An example of such a system comprises an epoxy, a polyol, thermoplastic spheres, modifying materials, phenoxy, polypropylene, mixtures thereof, among other components. This one component system can be heat activated. In other words the system expands by being exposed to elevated temperature, e.g., about 125C. If desired the single phase foam system can be initiated by employing a photo-initiator instead of, or in conjunction with, an elevated temperature. Examples of such initiators comprise at least one member selected from the group consisting of Union Carbide UVI 6974 among others. Normally, the amount of such an initiator corresponds from 0.5 to about 5 wt % of the foam precursor. More details regarding photoinitiators can be found in “Photopolymerization Behavior of Several Cationic Photoiniators in Catatonically Cured Resin Systems” by Edward Jurczak; that is hereby incorporated by reference.

Single phase systems are especially useful when applied upon a substrate by being sprayed. For example, the single phase system can be sprayed upon an automotive subassembly for reducing the amount of sound transmission to the interior of the car. In a further example, the single phase system can be sprayed upon a first component, e.g., a plastic fascia, exposed to UV to cause foaming and affixed upon a second component, e.g, metal support member, wherein the foam functions to reduce vibrations between the components.

A composite foam structure can be obtained in accordance with the instant invention. A structural modifier such as fibers, particles, rods, tubes, powders, mixtures thereof, among others, can be incorporated as a component of the foam precursor. The structural modifier can be employed for tailoring the chemical and/or physical properties of the resultant foam. Examples of suitable structural modifiers, normally as chopped fibers, ceramic or glass spheres or powders, can comprise at least one of nylon, carbon, carbonates, polymers such as polyethylene and polypropylene, graphite, Kevlar®, Dyneon, ceramic, fiberglass, mineral fillers, e.g., mica, metals, among other materials. The amount of such structural modifiers normally comprises about 1 to about 60 wt. % of the uncured foam precursor.

Any suitable commercially available foam production equipment can be employed for mixing and dispensing the inventive foam precursors to obtain the inventive foam. Examples of such equipment comprises DoPag (ECONO-MIX) supplied by Kirkco Corporation, Monroe, N.C.; as well as equipment supplied commercially by Jesco Products Company, Inc, Sterling Heights, Mich. Another example comprises using an Econo-Mix pump in combination with an Albion static mix head. The foam precursors can also be mixed by employing a power mix gun such as supplied by Sealant and Equipment Company, Oak Park, Mich. If desired, the inventive foam can be expanded within a cavity, e.g., an automotive A pillar, by employing a dispensing apparatus having a replaceable/disposable static mix head. That is, the static mix head can comprise a replaceable plastic tubing having a center piece with a helix or vortex configuration, that is connected to a pump discharge flange and inserted into the cavity for foaming the precursors.

In one aspect of the invention, the inventive foam is dispensed through a commercially available dual tube dispenser (e.g., a 4:1 dual tube dispenser supplied by Tah Industries). That is, one of dual tubes is loaded with an inventive Part A composition and the other tube contains an inventive Part B. The Part A and B are dispensed by the dual tube dispenser and pass through a static tube mixer (also known as a motionless mixer). The Part A and B are contacted by the static tube mixer thereby causing the Parts A and B to react and produce a foam. When dispensing the inventive compositions via a dual tube dispenser, the inventive compositions can be employed as replacement for conventional caulks as well as commercial cavity filling foams, e.g., polyurethane foams.

Another static mix head design has a valve type of arrangement that is illustrated in FIGS. 2A and 2B . Referring now to FIG. 2A , FIG. 2A illustrates a one-way value type of arrangement wherein the foam or precursors thereof are introduced or injected via a one-way valve 1 (commonly known as a zerk) that is positioned within a cap 2 . Valve 1 can also include a flap or secondary valve 1 A that prevents foam from escaping by reverse flow through valve 1 . The cap 2 seals or defines one end of a cavity being filled with foam. The cap 2 can include hooks or locking tabs 3 for securing the position of cap 2 , e.g, within the so-called A pillar of an automobile thereby permitting foam to be dispensed within the automotive cavity in a controlled manner. Normally, one end of the valve 1 is connected to a mixing zone 4 such as the aforementioned static mixers having helical vanes 5 . After traveling through the valve 1 and static mixer 4 , the foam is released into the cavity to be filled with foam. The area and direction into which the foam expands can be control and/or defined by using a containment means such as a polymeric bag 6 (the containment means is described below in greater detail).

Referring now to FIG. 2B , this type of arrangement provides a longer mixing time for the foam precursors before the foam is released into the cavity to be filled. The arrangement illustrated in FIG. 2B can also be employed as a cap 10 to seal or define one end of the cavity to be sealed. After delivering the foam precursors, a mix head 11 or previously described valves ( 4 and 5 of FIG. 2 A). The foam precursors travel through mix head 11 and are released at the opening defined at 12 as foam. The opening 12 can also be within the aforementioned containment means. The caps 1 and 10 can remain associated with the foam product within the cavity. By using such a replaceable mix head, any problems associated with clogged mix heads are avoided. Two pressure streams can also be employed, to converge in a mix chamber or cavity to be foamed and mix action occurs without use of additional mixing apparatus. In addition to the foregoing, the inventive foam composition and precursors thereof can be injected, extruded, shaped, sprayed, cast, molded, among other conventional processes in order to obtain a desirable foam article. The configuration of the foam article can be virtually any shape including continuous shapes such as films or webs, discrete forms, among other shapes.

While the above description emphasizes particular foam compositions, the inventive compositions (and precursors thereof) can include additives such as dyes, fillers, surfactants, pigments, nucleating agents, among other conventional employed foam additives. If desired a pH indicator can be added to the precursor in order to provide a visual detection means for a reaction product. An example of a suitable pH indicator comprises at least one member selected from the group consisting of methyl red, methyl blue, chlorophenol red, bromothymol blue. That is, as the foam precursor react, e.g, acid-epoxy, the acid is consumed thereby changing the pH and causing the pH indicator to change color.

If desired, the inventive composition can be laminated or joined with other articles, e.g., laminated onto metal foil, Mylar, fiberboard, veneer, Formica® etc. In one aspect of the invention, the inventive foam precursors can be applied between two such laminating materials in order to form components that are useful in fabricating furniture. For example, the inventive foam is expanded between two laminating materials, one of which comprises the upper surface (e.g., a wood veneer) and the second the lower surface of a table top. Any excess foam can be removed by conventional methods such as sawing, scraping, etc. The foam imparts structural integrity to the article while reducing weight and fabrication time.

The inventive composition can also be expanded within a control or containment device or bag having a predetermined shape thereby forming a foamed article that replicates the bag, e.g, refer to U.S. Pat. Nos. 4,269,890 (Breitling), 4,232,788 (Roth), 4,390,333 (Dubois); the disclosure of each of which is hereby incorporated by reference. When expanding the foam into a bag, the previously described valves illustrated in FIGS. 2A and B ; those supplied commercially by Inflatable Packaging as part no. IP04, or any other suitable delivery means can be employed at the opening in the bag in order to control introduction of the foam into the bag.

For example, a bag replicating a cavity such as an automotive cavity or any other desirable configuration unrolls or expands into the cavity as foam is introduced into the bag via the valve. If desired, the bag may comprise or be coated with a heat sensitive adhesive wherein the heat generated by the exothermic foam reaction activates the adhesive. The adhesive can permanently affix the foam containing bag at any desirable location. The bag can also include predetermined areas having weakened seams or perforations that are designed to rupture as the foam expands thereby directing the expanding foam. Similarly, the bag composition can be selected such that the bag melts when exposed to the foam. The melting bag can direct the expanding foam, form a coating upon the foam, and function as an adhesive, among other utilities. Further, a plurality of bags can be employed wherein one bag is surrounded by another bag. The inner and/or outer bag can possess the aforementioned predetermined properties. Furthermore, the bag can comprise areas having distinct chemical and/or physical properties, e.g., a bag comprising one sheet of polyethylene heat sealed around its periphery to a sheet comprising polybutadiene. At least a portion of the bag can be fabricated from one or members selected from the group consisting of polyethylene, polyester, vinyl, nylon, Surlyn®, ethylene vinyl acetate, styrene-isoprene-styrene, styrene-butadiene-styrene or other blocked copolymers, polybutadiene, among other plastic materials with melt points corresponding to temperature range of reaction, polyamide, modified EVA's, modified polyethylene, modified polybutadiene, GMA, SBR, among other plastic materials suitable for bag or bladder construction and seaming capability. The bag or containment means can be utilized with a wide range of foam compositions in addition to the previously described epoxy containing foams. Examples of foams that can be expanded into the previously described containment bags or means comprise at least one of epoxy amine, acrylic, and phenolic among others.

The foam precursors can be removed from surfaces, equipment, among other articles by employing non-hazardous cleaning materials. An example of suitable cleaning material comprises water, isopropyl alcohol, 2-butoxyethanol and a chelating agent. The cleaning material can be dispensed as an aerosol by using a propellant such as DME, hydrocarbons and carbon dioxide.

Moreover, the inventive foam can be fabricated to possess a substantially uniform or varying density throughout one or more of its dimensions. The ability to tailor foam density in individual articles as well as throughout an article is a marked improvement in the art. Foams having varying densities can be employed for attenuating or focusing sound, various forms of electromagnetic radiation, radar, etc.

While the above description emphasizes a reaction between an epoxy containing compound and one or more acid or hydrogen donor, the inventive method can be achieved by employing other polymer systems such as silicones, urethanes, silanes, hydroxyl or caboxyl modified elastomers; hydroxyl, carboxyl or epoxy functional compounds, reactive liquid polymers such as Hycar®, among others. That is, a polymer system is contacted with an acid that generates an exothermic reaction which in turn activates an expansion or foaming agent.

The following Examples are provided to illustrate not limit the scope of the invention as defined in the appended claims. Unless indicated otherwise, commercially available apparatus and materials were employed in these Examples.

EXAMPLE 1

A foam product was produced by mixing a 2-part system (A-side precursor and B-side precursor) through a conventional foam production apparatus comprising a static mixer that was manufactured by Albion (Model No. 535-1 or equivalent). The constituents of the foam were maintained in two separate supplies of materials, an A-side precursor and B-side precursor.

The A-side precursor comprised a blend of the epoxy and the thermoplastic microspheres including a blowing agent, in ratio of 30 parts to 15 (100 parts total). The B-side precursor comprised a blend of the phosphoric acid and the polyol in a 30 part to 50 part ratio (also 100 parts). The feed ratio of A-side precursor to B-side precursor to the mixer head was 1:1. The pH of the B-side precursors was about 1.6 prior to reaction with A-side precursor.

A pressurized flow through the mixing chamber produced a polymer which rapidly expands and released an amount of exothermic heat sufficient to produce a foam.

EXAMPLE 2

The process of Example 1 was repeated with the exception that the ratio of epoxy to thermoplastic microspheres in A-side precursor was 2:1, and the ratio of phosphoric acid to polyol in B-side precursor was 3:5. The feed ratio of A-side precursor to B-side precursor to the mixer head was 3:1.

EXAMPLE 3

The process of Example 1 was repeated with the exception that the A-side precursor and B-side precursor components were mixed together by hand (instead of using the static mixer).

EXAMPLE 4

This example demonstrates the formation of a composite foam. The process of Example 1 was repeated with the exception that about 5 wt. % polytetrafluoroethylene powder (TEFLON® supplied by the DuPont Company) was added to the A-side precursor composition. The A-side precursor and B-side precursor were contacted in the manner described in Example 1. A composite foam was recovered wherein the composite foam had greater flexibility or pliability in comparison the foam obtained by the process of Example 1.

EXAMPLE 5

A two phase system was used to produce a foam. The A-side precursor was composed of epoxy and microspheres in a 2:1 ratio (67% epoxy, 33.3% microspheres) by weight. (It is noted that for best results, the mix should be used within in 4-8 hours of mixing since certain epoxies can dissolve certain spheres). The A-side precursor was hand-stirred to a smooth consistency.

The B-side precursor was composed of Polyol (Tone 0301) and Phosphoric acid (10%) by weight). The acid was blended into the polyol. A-side precursor to B-side precursor ratio of 1:1 was contacted in a static tube mixer and produced a foam. The ratio of A to B can be from 1:1 to 4:1 depending on acid concentration.

EXAMPLE 6

A two phase system was used to produce a foam. The A-side precursor comprised an of epoxy (UCB-Radcure UVACURE 1500). The B-side precursor was comprised of a polyol (50 wt. %—Tone 0301), phosphoric acid diluted with water (approximately 50% acid in a commercially available solution) at 20%, and 30% microspheres. The spheres were hand-stirred into the polyol to a smooth consistency. The acid mixture was blended by hand-stirred into the sphere-polyol mix. An A-side precursor to B-side precursor ratio of 1:1 was contacted in a static tube mixer and produced a foam. The ratio of A to B can be from 1:1 to 4:1 depending on acid concentration.

EXAMPLE 7

A two phase system was used to produce a foam. The A-side precursor comprised an epoxy (UCB-Radcure UVACure1500) While the B-side precursor comprised polyol (Tone 0301), polyvinyl alcohol and water blend (PVOH:H20 3:1 blend that corresponded to 20% of the polyol) and microspheres 30% by weight of polyol and acid can be 10% of total ‘B’ mixture. The spheres were hand-stirred into the polyol to a smooth consistency. The PVOH and water are hand-stirred. The PVOH/water solution temperature was 140° F. The PVOH blend was added to the polyol by hand stirring. The acid was hand-stirred into the sphere-PVOH-polyol mix. The A-side precursor to B-side precursor ratio of 1:1 was contacted in a static tube mixer and produced a foam. The ratio of A to B can be from 1:1 to 4:1 depending upon acid concentration.

EXAMPLE 8

A two phase system was used to produce a foam. The A-side precursor comprised an epoxy (UCB-Radcure UVACure 1500) and a phenoxy resin (Paphen PKHP-200 that corresponded to 25% of A-side precursors, epoxy is 75% of A-side precursors). The B-side precursor comprised 45% polyol (Tone 0301), 23.5% polyvinyl alcohol (Airvol 203S) and 23.5% microspheres. Phosphoric acid was 10% by wt. of the B-side precursor. Spheres are hand-stirred into the polyol to a smooth consistency. The PVOH, microspheres, and polyol are blended by hand stirring. The phosphoric acid was hand-stirred into the sphere-PVOH-polyol mix. An A-side precursor to B-side precursor ratio of 1:1 was used contacted in a static tube mixer to produce a foam. The A to B ratio can range from 1:1 to 4:1 depending on acid concentration.

EXAMPLE 9A

A two phase system, namely an A-side precursor and a B-side precursor, was used to produce a foam. The A-side precursor comprised an epoxy (UCB-Radcure UVACure 1500) 60 wt %, polypropylene powder (Equistar FP 800-00) 20 wt %, polyvinyl alcohol (Airvol 203S) 20 wt %. The B-side precursor comprised polyol (Tone 0301) 60 wt % and microspheres 30%. Phosphoric acid was 10%. Spheres are hand-stirred into the polyol until a smooth consistency was obtained. The microspheres and polyol are blended by hand stirring. The phosphoric acid was hand-stirred into the microspheres and polyol mix. An A-side precursor to B-side precursor ratio of 1:1 was used and contacted in a static tube mixer to produce a foam. The A to B ratio can, however, range from 1:1 to 4:1 depending on acid concentration.

EXAMPLE 9B

This Example employed a two phase system wherein the A-side precursor comprised a gel. A two phase system, namely an A-side precursor and B-side precursor, was used to produce a foam. The A-side precursor comprised an epoxy (UCB-Radcure UVACure 1500) 59 wt %, polypropylene powder (Equistar FP 800-00) 20 wt %, polyvinyl alcohol (Airvol 203S) 20 wt % and surfactant (gelling agent) at 1 wt %. The B-side precursor comprised polyol (Tone 0301) 60 wt % and microspheres 30%. Phosphoric acid was 10%. Spheres are hand-stirred into the polyol until a smooth consistency was obtained. The microspheres and polyol are blended by hand stirring. The phosphoric acid was hand-stirred into the microspheres and polyol mix. An A-side precursor to B-side precursor ratio of 1:1 was used and contacted in a static tube mixer to produce a foam. The A to B ratio can, however, range from 1:1 to 4:1 depending on acid concentration.

EXAMPLE 10

A bag or containment device approximately 8×8 inches in size and having a one-way valve located on one end of the bag was constructed from two sheets of high density polyethylene film. The seams of the bag were designed to rupture at specific locations, which directs foam expansion into cavity area adjacent to weak seams. The sheets were joined by heating on a TEW Electric Heating Company Ltd sealing apparatus. The seams were selectively reinforced by double sealing or weakened to provide multiple points for foam direction from the same bag. The foam composition demonstrated by Example 9 was introduced into this bag. As the foam expanded, the foam escaped from the bag through the relatively weak seams.

EXAMPLE 11

A bag or bladder composed of each of polyethylene, ethylene vinyl acetate, polybutadiene were fabricated by using the apparatus described in Example 10. The foam of Example 9 was introduced into these bags. The bags, having a melting point less than the exothermic reaction temperature of the foam, failed and released the foam.

EXAMPLE 12

A bag or bladder composed of each of modified EVA (Bynel®), modified polyethylene (Primacor® supplied by Dow Chemical Company), modified butadiene, glycidal methacrylate (GMA) were fabricated by using the apparatus of Example 10. The foam of Example 9 was introduced into these bags. The heat released from the exothermic reaction of the foam caused the bags to melt. The melting bag material adhered to the foam thereby modifying the surface of the foam. The melting bag also adhered the foam to any surrounding surfaces or articles.

EXAMPLE 13

A bag or bladder composed of each of polypropylene, polyethylene, woven nylon mesh, aluminized fiberglass mesh was fabricated by using the apparatus of Example 10. Each of the bags was further processed to possess multiple perforations (25-100 holes/in.). The foam of Example 9 was introduced into each of these bags. The perforations allowed the foam to escape in controlled quantities while also generally retaining the shape of the bag.

EXAMPLE 14

Two bags or bladders, namely an inner and outer bag were fabricated by using the apparatus of Example 10. The inner bag comprised modified butadiene and the outer bag comprised high density polyethylene. The inner bag was placed within the outer bag and the outer bag was sealed. The foam of Example 9 was introduced into the inner bag. Inner bag or bladder melted during the foam reaction. The inner bag was of sufficient size to contain the required amount of mixed foam precursors to fill the out bag. Outer bag construction was of material and size to contain reaction within the cavity.

EXAMPLE 15

The insertion loss or sound dampening characteristics of the foam produced in accordance with Example 9A was tested in accordance with Society of Automotive Engineers (SAE) J 1400. The sample size was 3×3×10 inches and placed within an E-coated metal channel. An increase in insertion loss corresponds to an increase in sound dampening properties that in turn corresponds to less noise within the passenger compartment of an automobile.

FREQ. (Hz) INSERTION LOSS (dB)
125        12.5
160        10.6
200        11.4
250        12.0
315        24.5
400        35.4
500        46.8
630        38.4
800        40.1
1000       45.7
1250       45.1
1600       49.6
2000       49.2
2500       50.1
3150       50.9
4000       55.5
5000       58.7
6300       59.2
8000       64.2

These data illustrate the desirable sound absorbing characteristics of the inventive foam compositions.

EXAMPLE 16

The viscosity of the Part A foam precursor fabricated in accordance with Example 9A was tested in accordance with conventional methods and apparatus (Brookfield Viscometer, Spindle 27, Thermal-Cell). The viscosity as a function of temperature is listed below.

	RPM	Temp 75 F.	Temp 110 F.	Temp 150 F.
	0.5	13,000	8,000	3,000
	1	10,500	5,500	2,500
	2.5	8,160	3,400	1,600
	5	6,680	2,300	1,100
	10	5,700	1,800	800
	20	4,830	1,480	600
	50	3,900	1,250	468
	100	3,280	1,100	404

The viscosity of the Part B foam precursor fabricated in accordance with Example 9A was tested in accordance with conventional methods and apparatus (Brookfield Viscometer, Spindle 27, Thermal-Cell). The viscosity as a function of temperature is listed below.

	RPM	Temp 75 F.	Temp 110 F.	Temp 150 F.
	0.5	22,000	13,000	4,000
	1	20,000	10,000	2,500
	2.5	18,600	7,000	1,600
	5	17,800	5,320	1,300
	10	17,300	4,500	1,100
	20		4,000	975
	50		3,700	880
	100		3,580	860

EXAMPLE 17

This Example illustrates foam formation as a result of being activated by exposure to an energy source, e.g, UV light. A radiation curable foam having the following components was prepared:

COMPONENT	TRADE NAME	SUPPLIER	AMOUNT
Cycloaliphatic epoxy	UVACURE 1500	Radcure	50	wt. %
Caprolactone polyol	Tone 0301	Union Carbide	40
Blowing agent	Expancel DU551	Expancel Inc.	9
Sulfonium salt	UVI-6974	Union Carbide	1

The above components were combined as follows. The Uvacure and polyol were added together in a mixing vessel and mixed until the solution was clear. The UVI 6974 was added to the mixture, and mixed until substantially completely dispersed (about 2 minutes). The Expancels spheres were added to the mixture and mixed until substantially lump free. For best results, the minimum amount of mixing time, and shear were employed.

The foam precursors were placed onto a conveyor and exposed to a source of UV light. The method for exposing the precursors to UV light is described in the previously identified U.S. patent application Ser. No. 09/197,107, filed Nov. 20, 1999, both filed in the name of Jeffrey Pachl et al., and entitled “Curable Sealant Composition”.

This UV activated foam was modified by adding an acrylic monomer or acrylated oligomer. This modified LTV activated foam was prepared as described above and comprised:

COMPONENT	TRADE NAME	SUPPLIER	AMOUNT
Acrylated	IRR 84	UCB RADCURE	93.5	wt. %
oligomer
Acid
functional
Oligomer	Ebecryl 170	UCB RADCURE	0.9
Photo-	Darocure 1173	Ciba-Giegy	0.9
initiator
Blowing	F30D-Micropearls	Pierce & Stevens	4.7
Agent

The resultant foam possessed a pressure sensitive adhesive characteristic. The tacky pressure sensitive characteristic was removed by adding an acrylate compound. A tack-free formulation comprised:

COMPONENT	TRADE NAME	SUPPLIER	AMOUNT
Acrylated	IRR 84	UCB RADCURE	92.6	wt. %
oligomer
Acid
functional
Oligomer	Ebecure 170	UCB RADCURE	0.9
Photo-	Darocure 1173	Ciba-Giegy	0.9
initiator
Blowing	F30D-Micropearls	Pierce & Stevens	4.7
Agent
Acrylate	Sartomer 444	Sartomer	0.9

The later two formulations were also activated by being exposed to natural light.

EXAMPLES 18-22 AND 25

The following Table lists the Components, Trade Names and Suppliers for the foam precursors that were employed in Examples 18 through 22 and 25. The foam in Examples 18-22 was prepared by contacting the Part A with the Part B listed in the tables below in a 2.75″ diameter by 1.92″ height ointment can and mixed by hand. Reaction Time and Temperature were determined in accordance with conventional methods. The percent vertical expansion as well as the shrinkage was determined visually. The Shore A test was conducted using a Type A-2 Shore Durometer Hardness test unit that meets ASTM D2240 requirements. The Shore A test was conducted about 4 hours after foam formation. The instantaneous peak reading was recorded.

Trade Name	Component	Supplier
Epon 862		Bis F/Epichlorohydrin Epoxy Resin	.Shell Chemical Co.
Expancel 091DU80	(244F)	Blowing Agent (thermal)	Expancel, Inc
Expancel 051DU	(223F)	Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
		propenoic acid methyl ester polymer with 2-
		propenenitrile and isobutane is the blowing
		agent
Expancel 054WU	(257F)	Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
		propenoic acid methyl ester polymer with 2-
		propenenitrile and isopentane is the blowing
		agent
Expancel 461DU	(208F)	Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
		propenoic acid methyl ester polymer with 1,1-
		dichloroethene and 2-propenenitrile and
		isobutane is the blowing agent
Expancel 551WU	(199F)	Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
		propenoic acid methyl ester polymer with 1,1-
		dichloroethene and 2-propenenitrile and
		isobutane is the blowing agent
Expancel 551WU80		Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
		propenoic acid methyl ester polymer with 1,1-
		dichloroethene and 2-propenenitrile and
		isobutane is the blowing agent
Expancel 642WU	(183F)	Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
		propenoic acid methyl ester polymer with 1,1-
		dichloroethene and 2-propenenitrile and
		isobutane is the blowing agent
Expancel 820DU	(167F)	Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
		propenoic acid methyl ester polymer with 1,1-
		dichloroethene and 2-propenenitrile and
		isobutane is the blowing agent
Expancel 820WU	(167F)	Blowing Agent (thermal): 2-methyl 2-	Expancel, Inc.
	propenoic acid methyl ester polymer with 1,1-
	dichloroethene and 2-propenenitrile and
	isobutane is the blowing agent
Heloxy 505	Epichlorohydrin Castor Oil Based Epoxy	Shell Chemical Co.
	Resin (aliphatic triglyceride triglycidyl ether)
SR 239	1,6 Hexanediol Dimethacrylate	Sartomer
SR 495	Caprolactone Acrylate	Sartomer
Vertrel XF	Blowing Agent: 2,3-Dihydroperfluoropentane	DuPont
	(Pentane,1,1,1,2,3,4,4,5,5,5-decafluoro:
	CF3CHFCHFCF2CF3)
Micropearls F30D	Blowing Agent (thermal): isobutane	HM Royal (Pierce &
	encapsulated in polymer vinylidene chloride	Stevens)
Ebecryl 170	Adhesion Promoter: Acrylate modified acidic	UCB Radcure
	adhesion promoting agent
Amicure CG1400	Dicyandiamide	Air Products
Glycolic Acid (70% Tech)	Technical grade (70%)	DuPont
H 3 PO 4 (>95% conc.)	concentrated grade via distillation of the 75%	DeNOVUS
	technical grade from Harcros Chemical
HQ54	merchant grade (73%)	PCS
Amberphos-54 (AMMGA)	merchant grade (75%)	PCS
H 3 PO 4 (85% Reagent)	reagent grade (85%)	Fischer Scientific
H 3 PO 4 (75% technical)	technical grade (75%)	Harcros Chemicals
H 3 PO 4 (85% technical)	technical grade (85%)	FMC/Harcros
		Chemicals
BTL 71001	Elastomer: EVA powder	BTLSR Toledo
MU 760-00	Elastomer: EVA powder: MI = 23: MP = 187 F:	Equistar
	VA = 19: Particle Size = 35 mesh
Microthene FA 700-00	Elastomer: HDPE powder: MI = 10.5:	Millennium
	MP = 273 F: Particle Size = 20 microns
Microthene FN 514-00	Elastomer: LDPE powder: MI = 70: MP = 216 F:	Millennium
	Particle Size = 20 microns
Microthene FP 800-00	Elastomer: Polypropylene powder: MP = 325 F:	Equistar
	Particle Size = 20 microns
LIR 403	Elastomer: Rubber: (polyisoprene liquid	Kuraray Co
	rubber)
Kraton D1107	Elastomer: SIS rubber pellets	Shell Chemical Co
Q325	Calcium carbonate	JM Huber Corp
Quikrete	Concrete mix	Quikrete Co.
Dicaperl CS-10-200	Hollow ceramic spheres	Grefco Inc
Qcel 650-D	Inorganic microspheres	PQ Corporation
SynPro Li Stearate	Li stearate	Ferro
A-C 6702	Oxidized polyethylene	Allied Signal
Airvol 203S	Polyvinyl Alcohol (PVOH)	Air Products
G	Sodium silicate	PQ Corporation
BTL 74001	Versatic acid ester/polyvinyl acetate ester	BTLSR Toledo
AZO 77	Zinc oxide	Morton Meyer
Isopropyl Alcohol (70%)	Alcohol	Commercial
Ethanol	Alcohol: Pure Grain Alcohol	Commercial
Ircosperse 2174	Dispersant	Lubrizol
Carbopol EZ-1	Emulsion Thickener	BF Goodrich
#1 Castor Oil	Oil	Acme-Hardesty
Lucant HC-2000	Oil: Hydrocarbon based synthetic oil	Mitsui Chemical
Vasoline	Petroleum Jelly	Chesebrough-
		Ponds
Indopol L100	Polybutene	Amoco
Unifilm 100HSM	Rheology Control Agent	Troy Chemical
Z6040	Silane	Dow Corning
Z6124	Silane: Arylalkoxy silane	Dow Corning
Dish Soap	Soap	Commercial
Boraxo	Soap: Sedium tetraborax decahydrate	Dial Corp
Triton X45	Surfactant	Union Carbide
Texaphor Special	Surfactant: Anionic Surfactant	Henkel
KRTTS	Titanate	Kenrich
Santolink XI-100	Allyl glycidyl ether alcohol resin	Solutia/Monsanto
SB 400	Aromatic acid methacrylate-mixed half ester	Sartomer
Pliolite AC	Copolymer: (styrene-acrylate: powder)	Goodyear
Pliolite S-5A	Copolymer: (styrene-butadiene: powder)	Goodyear
CMD 50859	Epoxy:	Shell Chemical Co
CMD 8750	Epoxy:	Shell Chemical Co
PEP 6180	Epoxy: (epoxy toughener: hydrogenated Bis	Pacific Epoxy
	A:)
PEP 6210 PA	Epoxy: (epoxy toughener: polyether adduct,	Pacific Epoxy
	epoxy functionality: EEW = 210: visc = 500 cps)
Erisys GE-60	Epoxy: (sorbitol glycidyl ether - aliphatic	CVC Specialty
	polyfunctional epoxy): liquid: EEW = 170:	Chemicals
	visc = 13,000 cps
Epalloy 5000	Epoxy: Bis A: (epoxidized hydrogenated Bis	CVC Specialty
	A resin): EEW = 220: visc = 1900 cps	Chemicals
DER 317	Epoxy: Bis A: liquid	Dow Chemical
DER 331	Epoxy: Bis A: liquid	Dow Chemical
DER 736	Epoxy: Bis A: liquid	Dow Chemical
Epon 828	Epoxy: Bis A: liquid	Shell
Uvacure 1500	Epoxy: cycloaliphatic	UCB Radcure
Uvacure 1502	Epoxy: cycloaliphatic	UCB Radcure
Uvacure 1533	Epoxy: cycloaliphatic	UCB Radcure
Cryacure UVR 6128	Epoxy: cycloaliphatic	Union Carbide
K126	Epoxy: cycloaliphatic: (cycloaliphatic	Sartomer
	diepoxide)
Eponex 1510	Epoxy: cycloaliphatic: (cycloaliphatic glycidyl	Shell Chemical Co
	ether): (hydrogenated DGEBPA)
Erisys GE-22	Epoxy: cycloaliphatic: (difunctional	CVC Specialty
	cycloaliphatic): (cyclohexanedimethanol	Chemicals
	diglycidyl ether): EEW = 155: visc = 60 cps
Uvacure 1534	Epoxy: cycloaliphatic: cycloaliphatic epoxy-	UCB Radcure
	polyol blend
Erisys GE-35	Epoxy: Glycidyl ether of castor oil	CVC Specialty
		Chemicals
Epon SU2.5	Epoxy: Novolac	Shell
Epalloy 8240	Epoxy: Novolac: (epoxidized phenol novolac:	CVC Specialty
	liquid): EEW = 170: visc = 6550 cps: fnc = 2.35	Chemicals
Epon 58005	Epoxy: rubber modified: (40% CTBN)	BF Goodrich
Erisys EMRM-22	Epoxy: rubber modified: (CTBN modified	CVC Specialty
	epoxy)	Chemicals
Tone EC	Monomer: Lactone: 2-oxepanone (6-	Union Carbide
	hydroxyhexanoic acid-e-lactone)
Santicizer 261	Plasticizer: Alkyl Benzyl Phthalate	Solutia
Santicizer 278	Plasticizer: Alkyl Benzyl Phthalate	Solutia
Santicizer 160	Plasticizer: Butyl Benzyl Phthalate	Solutia
Santicizer 97	Plasticizer: Dialkyl Adipate	Solutia
Santicizer 141	Plasticizer: Flame Retardant: 2-ethyl	Solutia
	Diphenyl Phosphate
CAPA 316	Polyol	Solvay Interox Ltd
Tone 0201	Polyol: (caprolactone-based polyol: diol):	Union Carbide
	Hydroxyl # = 212:
Tone 0301	Polyol: (caprolactone-based polyol: triol):	Union Carbide
	Hydroxyl # = 560: visc-225 @ 55 C
Arcol E-351	Polyol: (polyether polyol: capped diol):	Arco Chemical Co
	Hydroxyl # = 40: visc = 507 Cp
Arcol DP-1022	Polyol: (polyether polyol: diol): Hydroxyl	Arco Chemical Co
	# = 1200: visc = 175 cP
PPG-425	Polyol: (polyether polyol: diol): Hydroxyl	Arco Chemical Co
	# = 263: visc = 71 cps
Acclaim Polyol 4220	Polyol: (polyether polyol: monol diol):	Arco Chemical Co
Acclaim Polyol 6300	Polyol: (polyether polyol: monol triol):	Arco Chemical Co
	Hydroxyl # = 28: visc = 1452 cP: fnc = 2.94: acid
	value = 0.01
Arcol LG-650	Polyol: (polyether polyol: triol): Hydroxyl	Arco Chemical Co
	# = 650: visc = 1059 cP
Ebecryl 81	Polyol: Modified polyester polyol	Radcure
K-Flex 188	Polyol: Polyester Polyol:	King Industries
Desmophen L-951	Polyol: Short chained polyol: Hydroxyl # = 265	Bayer
Hycar 1300x40	Rubber	BF Goodrich
Hycar 1300X13	Rubber: (CTBN acrylonitrile liquid rubber)	BF Goodrich
Nipol 1312	Rubber: (liquid nitrile rubber)	Zeon Chemical
CN 301	Rubber: (methacrylated polybutadiene)	Sartomer
R45HT	Rubber: (PBD hydroxyl terminated)	Elf Atochem
Actipol E-16	Rubber: Activated polybutene: (Epoxidized	Amoco
	polybutene): Liquid
Trilene M-101	Rubber: Epoxidized EPDM	Uniroyal
PBD 605	Rubber: Hydroxyl terminated PBD	Elf Atochem
Kraton L-2203	Rubber: Hydroxyl terminated poly	Shell Chemical Co
	(ethylene/butylene) polymer: Diol
Ricon 100	Rubber: Styrene PBD: Liquid	Ricon Resins
Ricon 184	Rubber: Styrene PBD: Liquid	Ricon Resins
SAT 010	Silyl	Kaneka
SAT 030	Silyl	Kaneka
SAT 200	Silyl	Kaneka
Vertrel XF	2,3-Dyhydroperfluoropentane (Pentane,	DuPont
	1,1,1,2,3,4,4,5,5,5-decafluoro:
	CF3CHFCJFCF2CF3)
Micropearls F30D	Thermal Blowing Agent: isobutane	HM Royal (Pierce &
	encapsulated in polymer vinylidene chloride	Stevens)

The following terms and definitions are referenced in Examples 18-22.

Tin Ointment Can: Dimensions 2.75″ d×1.92″ h

Initial Rxn Time: Time that initial expansion is observed (includes mix time, does not include time to pour part A into part B

Final Rxn Time: Time for reaction to go to completion (includes “Initial Rxn Time”)

Rxn Temp: The peak temperature observed during the reaction

% Ht Expansion: % HE=[(h f −h i )/h i ]×100

Density: Weight of 1 in 3 block of expanded material (g/in 3 )

H 2 O Absorption 1: 100×(W 3 −W 2 )/(W 2 −W C ): W C =weight of aluminum coupon only W 2 =weight of coupon+material before submerging in water W 3 =weight of coupon+material after submerging in water: Mix material, apply to a 3″×3″ aluminum coupon, allow to cool to room temperature, submerge in water for 24 hrs, wipe off excess and immediately calculate water absorption.

H 2 O Absorption 2: Take a 1.5 inner diameter×h Polyvinyl chloride (PVC) pipe: use Daubert #2-76GSM paper as the release liner inside the PVC pipe (use some means to cap the bottom so that material does not exude out): mix part A & B and pour into the pipe and allow to expand and cure: cool to room temperature: cut 1.5″ lengths so that the sample size is ≈1.5″d×1.5″h: sand the edges: submerge in water for 24 hrs: remove the sample, wipe off excess water and immediately calculate % water absorption. % Water Absorption=100×(W F −W 1 )/W 1

H 2 O Absorption 3: “Open Chunk”: Mix part A & B in a polystyrene plastic cup: allow to expand and cure: cool to room temperature: Cut a “chunk” of foam from the top surface: submerge in water for 24 hrs: remove the sample, wipe off excess water and immediately calculate % water absorption: % Water Absorption=100×(W F W 1 )/W 1

Hardness: Shore A: The foam surface may be irregular: Take highest instantaneous reading from top surface after conditioning at room temperature for 4 hrs minimum

Shrinkage: Rating: 0=none 1=<1 mm from edge 2=1-2 mm from edge 3=2-3 mm from edge 4=3-4 mm from edge 5=4-5 mm from edge 6=5-6 mm from edge (shrinkage is usually not symmetrical: take the largest gap and divide by 2 if it did not shrink equally from the outer perimeter. Other values listed will be visually results: Rating 1=very slight, Rating 2=noticeable, Rating 3 & 4=significant, Rating 5 & 6=very significant

EXAMPLE18

Components	SAMPLE NO
Wt. %	1	2	3	4	5	6	7	8	9
Part A
Uvacure 1500	30	30	30	30	30	30	20	30	30
Microthene	10	10	10	10		10	10	10
FP800-00
Airvol 203 S	10	10	10	10	10	10	10	10	10
(PVOH)
Dicaperl CS-					10
10-200
Hycar 1300x13						10
PEP 6180							10	5
Part B
Tone 0301	29.65	29.65	29.65	29.65	29.65	29.65	29.65	29.65	29.65
(Polyol)
Micropearls	14.85	10	12	16	14.85	14.85	14.85	14.85	14.85
F30D
H 3 PO 4	5.5	5.5	5.5	5.5	5.5	5.5	5.5	5.5	5.5
(Reagent: 85%)
Rxn Time	59 sec	57 sec	56	57 sec	53 sec	65 sec	64 sec	58 sec	61 sec
Rxn Temp	288 F.	291 F.	289 F.	265 F.	292 F.	265 F.	238 F.	289 F.	270 F.
% Vertical	487%	413%	434%	468%	482%	385%	205%	404%	528%
Expansion
Hardness -	20	19	20	21	17	22	23	26	18
Shore A
Shrinkage	None	None	None	None	Very Slight	Noticeable	Noticeable	Very Slight	Very Slight
Components	SAMPLE NO
Wt. %	10	11	12	13	14	15	16	17	18
Part A
Uvacure 1500	30	30	20	30	30	30	30	30	15
Microthene			10	10					10
FP800-00
Airvol 203 S	20	10	10	10	10	10	10	10	10
(PVOH)
Microthene		10			10
FN514-00
DER 317			10
Microthene					10
FA700-00
Equistar MU						10
76000
AC 6702							10
BTL 71001								10
Cryacure UVR									15
6128
Part B
Tone 0301	29.65	29.65	29.65	20	29.65	29.65	29.65	29.65	29.65
(Polyol)
Micropearls	14.85	14.85	14.85	14.85	14.85	14.85	14.85	14.85	14.85
F30D
H 3 PO 4	5.5	5.5	5.5	5.5	5.5	5.5	5.5	5.5	5.5
(Reagent: 85%)
CN 301				9.65
Rxn Time	55 sec	50 sec	56	40 sec	51 sec	55 sec	50 sec	49 sec	56 sec
Rxn Temp	276 F.	274 F.	242 F.	268 F.	277 F.	271 F.	280 F.	292 F.	259 F.
% Vertical	494%	396%	226%	361%	388%	406%	415%	519%	326%
Expansion
Hardness -	16	23	22	42	22	19		19	15
Shore A
Shrinkage	None	Very Slight	Very Slight	Very Slight	Very Slight	Very Slight	Very Slight	None	Very Slight
Components	SAMPLE NO
Wt. %	19	20	21	22	23	24	25	26	27
Part A
Uvacure 1500	30	30	30	30	30	30	20	30	30
Microthene	10	10	10	10	10	10	10	10
FP800-00
Airvol 203 S	10		10	10	10	10	10	10	10
(PVOH)
Quickrete		20
Concrete Mix
DER 331					10
Epalloy 8240							10
Q325									10
Part B
Tone 0301	29.65	29.65	29.65	29.65	29.65		29.65	29.65	29.65
(Polyol)
Micropearls		14.85			14.85	14.85	14.85		14.85
F30D
H 3 PO 4	8	5.5	5.5	5.5	5.5	5.5	5.5	5.5	5.5
(Reagent: 85%)
Acclaim 6300						29.65
Expancel	14.85
091DU80
Expancel			14.85	14.85
642WU
Expancel								7.5
051DU
Rxn Time		52 sec	55 sec	52 sec	54 sec	46 sec	55 sec	72 sec	50 sec
Rxn Temp	298 F.	282 F.	289 F.	285 F.	270 F.		278 F.	323 F.	274 F.
% Vertical	183%	282%	460%	450%	378%	206%	388%	219%	570%
Expansion
Hardness -	75	18	10	12	43	23	39	53	21
Shore A
Shrinkage	None	Very Slight	Very Slight	None	Noticeable	None	Noticeable	Very Slight	Noticeable
Components	SAMPLE NO
Wt. %	28	29	30	31	32	33	34	35	36
Part A
Uvacure 1500		30	30	30	30	30	30	30	30
Microthene	10	10	10	10			10	10	10
FP800-00
Airvol 203 S	10	10	10	10	10	10	10	10	10
(PVOH)
Sartomer K126	30
Epon 58005			10
DER 736				10
Sodium					10
Silicate
Q Cel 650-D						10
Texaphor							4
Special
Blue Dish								2
Wish Soap
Part B
Tone 0301	29.65	29.65	29.65	29.65	29.65	29.65	29.65	29.65
(Polyol)
Micropearls	14.85		14.85	14.85	14.85	14.85	14.85	14.85	14.85
F30D
H 3 PO 4	5.5	5.5	5.5	5.5	5.5	5.5	5.5	5.5	5.5
(Reagent: 85%)
Expancel		14.85
820DU
E-351 Polyol									29.65
Rxn Time	50 sec	50 sec	54 sec	61 sec	58 sec	49 sec	68 sec	71 sec	40 sec
Rxn Temp	285 F.	296 F.	273%	271 F.		294 F.		281 F.	295 F.
% Vertical	483%	410%	396%	374%	410%	445%	530%	502%	302%
Expansion
Hardness -	20	32	34	30	10	18	13	23	38
Shore A
Shrinkage	None	Noticeable	Noticeable	Significant	Significant	None	Very Slight	None	None
Components	SAMPLE NO
Wt. %	37	38	39	40	41	42	43	44	45
Part A
Uvacure 1500	30	30	30	30	30		30	30	25
Microthene	10	10	10	10	10	10	10	10	10
FP800-00
Airvol 203 S	10	10	10		10	10	10	10	10
(PVOH)
Shell CMD			5
50809
Z6124				2
Uvacure 1502						30
Expancel								14.85
461DU
Epon 1510									5
Part B
Tone 0301			29.65	29.65	29.65	29.65	14.65	29.65	29.65
(Polyol)
Micropearls	14.85	14.85	14.85	14.85	14.85	14.85	14.85		14.85
F30D
H 3 PO 4	5.5	5.5	5.5	5.5	5.5	5.5
(Reagent: 85%)
Sartomer SB	29.65
400
LIR 403		14.65
Santolink XI-		15					15
100
75% Isopropyl					9.65
Alcohol
Amberphos-54							6.5	6.5	6.5
Rxn Time	37 sec	32 sec	55 sec			67 sec	45 sec	51 sec	82 sec
Rxn Temp	292 F.		305 F.			282 F.		291 F.
% Vertical	345%	188%	462%	561%	638%	450%	440%	340%	334%
Expansion
Hardness -	39	45	32	15	3	25	43	35	43
Shore A
Shrinkage	Noticeable	None	Very Slight	None	Very Slight	None	Very Slight	None	Noticeable
	Components	SAMPLE NO
	Wt. %	46	47	48	49
	Part A
	Uvacure 1500	30	30	30	30
	Microthene FP800-00	10	10
	Airvol 203 S (PVOH)	10	10
	Erisys GE-60		10
	SAT 200 (silyl)			20
	Kraton D1107				5
	Part B
	Tone 0301 (Polyol)	20
	Micropearls F30D	14.85	14.85	14.85	14.85
	Amberphos-54	6.5
	#1 Castor Oil	9.65
	Arcol LG-650		29.65
	HQ54 (73% H 3 PO 4 )		6.5	6.5
	Arcol DP-1022			29.65	29.65
	H 3 PO 4 (75% technical grade)				6.5
	Rxn Time	47 sec	110 sec	101 sec	83 sec
	Rxn Temp	287 F.		289 F.
	% Vertical Expansion	364%	350%	458%	620%
	Hardness - Shore A	32	25	9	7
	Shrinkage	Very Slight	Very slight	Noticeable	Significant

EXAMPLE 19

Components wt. %	Sample No. 1	Sample No. 2	Sample No. 3	Sample No. 4
Part A
Uvacure 1500	30	30	30	30
Microthene FP800-00	10	10	10	10
Airvol 203 S (PVOH)	10	10	10	10
Part B
Tone 0301 (Polyol)
Micropearls F30D	14.85	14.85	14.85	14.85
Amberphos-54 (AMMGA)	6.5	6.5	6.5	6.5
Tone 0201	14.65	20	9.65
Santolink XI-100	15	9.65	20
Arcol DP-1022				29.65
Initial Rxn Time	27 sec	24 sec	—	63 sec
Initial Rxn Temp	204 F.	—	—	201 F.
Rxn Time	42 sec	35 sec	—	99 sec
Rxn Temp	—	—	—	—
% Vertical Expansion	293%	277%	249%	550%
Hardness - Shore A	55	59	53	4
Shrinkage	Significant	Significant	Noticeable shrinkage	Noticeable
	(>2 mm < 4 mm from	(>2 mm < 4 mm from	(>1 mm < 2 mm from	shrinkage
	edge of tin cup) after	edge of tin cup) after	edge of tin cup) after	(>1 mm < 2 mm
	cooling to RT	cooling to RT	cooling to RT	from edge of tin
				cup) after cooling
				to RT

EXAMPLE 20

Component wt %	Sample No. 1	Sample No. 2	Sample No. 3	Sample No. 4	Sample No. 5	Sample No. 6
Part A
Uvacure 1500	30	30	30	30	40	34.46
Nipol 1312			15	15
Lucant HC-2000	15
Carbopol EZ-1		5
Microthene FP800-00		10
Microthene FN-514-00					20	12.75
Kraton D1107						3.79
Part B
Arcol PPG-425	20		15	10	20
Micropearls F30D	14.85		14.85	14.85	14.85	14.85
75% H 3 PO 4 (tech)	6.5		6.5	6.5	6.5	6.5
Jeff P. Control Part B		50
Arcol DP-1022			5	10
Tone 0301						14.65
Santolink XI-100						15
Initial Rxn Time	40 sec	34 sec	51 sec	50 sec	51 sec	29 sec 31 sec
Final Rxn Time	50 sec	52 sec	65 sec	65 sec	73 sec	70 sec 65 sec
% Ht Expansion	390%	423%	387%	310%	292%	374%
Water Absorption	81% 75%	31% 33%	73% 98%	46% 58%	19% 28%	18% (matl chunk)
Shore A Hardness	27	28	32	33	62	38
Shrinkage	0	0	≈5.5 mm	≈7 mm	2 mm	2 mm
Component wt %	Sample No. 7	Sample No. 8	Sample No. 9	Sample No. 10	Sample No. 11	Sample No. 12
Part A
Uvacure 1500	30.4	34.46	34.46	50.7	50.7	27.9
Kraton D1107	3.34	3.79	3.79	5.6	5.6	3.1
Microthene FN514-00	11.26	12.75	12.75	18.8	18.8	10.3
Part B
Tone 0301	14.65
Santolink XI-100	15
Micropearls F30D	14.85	14.85	11.6	14.85	14.85	14.85
75% H 3 PO 4 (tech)	6.5	6.5	5.1	6.5	12.5	6.5
Arcol PPG-425						20
Arcol DP-1022		29.65	23.3	29.65	29.65
Initial Rxn Time		83 sec	96 sec	101 sec	28 sec	41 sec
Final Rxn Time		107 sec	132 sec	136 sec	42 sec	58 sec
% Ht Expansion	432%	398%	368%	252%	313%	402%
Density (g/in 3 )
Water Absorption
Shore A Hardness	36	13	18	28	24	46
Shrinkage	1 mm	1 mm	3 mm	5 mm	1 mm	0.5 mm
Component wt %	Sample No. 13	Sample No. 14	Sample No. 15	Sample No. 16	Sample No. 17	Sample No. 18
Part A
Uvacure 1500	40.5	40.5	40.5	46.29	46.29	40
Microthene FN-514-00	4.5	4.5	4.5	8.57	8.57
Kraton D1107	15	15	15	5.14	5.14
Nipol 1312						15
Part B
Arcol PPG-425	20	20	20	20	20	20
Micropearls F30D	14.85	24.85	24.85	24.85	24.85	24.85
75% H 3 PO 4 (tech)	6.5	8.5	8.5	8.5	8.5	8.5
Glycolic Acid (70% tech)			6		6
Initial Rxn Time	46 sec	34 sec	33 sec	27 sec	27 sec	32 sec
Final Rxn Time	58 sec	48 sec	49 sec	40 sec	39 sec	46 sec
% Ht Expansion	317%	377%	480%	405%	395%	508%
Density (g/in 3 )			1.99
Water Absorption		115% 142%	116% 174%	59% 131%	443% 409%	131% 160%
Shore A Hardness	63	42	13	29	13	25
Shrinkage	4 mm	0.5 mm	0.5 mm	1.5 mm	1 mm	1 mm
Component wt %	Sample No. 19	Sample No. 20	Sample No. 21	Sample No. 22	Sample No. 23	Sample No. 24
Part A
Uvacure 1500	40	40	40	40	40	35
Microthene FN-514-00
Kraton D1107
Nipol 1312	15	15	15	15	15	15
Carbopol EZ-1		5	5
Epon CMD 50859						5
Part B
Arcol PPG-425	20	20	20	20	20	20
Micropearls F30D	24.85	24.85	24.85	24.85	24.85	24.85
75% H 3 PO 4 (tech)	8.5	8.5	8.5	8.5	8.5	8.5
Glycolic Acid (70% tech)	6		3
#1 Castor Oil				8
Z6040					1
Initial Rxn Time	30 sec	30 sec	25 sec	33 sec	36 sec	37 sec
Final Rxn Time	42 sec	41 sec	39 sec	59 sec	57 sec	52 sec
% Ht Expansion	382%	402%	417%	421%	455%	432%
Density (g/in 3 )
Water Absorption		144% 133%	152% 162%	66% 55%	105% 108%	99% 129%
						(open chunk:
						137%)
Shore A Hardness	18	24	17	23	29	23
Shrinkage	3 mm	0 mm	1.5 mm	0 mm	0.5 mm	0 mm
Component wt %	Sample No. 25	Sample No. 26	Sample No. 27	Sample No. 28	Sample No. 29	Sample No. 30
Part A
Uvacure 1500	40	40	40	40	40	40
Microthene FN-514-00
Kraton D1107
Nipol 1312	15
SAT 030		15	15	15	15
CN 301						15
Part B
Arcol PPG-425		20	20	20	20	20
Micropearls F30D	24.85	24.85	24.85	24.85	24.85	24.85
75% H 3 PO 4 (tech)	8.5	8.5	8.5	8.5	8.5	8.5
Arcol Acclaim 6300	20
#1 Castor Oil			8	15		8
Tone EC Monomer					10
Initial Rxn Time	36 sec	38 sec	50 sec	61 sec	54 sec	42 sec
Final Rxn Time	—	56 sec	74 sec	95 sec	73 sec	60 sec
% Ht Expansion	150%	555%	492%	370%	467%	445%
Density (g/in 3 )			1.939
Water Absorption		67% 95%	48% 45%	44% 37%	50% 95%	62% 39%
		(open chunk:	(open chunk:		(open chunk:	(open chunk:
		260%)	49%)		75%)	143%)
Shore A Hardness		18	24	20	25	25
Shrinkage	1.5 mm	0 mm	0 mm	0.5 mm	3 mm	0 mm
Component wt %	Sample No. 31	Sample No. 32	Sample No. 33	Sample No. 34	Sample No. 35	Sample No. 36
Part A
Uvacure 1500	40	40	40	40	40
CN 301		15		15
Uvacure 1534						40
Part B
Arcol PPG-425	20		20	20	20	20
Micropearls F30D	24.85	24.85	24.85	24.85	24.85	24.85
75% H 3 PO 4 (tech)	8.5	8.5	8.5	8.5	8.5	8.5
#1 Castor Oil	8	8	8	8	8	8
CN 301	15		22		15	15
Ebecryl 81		20
Z6040				1.5
KR TTS					1.5
Initial Rxn Time	41 sec	88 sec	38 sec	39 sec	37 sec	163 sec
Final Rxn Time	59 sec	120 sec	55 sec	—	54 sec	265+ sec
% Ht Expansion	461%	153%	386%	479%	433%
Density (g/in 3 )
Water Absorption	99% 66%		37% 45%	45% 34%	294% 243%
	(open chunk:		(open chunk:	(open chunk:	(open chunk:
	160%)		151%)	158%)	184%)
Shore A Hardness	22	72	22	22	22
Shrinkage	0 mm	1 mm	0 mm	0.5 mm	0 mm
Component wt %	Sample No. 37	Sample No. 38	Sample No. 39	Sample No. 40	Sample No. 41	Sample No. 42
Part A
Uvacure 1500	40	40	40	40	40	50.91
Ricon 100	15					19.09
SAT 030		25
Ricon 184			15	15
Expancel 461DU				10
Actipol E-16					15
Part B
Arcol PPG-425	20	20	20	20	20	20
Micropearls F30D	24.85	24.85	24.85	14.85	24.85	24.85
75% H 3 PO 4 (tech)	8.5	8.5	8.5	8.5	8.5	8.5
#1 Castor Oil	8	8	8	8	8	8
Initial Rxn Time	39 sec	66 sec	39 sec	31 sec	39 sec	43 sec
Final Rxn Time	64 sec	102 sec	63 sec	50 sec	68 sec	72 sec
% Ht Expansion	504%	348%	470%	345%	395%	432%
Density (g/in 3 )
Water Absorption	77% 79%	26% 43%	84% 93%	60% 63%	71% 90%	105% 72%
	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:
	119%)	121%)	108%)	166%)	101%)	186%)
Shore A Hardness	26	22	27	30	32	31
Shrinkage	0 mm	0 mm	0 mm	0 mm	0 mm	0.5 mm
Component wt %	Sample No. 43	Sample No. 44	Sample No. 45	Sample No. 46	Sample No. 47	Sample No. 48
Part A
Uvacure 1500	40	40	40	40	40	40
SAT 030	15		15	15	15	15
Kraton L-2203		15
Erisys GE-35						10
Part B
Arcol PPG-425	20	20	20			20
Micropearls F30D	24.85	24.85	24.85	24.85	24.85	24.85
75% H 3 PO 4 (tech)	8.5	8.5	8.5	8.5	8.5	8.5
#1 Castor Oil	8	8	8	8	8	8
CN 301	15
Santolink XI-100			10
Tone 0301				20	29.65
Initial Rxn Time	52 sec	39 sec	53 sec	31 sec	36 sec	48 sec
Final Rxn Time	84 sec	65 sec	83 sec	49 sec	53 sec	77 sec
% Ht Expansion	275%	431%	350%	480%	502%	395%
Density (g/in 3 )
Water Absorption	34% 36%	79% 61%	26% 40%	159% 220%	102% 102%	96% 75%
	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:
	119%)	62%)	117%)	212%)	205%)	135%)
Shore A Hardness	30	26	27	17	16	25
Shrinkage	0 mm	0 mm	0.5 mm	0 mm	0 mm	0 mm
Component wt %	Sample No. 49	Sample No. 50	Sample No. 51	Sample No. 52	Sample No. 53	Sample No. 54
Part A
Uvacure 1500	40	40	40	40	40	40
SAT 030	15	15	15	15	15	15
Erisys GE-35	10
Part B
Arcol PPG-425	20	20		20	20	20
Micropearls F30D	24.85	24.85	24.85	24.85	24.85	24.85
75% H 3 PO 4 (tech)	12	8.5	8.5	8.5	8.5	8.5
#1 Castor Oil	8	8	8	8		8
Kraton L-2203		15
Tone 0201			20
Santicizer 261				10	15
Z6124						2
Z6040						1
Initial Rxn Time	29 sec	59 sec	27 sec	51 sec	53 sec	45 sec
Final Rxn Time	50 sec	118 sec	36 sec	67 sec	63 sec	78 sec
% Ht Expansion	410%	317%	422%	263%	225%	458%
Density (g/in 3 )	1.826
Water Absorption	74%	29% 44%	104% 138%	19% 22%	41% 54%	22% 24%
	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:
	53% & 64%)	86%)	133%)	75%)	137%)	180%)
Shore A Hardness	12	34	30	44	50	23
Shrinkage	0 mm	0.5 mm	2 mm	0 mm	0 mm	0.5 mm
Component wt %	Sample No. 55	Sample No. 56	Sample No. 57	Sample No. 58	Sample No. 59	Sample No. 60
Part A
Uvacure 1500	40	40	40	40	40	40
SAT 030				15
SAT 010	15
SAT 200		15
PBD 605			15		15	15
Part B
Arcol PPG-425	20	20	20	20	20	15
Micropearls F30D	24.85	24.85	24.85	24.85	24.85	24.85
75% H 3 PO 4 (tech)	8.5	8.5	8.5	8.5	8.5	8.5
#1 Castor Oil	8	8	8	8	8	8
Santicizer 261				5	5	10
Z6124				2	2	2
Z6040				1	1	1
Initial Rxn Time	58 sec	50 sec	40 sec	51 sec	40 sec	29 sec
Final Rxn Time	83 sec	76 sec	80 sec	85 sec	69 sec	39 sec
% Ht Expansion	444%	435%	536%	388%	433%	320%
Density (g/in 3 )
Water Absorption	44% 60%	96% 105%	25% 27%	65% 53%	32% 33%	115% 105%
	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:
	191%)	131%)	34%)	85%)	54%)	197%)
Shore A Hardness	25	20	24	22	23	19
Shrinkage	0 mm	0 mm	0 mm	0 mm	0.5 mm	0.5 mm
Component wt %	Sample No. 60	Sample No. 61	Sample No. 62	Sample No. 63	Sample No. 64	Sample No. 65
Part A
Uvacure 1500	40	40	40	40	40	40
PBD 605	15	20	25	15	15	15
Part B
Arcol PPG-425	20	20	20	20	25	20
Micropearls F30D	24.85	24.85	24.85	24.85	24.85	14.85
75% H 3 PO 4 (tech)	8.5	8.5	8.5	8.5	8.5	6.5
#1 Castor Oil	6	6	6	3	8
Santicizer 261	7	7	7	5
Z6124	2	2	2
Z6040	1	1	1
Initial Rxn Time	37 sec	43 sec	43 sec	42 sec	46 sec	48 sec 42 sec
Final Rxn Time	62 sec	74 sec	72 sec	71 sec	86 sec	77 sec 60 sec
% Ht Expansion	411%	357%	337%	493%	423%	475% 486%
Density (g/in 3 )						2.17
Water Absorption	28% 26%	17% 25%	56% 34%	43% 49%	29% 26%	17% 15%
	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:	(open chunk:
	119%)	126%)	121%)	134%)	71%)	14%)
Shore A Hardness	23	22	18	20	20	29 30
Shrinkage	0.5 mm	0.5 mm	0.5 mm	0.5 mm	0.5 mm	0.8 mm
	Component wt %	Sample No. 66	Sample No. 67	Sample No. 68
	Part A
	Uvacure 1500	40	40	40
	PBD 605	15	15	15
	Z6040			1
	Part B
	Arcol PPG-425	20	20	20
	Micropearls F30D	24.85	24.85	24.85
	75% H 3 PO 4 (tech)	8.5	8.5	8.5
	#1 Castor Oil	3	3	3
	Santicizer 261	7	7	7
	Z6124		2	2
	Initial Rxn Time	39 sec	38 sec	41 sec
	Final Rxn Time	65 sec	55 sec	56 sec
	% Ht Expansion	455%	403%	439%
	Density (g/in 3 )
	Water Absorption	57% 72%	131% 130%	107% 88%
		(open chunk =	(open chunk =	(open chunk =
		153%)	160%)	156%)
	Shore A Hardness	28	25	28
	Shrinkage	0.5 mm	0.5 mm	1 mm

EXAMPLE 21

Component wt %	Sample No. 1	Sample No. 2	Sample No. 3	Sample No. 4	Sample No. 5	Sample No. 6
Part A
Uvacure 1500	32.7	36.4	43.6	40	40	40
PBD 605	12.3	13.6	16.4	20	25	15
Part B
Arcol PPG-425	20	20	20	20	20	20
Micropearls F30D	14.85	14.85	14.85	14.85	14.85	14.85
75% H 3 PO 4 (tech)	6.5	6.5	6.5	6.5	6.5	6.5
Santicizer 160						4
Initial Rxn Time	47 sec	47 sec	50 sec	51 sec	54 sec	49 sec
Final Rxn Time	75 sec	70 sec	78 sec	—	104	67 sec
% Ht Expansion	564%	454%	430%	427%	387%	426%
Density (g/in 3 )
H 2 O Absorption 1
H 2 O Absorption 2
H 2 O Absorption 3	37%	31%	14%	28% 30%	42% 31%	74%
Shore A Hardness	28	31	32	33	33	38
Shrinkage	0 mm	0.3 mm	1.5 mm	0.8 mm	0.5 mm	3 mm
Component wt %	Sample No. 7	Sample No. 8	Sample No. 9	Sample No. 10	Sample No. 11	Sample No. 12
Part A
Uvacure 1500	40	40	40	40	40	40
PBD 605	15	15	15	10	15	15
Part B
Arcol PPG-425	20	20	20	20	20	20
Micropearls F30D	14.85	14.85	14.85	14.85	14.85	14.85
75% H 3 PO 4 (tech)	6.5	6.5	6.5	6.5	8	9.5
Santicizer 160	8
Santicizer 278		4	8
Initial Rxn Time	51 sec	54 sec	55 sec	42 sec	32 sec	27 sec
Final Rxn Time	71 sec	80 sec	83 sec	57 sec	—	38 sec
% Ht Expansion	332%	395%	338%	529%	567%	500%
Density (g/in 3 )
H 2 O Absorption 1		44% 23%	26% 26%	61% 90%	25% 33%	56% 65%
H 2 O Absorption 2
H 2 O Absorption 3	106%	63%	87%	126%	34%	92% 83%
Shore A Hardness	43	24	32	30	29	28
Shrinkage	4 mm	2 mm	2 mm	0 mm (had	0.5 mm (had	0.75 mm (had
				radial shrinkage)	radial shrinkage)	radial shrinkage)
Component wt %	Sample No. 13	Sample No. 14	Sample No. 15	Sample No. 16	Sample No. 17	Sample No. 18
Part A
Uvacure 1500	40	40	40	40	40	40
PBD 605	15	15	15	15	15	15
Epon SU2.5	10
Epon 828				5
Part B
Arcol PPG-425	20		29.98		20	20
Micropearls F30D	14.85	14.85	22.27	14.85	14.85	14.85
75% H 3 PO 4 (tech)	6.5	6.5	9.75	6.5	6.5
CAPA 316		20
Tone 0301				20
Dicy 1400				2	0.26
85% H 3 PO 4 (tech)						6.5
Initial Rxn Time	—	20 sec	50 sec	74 sec	49 sec	36 sec
Final Rxn Time	—	—	—	99 sec	70 sec	76 sec
% Ht Expansion	414%	430%	445%		451%	433%
Density (g/in 3 )
H 2 O Absorption 1			97% 106%			19% 14%
H 2 O Absorption 2
H 2 O Absorption 3	40% 56%	69% 65% 57%	128%			22% 13% 17%
Shore A Hardness	53	43	26		30	32
Shrinkage	3 mm	0 mm (had	2.8 mm	very significant	2.6 mm	0 mm
		radial shrinkage)
Component wt %	Sample No. 19	Sample No. 20	Sample No. 21	Sample No. 22	Sample No. 23	Sample No. 24
Part A
Uvacure 1500	40	40	35	35	35	40
PBD 605	15	15	15	15	15	15
Epon 828						10
Part B
Arcol PPG-425	20					20
Micropearls F30D	14.85	14.85	14.85	14.85	14.85	14.85
75% H 3 PO 4 (tech)	6.5	6.5	6.5	5	8	6.5
Ebecryl 170	5					15
Desmophen L-951		20	20	20	20
Initial Rxn Time	25 sec	44 sec 50 sec	48 sec 48 sec	72 sec	37 sec 34 sec	18 sec
Final Rxn Time	43 sec	64 sec 67 sec	79 sec 70 sec	100 sec	57 sec 51 sec	35 sec
% Ht Expansion	415%	467% 510%	505% 442%	420%	530% 535%	289%
Density (g/in 3 )	1.93	2.02
H 2 O Absorption 1	9% 15%	15% 18%	20% 22%		39% 19%
H 2 O Absorption 2					36%
H 2 O Absorption 3	39% 22%	32% 22% 37%	60% 49% 73%		66% 55% 61%	81% 48%
Shore A Hardness	35	38 31	29 32	31	30 27	52
Shrinkage	0.3 mm	1.5 mm 0.8 mm	0.5 mm 0.75 mm	3.3 mm	0.5 mm 0.75 mm	2 mm
Component wt %	Sample No. 25	Sample No. 26	Sample No. 27	Sample No. 28	Sample No. 29	Sample No. 30
Part A
Uvacure 1500	40	30	40	30	40	40
PBD 605	15		15	15	15	7.5
Epon 828				10
SAT 030						7.5
Part B
Arcol PPG-425						20
Micropearls F30D	14.85	14.85	14.85	14.85	14.85	14.85
75% H 3 PO 4 (tech)			6.5	6.5	6.5	6.5
Desmophen L-951	20		10	20
Ebecryl 170	20	30	5	5
Santicizer 261			10
K-Flex 188					20
Initial Rxn Time		<10 sec	21 sec	25 sec	27 sec	48 sec
Final Rxn Time			36 sec	41 sec	—	61 sec
% Ht Expansion		350%	358%	333%	456%
Density (g/in 3 )				3.45
H 2 O Absorption 1				28% 38%
H 2 O Absorption 2				89%
H 2 O Absorption 3			94% 95%	84% 83% 85%	32% 28% 30%	19% 22%
Shore A Hardness			39	37	47
Shrinkage		0.5 mm	2.5 mm	2.5 mm	0.9 mm
Component wt %	Sample No. 31	Sample No. 32	Sample No. 33	Sample No. 34	Sample No. 35	Sample No. 36
Part A
Uvacure 1500	40	40	40	40	40	20
PBD 605	7.5		15	15		15
Epon 828
SAT 030	7.5
Trilene M-101		15
Hycar 1300x40					15
Uvacure 1533						20
Part B
Arcol PPG-425	20	20	20	20	20	20
Micropearls F30D	14.85	14.85	14.85	14.85	14.85	14.85
75% H 3 PO 4 (tech)	6.5	6.5	6.5	6.5	6.5	6.5
Ebecryl 170	2
#1 Castor Oil			6
Santicizer 141				10
Initial Rxn Time	31 sec	46 sec	49 sec	56 sec	45 sec	47 sec
Final Rxn Time	49 sec	60 sec	68 sec	71 sec	55 sec	78 sec
% Ht Expansion		394%
Density (g/in 3 )
H 2 O Absorption 1
H 2 O Absorption 2
H 2 O Absorption 3	22% 23%	114% 81% 107%	17% 15%	51% 70%		30% 34%
Shore A Hardness		40
Shrinkage		2.75 mm
Component wt %	Sample No. 37	Sample No. 38	Sample No. 39	Sample No. 40	Sample No. 41	Sample No. 42
Part A
Uvacure 1500	25	40	40	40
PBD 605	15	15	15	15
Epon 828					45	45
Uvacure 1534	15
Part B
Arcol PPG-425	20	20	20	20
Micropearls F30D	14.85	14.85	14.85	14.85	15	15
75% H 3 PO 4 (tech)	6.5
H 3 PO 4 (conc: >95%)		6.5	4.9	4	10	10
Tone EC Monomer					20
#1 Castor Oil						20
Initial Rxn Time	58 sec	28 sec	33 sec	37 sec	58 sec	33 sec
Final Rxn Time	73 sec	37 sec	52 sec	50 sec	93 sec	—
% Ht Expansion		274%	261%	181%	510%	300%
Density (g/in 3 )					1.8
H 2 O Absorption 1
H 2 O Absorption 2
H 2 O Absorption 3	27% 33%		15% 20%		37% 38%
			(72 hrs)		(72 hrs)
Shore A Hardness		62	60	62	48	68
Shrinkage					0 mm	0 mm
	Component wt %	Sample No. 43	Sample No. 44	Sample No. 45	Sample No. 46
	Part A
	Epon 828	45	45	50	50
	Vertrel XF				5
	Part B
	Micropearls F30D	15	15	15	10
	H 3 PO 4 (conc: >95%)	10	20	10	10
	Santicizer 261	20
	Pure Grain Alcohol		20
	(EtOH)
	Santicizer 97			20	20
	Initial Rxn Time	24 sec	108 sec	27 sec	26 sec
	Final Rxn Time	72 sec	130 sec	—	—
	% Ht Expansion	182%	575%	376%	297%
	Density (g/in 3 )		1.37
	H 2 O Absorption 1
	H 2 O Absorption 2
	H 2 O Absorption 3		843%
			(after 15 mins)
	Shore A Hardness	78	4		62
	Shrinkage	0.5 mm	0.5 mm		0 mm

EXAMPLE 22

Component wt %	Sample No. 1	Sample No. 2	Sample No. 3	Sample No. 4	Sample No. 5	Sample No. 6
Part A
Uvacure 1500	40
PBD 605	15
Epon 828		40	40	35	35	50
Santicizer 97				5	5
Part B
Desmophen L-951	20
H 3 PO 4 (75% tech)	6.5
Micropearls F30D	2	10	10	10	10	10
H 3 PO 4 (>95% conc)		10	10	10	10	10
Arcol PPG-425		20
Santicizer 97			20	20	15	20
#1 Castor Oil					5
Initial Rxn Time	43 sec	263 sec	20 sec	19 sec	24 sec	25 sec
Final Rxn Time	54 sec	299 sec	—	—	—	—
% Ht Expansion	86%	308%	189%	118%	122%	184%
Density (g/in 3 )		2.50	6.20		6.93	6.13
H 2 O Absorption 1	3%
H 2 O Absorption 2
H 2 O Absorption 3	3%	27% 23%	8% 10%	18% 22% 18%	11% 12%	5% 6%
Shore A Hardness			88	90	88	88
Shore D Hardness	(32)		27 (30)	30 (32)	27 (30)	28 (30)
(##) = calculated
Shrinkage	2.2 mm	0 mm	0 mm	0 mm	0 mm	0 mm
Component wt %	Sample No. 7	Sample No. 8	Sample No. 9	Sample No. 10	Sample No. 11	Sample No. 12
Part A
Epon 828	40	20	40	40	40	60
CMD 50859		20
Tone EC					2	3
Part B
Santicizer 97		20	20	15	15	15
H 3 PO 4 (>95% conc)	10	10	10	10	10	10
Micropearls F30D	10	10	6	6	4	4
Santicizer 160	20
#1 Castor Oil				5	5	5
Initial Rxn Time	17 sec	22 sec	18 sec	22 sec	22 sec	30 sec
Final Rxn Time	—	—	—	—	—	—
% Ht Expansion	260%	152%	120%	145%	99%	92%
Density (g/in 3 )		4.20	7.03	6.40	6.94	8.19
H 2 O Absorption 1
H 2 O Absorption 2
H 2 O Absorption 3	40% 32% 39%	50% 34%	13% 12%	13% 11%	15% 10%	3% 2%
Shore A Hardness		80	91	86	93	98
Shore D Hardness		23 (22)	32 (33)	26 (28)	34 (36)	46 (42)
(##) = calculated
Shrinkage	0 mm	0 mm	0 mm	0 mm	0 mm	0 mm
Component wt %	Sample No. 13	Sample No. 14	Sample No. 15	Sample No. 16	Sample No. 17	Sample No. 18
Part A
Epon 828	40	60	80	80	50	50
Santicizer 97	5	7.5	10	10
Vertrel XF				5	10
Part B
Santicizer 97	15	15	15	15	20	20
H 3 PO 4 (>95% conc)	10	10	10	10	10	10
Micropearls F30D	6	6	6	6	5	10
#1 Castor Oil	10	10	10	10		10
Initial Rxn Time	—	—	69 sec	66 sec	24 sec	41 sec
Final Rxn Time	—	—	—	—	—	—
% Ht Expansion	—	—	60%	61%	238%	123%
Density (g/in 3 )	—	—	—	—	—	4.64-8.38
H 2 O Absorption 1	—	—	—	—	—	—
H 2 O Absorption 2	—	—	—	—	—	—
H 2 O Absorption 3	14%	8% 8%	1% 1%	—	—	32% 35%
Shore A Hardness	—	—	—	90	—	90
Shore D Hardness	—	—	—	(32)	—	29 (32)
(##) = calculated
Shrinkage	—	—	0 mm	0 mm	0 mm	0 mm
	Component wt %	Sample No. 19
	Part A
	Epon 828	65
	Santicizer 97	5
	Part B
	Santicizer 97	15
	H 3 PO 4 (>95% conc)	10
	Micropearls F30D	10
	Initial Rxn Time	25 sec
	Final Rxn Time	—
	% Ht Expansion	176%
	Density (g/in 3 )	6.55
	H 2 O Absorption 1
	H 2 O Absorption 2
	H 2 O Absorption 3	4% 4%
		(after 48 hrs)
	Shore A Hardness	93
	Shore D Hardness	(36)
	(## = calculated)
	Shrinkage	0 mm

EXAMPLE 23

This Example illustrates the ability to tailor the inventive foam compositions and obtain foams having a wide range of characteristics. A foam of relatively low density was produced by in accordance with Example 18. The foam was obtained by combining the following foam precursors:

AMOUNT	COMPONENT	TRADE NAME	SUPPLIER
Part A:
18.2	g	cylcoaliphatic	Uvacure 1500	Radcure
		epoxy
1.8	g	phenoxy resin	Phenoxy PKHP-200	Paphen
30	g	bis-A epoxy	D.E.R. 736	Dow Chemical
Part B:
29.65	g.	caprolactone	Tone 0301	Union Carbide
		polyol
14.85	g.	vinylidene	Micropearls F30D	Pierce & Stevens
		chloride
		encapsulated
		iso-butane
5.5	g.	phosphoric		ACROS
		Acid (85%)

Each component (Part A & B) was individually mixed by hand using a hand driven paddle in a cup or ointment can. The two were brought together in a single vessel, again mixed by hand, and allowed to react. The foam produced was similar in appearance to other types listed above, but had a final specific gravity 0.16 g/ml.

EXAMPLE 24

The following Example demonstrates employing the inventive foam as a structural material between two laminates to fabricate furniture. The components listed in the following Table were combined in accordance with Examples 18-22.

			Sample	Sample
Components wt. %	Sample No. 1	Sample No. 2	No. 3	No. 4
Part A
Epon 828	75		—	—		50
Santicizer 97	5		—	—		—
Epon 813	—		50	—		—
Epon 825	—		—	50		—
Part B
Santicizer 97	20		20	20		23
H 3 PO 4 (>95% conc)	10		10	10		10
Micropearls F30D	10		10	10		10
Initial Rxn Time	40	sec	33 sec	28	sec	28	sec
Final Rxn Time	—		—	—		—
% Ht Expansion	136%		262%	225%		170%
Density 1 (g/in 3 )	—		—	—		—
Density 2 (g/in 3 )	8.77		—	5.70		5.52
H 2 O Absorption 1	1% 1%	2%	—	—		—
H 2 O Absorption 2	—		—	—		—
Shore A Hardness	95		—	—		81
Shore D Hardness	40		—	—
(##) = calculated	(38)					(23)
Shrinkage	0	mm	0 mm	0	mm	0	mm
			Had significant
			radial
			shrinkage

The following Table lists components employed in the above Table for making foam.

Trade Name	Component	Supplier
#1 Castor Oil	#1 Castor Oil	Commercial
Epon 825	Bis A Epoxy	Shell Chemical Co.
Epon 828	Bis A Epoxy	Shell Chemical Co.
Epon 813	Bis A Epoxy Modified: (74% Bis-	Shell Chemical Co.
	phenol A epichlorohydrin resin &
	26% Cresyl glycidyl ether)
Santicizer 97	Dialkyl Adipate	Solutia
H 3 PO 4	Phosphoric acid: Took Harcros	DeNOVUS
(>95% conc)	75% Technical Grade & distilled
	to > 90% acid concentration
Micropearls	Therma Blowing Agent: isobutane	HM Royal (Pierce
F30D	encapsulated in polymer vinylidene	& Stevens)
	chloride

Sample No. 1 above was combined and introduced into a mold comprising standard 1″×4″×12″ boards and laminating materials comprising wood-grain Formica® and fiber-reinforced paper board that were maintained a defined distance about by wood spacers, i.e., a distance of about ½ inch. The boards and laminating materials were placed into “C” clamps and a vise. The foam composition was prepared and poured between the laminating materials. Once the foam reaction was completed and the foam had cooled to room temperature, the assembly was visually inspected. The foam had adhered to the laminating materials and provided structural support.

EXAMPLE 25

Component	Sample No.	Sample No.	Sample No.	Sample No.	Sample No.	Sample No.
Wt. %	1	2	3	4	5	6
Part A
Epon 828	48	23	50	34.5	50	50
Santicizer 97	2
Epon 825		23		9.5
Part B
Santicizer 97	19.8	20	20	18
H 3 PO 4 (>95%	11	10	10	10	10	10
conc)
Micropearls F30D	13.7	12.5	2	12.5	12.5	12.5
Expancel 642DU			2
Expancel 820DU			2
Expancel 551DU			2
Expancel 461DU			2
SR 239					20
SR 495						20
Initial Rxn Time	28 sec 26	38 sec	38 sec	28 sec 34	41 sec	79 sec
	sec			sec
% Ht Expansion	289%	320%	240%	306% 275%	269%	399%
Density 1 (g/in 3 )		2.41-2.75
Density 2 (g/in 3 )	3.35
H 2 O Absorption 1	16% 20%	13% 13%
Shore A	50	63
Hardness
Shrinkage	0 mm	0 mm	0 mm	0 mm	0.5 mm	1 mm (had
					(had radial	radial shrinkage)
					shrinkage)

EXAMPLE 26

The following Example demonstrates a composition of the instant invention that can be dispensed via a commercially available dual tube caulk gun.

Product Name	Chemical Name	Supplier	% range
Part A
Epon 862	Bis F epoxy resin	Shell	5-75
Cardura E-10	glycidyl ester	Walsh & Assoc	1-30
Polybd ®	polybutadiene	Elf Atochem	1-60
605 E
Micropearls	Isobutane encapsulated in	HM Royal	10-75
F30 D	Polymer vinylidene chloride
Part B
Phosphoric	phosphoric acid	Harcross	3-25
acid
CD513	methacrylate	Sartomer	1-10
SR495	caprolactone acrylate	Sartomer	1-10

Parts A and B were prepared separately by being mixed in lab scale beakers. Parts A and B were mixed and dispensed by using a 4:1 TAH Industries motionless mixer tube.

EXAMPLE 27

The following Table lists the Raw Materials that were employed in Example 27. The foam in Example 27 was prepared and tested in accordance with Examples 18-22 and 25. This Example illustrates foam having desirable flame resistant characteristics. Such foam can be employed in a wide range of applications including aerospace (e.g., aircraft insulation), automotive (e.g., sound abatement and structural support), among other end uses.

Raw Material	Description	Supplier
Intelimer 7004	Polymer Bound Imidazole Catalyst: MP = 149F	Landec
Intelimer 7024	Encapsulated 2-Ethyl-4-Methyl Imidazole:	Landec
	MP = 149F
Intelimer 7124	Polymer Bound Imidazole Catalyst	Landec
PEP 6137	Acrylic Monomer Modifier Epoxy: EEW = 150:	Pacific Epoxy
	Visc = 950 cP
PEP 6138	Acrylic Monomer Modified Epoxy: EEW = 150:	Pacific Epoxy
	Visc = 100 cP
PEP 6139	Acrylic Monomer Modified Epoxy: EEW = 130:	Pacific Epoxy
	Visc = 3000 cP
PEP 6264	Urethane Modified Epoxy: EEW = 210:	Pacific Epoxy
	Visc = 2000 cP
PEP 6431	Novolac: EEW = 170: visc = 25,000: fnc = 2.2	Pacific Epoxy
PEP 6433	Novolac: EEW = 170: visc = 8000: fnc = 2.2	Pacific Epoxy
NPEK-119	Bis A Epoxy: EEW = 180-195: Visc = 500-1200	Peninsula Polymers/Nan
		Ya Corporation
Epon 824	Bis A/Epichlorohydrin Based Epoxy Resin (85-90%)	Walsh & Assoc/Shell
	& Modified Base Epoxy Resin (10-15%)	Chemical
Epon 826	Bis A/Epichlorohydrin Based Epoxy Resin:	Walsh & Assoc/Shell
	EEW = 182: Visc = 8000 cP	Chemical
SR 239	DiFunctional: 1,6 Hexanediol Dimethacrylate:	Sartomer
	visc = 8: hydrophobic backbone
SR 9009	TriFunctional: Trifunctional Methacrylate:	Sartomer
	visc = 35
CD 9050	Monofunctional Acid Ester: Adhesion	Walsh &
	Promoting Monomer: visc = 20	Assoc/Sartomer
CD 9051	Trifunctional Acid Ester: Adhesion Promoting	Walsh &
	Monomer: visc = 250	Assoc/Sartomer
SR 444	Trifunctional Monomer: Pentaerythritol	Walsh &
	Triacrylate: Hydroxy Pendant Group:	Assoc/Sartomer
	visc = 520 cP
CD 513	Methacrylate Ester (Propoxylated 2 Allyl	Sartomer
	Methacrylate): Commercially available under
	5E consent
Ebecryl 2047	Trifunctional Acrylated Diluting Oligomer:	UCB Radcure
	visc = 400 cP: tensile = 1000 psi: elong = 8%:	UCB Radcure
	Tg = 3F
Ebecryl 3200	Acrylated Epoxy: visc = 3000 cP:	UCB Radcure
	tensile = 11,900 psi: elong = 6%: Tg = 118F
Kronitex TCP	Tricrecyl Phosphate: Flame Retardant	FMC Corp
Santicizer 143	Modified Triaryl Phosphate Ester	Solutia
Santicizer 148	Isodecyl Diphenyl Phosphate	Solutia
Santicizer 154	Triaryl Phosphate Ester: t-Butylphenyl	Solutia
	Diphenyl Phosphate
NOVOC RGS-2020DV	Modified Vinyl Ester: WPE = 300-2800:	Composite
	Visc = 800 cP: Acid Value = 14-20	Technology
Veova 10	Vinyl Ester Of Tertiary Carboxylic acid:	Walsh & Assoc/Shell
	Neodecanoic acid, ethenyl ester: visc = 8 cP
Components Wt. %	Sample No. 1	2	3	4
Part A
Epon 828	60	60	60	60
BK 5799 (carbon Black)	4 g	4 g	4 g	4 g
Part B
Santicizer 97	15	15	15	15
H 3 PO 4 (conc)	7.5	7.5	7.5	7.5
Micropearls F30D	8	8	8	8
Intelimer 7004		1.5
Intelimer 7024			1.5
Intelimer 7124				1.5
Initial Rxn Time (sec)	51 sec	64 sec	78 sec	81 sec
Shrinkage	0 mm	0 mm	0 mm	0 mm
% Height Expansion	221%	238%	257%	234%
Density 2 (g/in 3 )
Top	4.53	4.51	4.72	4.20
Bottom	4.87	4.93	5.25	4.76
Specific Gravity
% H 3 O Absorption 2	2.8% 2.0%	4.8% 3.0	6.8% 4.9%	7.5% 5.2%
Shore A: Initial	81 85	80 82	86 85	75 77
Shore A - After 24 hr Water Soak	82 84	79 79	80 78	72 71
Components Wt. %	Sample No. 5	6	7	8	9
Part A
Epon 828	60			30	30
BK 5799	4 g
Epon 826		60	60	30	30
Z6040					1
Part B
Santicizer 97		15	28.46	28.46	28.46
H 3 PO 4 (conc)	7.5	7.5	13.34	13.34	13.34
Micropearls F30D	8	8	14.23	14.23	14.23
CD 513	15
Initial Rxn Time (sec)	92 sec	50 sec	32 sec	31 sec	32 sec
Shrinkage	0 mm	0 mm	0 mm	0 mm	0 mm
% Height Expansion	383%	278%	238%	209%	240%
Density 1 (g/in 3 )
Density 2 (g/in 3 )
Top		4.75	3.72	5.05	4.50
Bottom		4.78	4.15	4.62	4.45
% H 2 O Absorption 1
% H 2 O Absorption 2		54% 71%	74% 38%	11% 9%	15% 13%
Shore A: Initial		90 86	74 77	89 87	83 80
Shore A - After 24 hr		78 75	45 57	70 73	57 56
Water Soak
Shore A: % Drop		13%↓, 13%↓	39%↓, 39%↓	21%↓, 16%↓	31%↓, 30%↓
After 24 hr H 2 O Soak
Components Wt. %	Sample No. 10	11	12	13	14
Part A
Epon 828	30	60	60	30	40
BK 5799				4 g)	4 g
Epon 826	30			30
Z6040	1	2.5	3.5	2
PEP 6264					20
Part B
Santicizer 97	28.46	28.46	28.46	25.14	15.5
H 3 PO 4 (conc)	11	13.34	13.34	11.79	7.5
Micropearls F30D	14.23	14.23	14.23	12.57	8
Initial Rxn Time (sec)	45 sec	38 sec	47 sec	44 sec	281 sec
Shrinkage	0 mm	0 mm	0.5 mm	0.5 mm	0.5 mm
% Height Expansion	178%	232%	227%	233%	50%
Density 1 (g/in 3 )
Density 2 (g/in 3 )
Top	6.11	4.53	5.14	4.13
Bottom	6.08	4.13	4.83	4.46
% H 2 O Absorption 1
% H 2 O Absorption 2	24% 26%	56% 41%	73% 86%	27% 20%
Shore A: Initial	84 86	72 67	81 79	83 80
Shore A - After 24 hr	67 68	30 31	44 38	50 48
Water Soak
Shore A: % Drop	20%↓, 21%↓	58%↓, 54%↓	46%↓, 52%↓	40%↓, 40%↓
After 24 hr H 2 O Soak
Components Wt %	Sample No. 15	16	17	18
Part A
Epon 828	40	40	40	40
BK 5799	4 g	4 g	4 g	4 g
PEP 6264	20
PEP 6137		20
PEP 6138			20
PEP 6139				20
Part B
Santicizer 97 $1.22/lb	15.5	15.5	15.5	15.5
H 3 PO 4 (conc) $0.70/lb	10	7.5	7.5	7.5
Micropearls F30D $8/lb	8	8	8	8
Initial Rxn Time (sec)	116 sec	74 sec	81 sec	77 sec
Shrinkage	0.5 mm	0 mm	0 mm	0 mm
% Height Expansion	55%	210%	223%	204%
Density 1 (g/in 3 )
Density 2 (g/in 3 )
Top	11.88	4.64	4.27	4.44
Bottom		5.24	4.94	4.99
% H 2 O Absorption 1
% H 2 O Absorption 2	20%	4% 3%	6% 5%	5% 3%
Shore A: Initial	96	84 86	78 84	85 87
Shore A - After 24 hr	90	73 75	63 66	72 70
Water Soak
Shore A: % Drop	6%↓	13%↓, 13%↓	19%↓, 21%↓	15%↓, 20%↓
After 24 hr H 2 O Soak
Components Wt %	Sample No. 19	20	21	22
Part A
Epon 828		40	45	50
BK 5799 (carbon black)
NPEK-119	60	10
DER 736			15
CD 513				10
Part B
Santicizer 97	15	24.73	24.73	28.8
H 3 PO 4 (>85% conc)	7.5	11.6	11.6	13.5
Micropearls F30D	8	12.37	12.37	14.4
Initial Rxn Time	68 sec	33 sec	instant	44 sec
% Ht Expansion	233%	241%		190%
Density (g/in 3 )
Top	4.50	4.18		4.01
Bot	4.28	4.72		4.44
H 2 O Absorption	25% 12%	25% 13%		151%
Shore A: Initial	85 81	75 82		67 68
Shore A: After Water Soak	67 58	52 60		10 16
Shore A % Drop After Water Soak	21%↓, 28%↓	27%↓,27%↓		85%↓, 77%↓
Shrinkage	0.2%	<2%
Components Wt. %	Sample No. 23	24	25
Part A
Epon 828	50	30	30
BK 5799 (carbon black)		4 g	4 g
Z 6040	2.5	2
Epon 826		30	30
Part B
Santicizer 97	22.86	25.14	16.76
H 3 PO 4 (>85% conc)	11.9	11.79	7.86
Micropearls F30D	12.7	12.57	8.38
Kraton D1107	2.54
Initial Rxn Time	33 sec	44 sec 53 sec	49 sec
% Ht Expansion	228%	233% 204%	210%
Density (g/in 3 )
Top	4.12	4.13	4.53
Bot	4.47	4.46	5.09
H 2 O Absorption	(72 hrs: 118% 148%)	27% 20%	3% 2%
Shore A: Initial	78 71	83 80	85 89
Shore A: After Water Soak	(72 hrs: 25 26)	50 48	79 82
Shore A % Drop After Water Soak	72 hrs Soak 68%↓, 63%↓	40%↓, 40%↓	7%↓, 8%↓
Shrinkage	0.2%	0.9%	0.6%
Components Wt %	Sample No. 26	27	28	29
Part A
Epon 828	30	30	30	60
BK 5799 (carbon black)	4 g	4 g	4 g	4 g
Epon 826	30	30	30
PEP 6210 PA	10
Cardura E-10			10	10
Part B
Santicizer 97	16.76	16.76	16.76	16.76
H 3 PO 4 (>85% conc)	7.86	7.86	7.86	7.86
Micropearls F30D	8.38	8.38	8.38	8.38
Initial Rxn Time	183 sec	44 sec	63 sec	57 sec ?
% Ht Expansion	<50%	197%	257%	250%
Density (g/in 3 )
Top		4.97	5.19	5.34
Bot		5.42	4.72	5.33
H 2 O Absorption		3% 3%	26% 17%	9% 4%
Shore A: Initial		87 89	88 82	88 84
Shore A: After Water Soak		82 84	62 57	63 56
Shore A % Drop After Water Soak		6%↓, 6%↓	30%↓, 31%↓	28%↓, 33%↓
Shrinkage		0.2%	2.1%	2.5%
Components Wt %	Sample No. 30	31
Part A
Epon 828	65.5	65.5
BK 5799 (carbon black)	4 g	4 g
Cardura E-10	3.5	3.5
Part B
Santicizer 97	17	17
H 3 PO 4 (>85% conc)	7.5	7.5
Micropearls F30D	8.5
Initial Rxn Time	84	53
% Ht Expansion	205% 215%	0%
Density (g/in 3 )
Top	5.09	—
Bot	5.60	18.83
H 2 O Absorption	(72 hrs: 4% 3%)	0.22% (96 hrs)
Shore A: Initial	90 90	>100
Shore A: After Water Soak	(72 hrs: 87 86)	>100 (96 hrs)
Shore A % Drop After Water Soak	(72 hrs: 3%↓, 4%↓)	0% (96 hrs)
Shrinkage	0.4%	3%
Compression: 1″d (psi)	1483 1450
Compression: 2″d (psi)	1113
Components Wt %	Sample No. 32	33	34	35
Part A
Epon 828	65.5	65.5	65.5	65.5
BK 5799 (carbon black)	4 g	4 g	4 g
Cardura E-10	3.5	3.5	3.5	3.5
Expancel 051DU	5
Part B
Santicizer 97	17	8.5
H 3 PO 4 (>85% conc)	7.5	7.5	7.5	7.5
Micropearls F30D		8.5	8.5	8.5
Expancel 051DU
Veova 10		8.5		7
Santolink XI-100			17
Cardura E-10				10
Initial Rxn Time	120+ sec	94 sec	232 sec	77 sec
% Ht Expansion	<25%	137%	258%	206%
Density (g/in 3 )
Top			4.16	4.68
Bot			4.19	5.27
H 2 O Absorption			2% 2%	1.3% 1%
Shore A: Initial			73 75	79 79
Shore A: After Water Soak			61 64	70 69
Shore A % Drop After Water Soak			16%↓, 15%↓	11%↓, 13%↓
Shrinkage			0.7%	1%
Components Wt %	Sample No. 36	37	38	39	40
Part A
Epon 828	55.5		95	65.5	65.5
Cardura E-10	3.5	3.5	5	3.5	3.5
Erisys GE-60	10
Epalloy 8240		65.5
BK 5799 (carbon Black)			4 g	4 g
Micropearls F30D					8.5
Part B
H 3 PO 4 (>85% conc)	7.5	7.5	11	7.5	7.5
Micropearls F30D	8.5	8.5	8.5	8.5
Cardura E-10	12	12		12
Veova 10	5	5
Santicizer 97			17	5
Initial Rxn Time	69 sec	75 sec	63 sec	203 sec	17 sec
% Ht Expansion	130%	229%	166%	245%	335%
Density (g/in 3 )
Top		4.63	5.83	4.46
Bot		5.42	6.11	4.99
H 2 O Absorption		(72 hrs) 5% 3%	1% 1%	10% 6%
				(72 hrs)
Shore A: Initial		74 74	94 95	76 76
Shore A: After		(72 hrs) 69 67	91 91	65 66
Water Soak				(72 hrs)
Shore A % Drop		(72 hrs)	3%↓, 4%↓	15%↓, 13%↓
After Water Soak		7%↓, 10%↓		(72 hrs)
Shrinkage	Slight	1%	0.4% 0.5%	1.1%
Compression: 1″d (psi)			2724 2504
Components Wt %	Sample No. 41	42	43	44	45
Parts A
Epon 828	65.5	65.5	65.5	65.5	65.5
Cardura E-10	3.5	3.5	3.5	3.5	3.5
BK 5799 (carbon Black)	4 g	4 g	4 g	4 g	4 g
Part B
H 3 PO 4 (>85% conc)	7.5	7.5	7.5	7.5	7.5
Micropearls F30D	8.5	8.5	8.5	8.5	8.5
Ebecryl 2047	17
Ebecryl 3200		17
CD 9051			17
CD 9050				17
SR 444					17
Initial Rxn Time	81 sec	92 sec	63 sec	82 sec	71 sec
% Ht Expansion	275%	275%	285%	290%	300%
Density (g/in 3 )
Top	4.69	3.92	3.67	3.89	3.59
Bot	4.70	4.75	4.20	4.06	4.12
H 2 O Absorption	32%? 2%	3% 27%?	6% 3%	29% 42%	15% 10%
					(see 1 below)
Shore A: Initial	88 83	83 83	81 82	78 80	78 78
Shore A: After	78 73	70 73	66 67	52 51	75 75
Water Soak
Shore A % Drop	11%↓, 12%↓	16%↓, 12%↓	19%↓, 18%↓	33%↓, 36%↓	4%↓, 4%↓
After Water Soak
Shrinkage	1.1%	0.2%	0.3%	2%	1.2%
Components Wt %	Sample No. 46	47	48	49
Part A
Epon 828	65.5	65.5	65.5	55.5
Cardura E-10	3.5	3.5	3.5	3.5
BK 577 (carbon Black)	4 g	4 g	4 g	4 g
Epalloy 8240				10
Erisys GE-60
Part B
H 3 PO 4 (>85% conc)	7.5	7.5	7.5	7.5
Micropearls F30D	8.5	8.5	8.5	8.5
Santicizer 278	17
SR 9009		17
SR 239			17
Santicizer 97				17
Initial Rxn Time	54 sec	54 sec	79 sec	49 sec
% Ht Expansion	260%	268%	320%	214%
Density (g/in 3 )
Top	4.07	3.99	3.63	4.82
Bot	4.83	4.41	4.20	5.41
H 2 O Absorption	27% 4% (see 1)	53% 39% (see 1)	12% 9%	3% 2%
Shore A: Initial	80 82	85 85	69 71	86 87
Shore A After Water Soak	67 72	77 79	65 67	83 85
Shore A % Drop After Water Soak	16%↓, 12%↓	9%↓, 7%↓	6%↓, 6%↓	4%↓, 2%↓
Shrinkage	0.6%	2%	6%	0.3%
Components Wt %	Sample No. 50	51	52	53
Part A
Epon 828	65.5	55.5	55.5	55.5
Cardura E-10	3.5	3.5	3.5	3.5
BK 5799 (carbon Black)	4 g	4 g	4 g	4 g
Micropearls F30D	8.5
PEP 6433		10
PEP 6431			10
Epalloy 8240				10
Part B
Santicizer 97	17	17	17	17
H 3 PO 4 (>85% conc)	7.5	7.5	7.5	7.5
Micropearls F30D		8.5	8.5	6.5
Initial Rxn Time	56 sec	88 sec	51 sec	52 sec
% Ht Expansion	165%	133%	157%	123%
Density (g/in 3 )
Top	5.39	8.98	5.72	7.15
Bot	5.82	9.59	6.30	7.63
H 2 O Absorption	2% 1%	36% 29%	0.7% 0.7%	0.5% 0.4%
	(72 hrs)
Shore A: Initial	89 90	97 98	91 94	97 97
Shore A: After Water Soak	85 87	93 94	87 91	95 95
Shore A % Drop After Water Soak	5%↓, 3%↓	4%↓, 4%↓	4%↓, 3%↓	2%↓, 2%↓
	(72 hrs)
Shrinkage	0.4%	0.2%	0.1%	0.3%
Compression: 1″d (psi)			1886 2090
Compression: 2″d (psi)				2190
Components Wt %	Sample No. 54	55	56	57	58
Part A
Epon 828	50	65.5	55.5	65.5	55
Cardura E-10		3.5	3.5	3.5	3.5
BK 5799 (carbon Black)	4 g	4 g	4 g	4 g	4 g
Epalloy 8240	20
PEP 6431			10
PBD 605					10
Part B
Santicizer 97	17	12	17	20.4	20.4
H 3 PO 4 (>85% conc)	7.5	7.5	7.5	9	9
Micropearls F30D	8.5	3.5	5	2.5	4
Initial Rxn Time	57 sec	51 sec	56 sec	54 sec 51 sec	37 sec
% Ht Expansion	213%	45%	40%	23% 30%	21%
Density (g/in 3 )
Top	5.21	10.77	—	12.28
Bot	5.87	10.89	9.44	12.41
H 2 O Absorption	2% 0.9%	0.2%	0.6%	1.1% (5 days)
			(72 hrs)
Shore A: Initial	88 92	100	99	100+
Shore A: After Water Soak	85 88	99	98	98 (5 days)
			(72 hrs)
Shore A % Drop After Water Soak	3%↓, 5%↓	1%↓	1%↓	2%↓ (5 days)
			(72 hrs)
Shrinkage	0.1%	1.4%	0.8%	1.9%
Compression: 1″d (psi)	1825 1939	4875 4768	3472 4070	5762 6141	5132 4874
Components Wt %	Sample No. 59	60	61
Part A
Epon 828	150.65	65.5	65.5
Cardura E-10	8.05
BK 5799 (carbon Black)	4 g	4 g	4 g
Veova 10		10
Z 6040			2
Part B
Santicizer 97	17	17	17
H 3 PO 4 (>85% conc)	16	7.5	7.5
Micropearls F30D	5	6.5	6.5
Initial Rxn Time	42 sec 30 sec	54 sec	96 sec
% Ht Expansion	20%	20%	122%
Compression: 1″d (psi)	7212 7201		1955 1940
Components Wt %	Sample No. 62	63	64
Part A
Epon 828	65.5	65.5	65.5
Cardura E-10	3.5		3.5
BK 5799 (carbon black)	4 g	4 g	4 g
Santicizer 97		3.5
Part B
Santicizer 97	20	20.4
H 3 PO 4 (>85% conc)	6.5	9	9
Micropearls F30D	4.5	2.5	2.5
RGS-2020 DV			20.4
Initial Rxn Time	81 sec	58 sec	175 sec
% Ht Expansion	32%	23%	67%
Density (g/in 3 )
Top		11.44	9.54
Bot	11.4	11.38	10.21
H 2 O Absorption	(72 hrs) 0.4%	0.9	1.3%
Shore A: Initial	100+	100+	98
Shore A: Water Soak	(72 hrs) 100	99	91
Shore A % Drop After Water Soak	(72 hrs) 0%+	1%+	7%
Salt: % Absorption	0.5%	1.5%
Salt: % Shore A Drop	1%+	16%+
Shrinkage	1.1	1.6%	2.2%
Compression: 1″d (psi)	4116 4452	4382 4933	3784 3786
Heat Age Rating	2	3
Components Wt %	Sample No. 65	66
Part A
Epon 828	42.8	50.4
Erisys GE-29	12.8	4.2
Micropearls F30D	12.8	10.8
BK 5799 (carbon black)	4 g	4 g
Part B
Santicizer 97	17.6	18
Santicizer 154	4.4	4.5
H 3 PO 4 (>85% conc)	13.2	11.2
Initial Rxn Time	25 sec	30 sec
% Ht Expansion	287%	275%
Density (g/in 3 )
Top		3.72
Bot
H 2 O Absorption	34%
Shore A: Initial	45	71
Shore A: Water Soak	14
Shore A % Drop After Water Soak	69%
Shrinkage	0.5%	0.2%
Flammability (vert)	Torch	Torch
Flame Time	3 sec	7 sec
Burn Length	0.06-0.19 in	3.75-7 in
Flammability (horiz)	Torch	Torch
Flame Time	5 sec	6 sec
Burn Length	3.25-3.75 in	—

A skilled person in this art would understand that these exemplary processes an be modified by manipulating process variables such as time and temperature of each aforementioned mixing step, mixing rate (RPM), time under vacuum, radiation source (e.g., UV light) and length of exposure and distance from source, and level of vacuum (mm Hg) as well as operating a continuous process. While the above Examples illustrate a batch process a skilled person in this art after having reviewed and understood the instant disclosure, would be capable of manipulating the aforementioned process variables to tailor the instant composition for a virtually unlimited array of product applications.

While the present invention has been described in certain preferred embodiments thereof, it will be apparent that various substitution, omissions, modifications, and other changes which may be made without departing from the spirit of the invention. Thus, the present invention should be limited only by the scope of the following claims including equivalents thereof.

Claims

1. A foam precursor comprising:(a) an A-side foam precursor composition comprising at least halogenated epoxy functional compound, and a blowing agent, and; (b) a B-side foam precursor composition comprising an acid source and at least one dialkyl adipate; wherein at least one of said foam precursors is encapsulated.

2. The foam precursor according to claim 1 wherein (a) further includes a modifying material.

3. The foam precursor according to claim 1 wherein (b) further comprises a carrier material.

4. The foam precursor of claim 1 wherein said blowing agent comprises an encapsulated blowing agent and the encapsulated blowing agent has at least two different activation temperatures.

5. The foam precursor of claim 1 wherein the encapsulated blowing agent comprises a thermoplastic shell that contains at least one of isobutane and isopentane blowing agent.

6. The foam precursor of claim 1 wherein at least one of the A-side precursor and the B-side precursor further comprises castor oil, at least one benzyl phthalate and at least one member selected from the group consisting of Bis A epoxy and Bis F epoxy.

7. The foam precursor of claim 1 wherein said epoxy compound is a bis-A or bis-F epoxy compound; the blowing agent comprises at least one of isopentane and isobutane and the A-side precursor further comprises at least one member selected from the group consisting of polypropylene, polyethylene and polyvinyl alcohol.

8. A method for producing a foam comprising:(a) combining an A-side foam precursor comprising at least one epoxy functional compound with a B-side foam precursor comprising at least one hydrogen donating Lewis acid and at least one dialkyl adipate, wherein at least one of said A-side and B-side comprise an encapsulated blowing agent, under conditions sufficient to provide an exothermic reaction within less than about 2 minutes from said combining; and (b) utilizing heat from the exothermic reaction so as to expand the combined components to form a foam.

9. The method of claim 8 wherein said at least one hydrogen donating Lewis acid comprises phosphoric acid.

10. The method of claim 9 wherein said phosphoric acid is substantially water free.

11. The method of claim 8 wherein said combining comprises dispensing through a mixing device comprising a static mix head.

12. The method of claim 8 wherein the combined A-side and B-side are dispensed into a containment device.

13. The method of claim 11 wherein said static mix head is affixed in a manner to substantially seal a cavity into which the foam is dispensed.