PRODUCTION OF CELLULAR THERMOPLASTIC RESINOUS MATERIAL

Abstract: Cellular thermoplastic resinous materials are produced by a process which comprises preparing a mixture of a thermoplastic resinous polymer, a powdered alkali metal borohydride and a finely divided activating agent of high surface area having a proton source adsorbed upon its surface, heating the mixture until the polymer is in molten condition whereupon foaming of the polymer occurs. The borohydride may be provided as pellets of a concentrated dispersion thereof in a substantially inert thermoplastic resinous polymer.

Description: "PRODUCTION OF CELLULAR THERNOPLASTIC RESINOUS MATERIAL" This invention relates to the production of cellular thermoplastic resinous material from a thermoplastic resin and a blowing agent. The use of alkali metal borohydrides such as sodium borohydride and potassium borohydride as blowing agents in connection with the production of cellular articles is well known. For example, United States Patent No. 2,951,819 utilizes an alkali metal borohydride in connection with the manufacture of cellular articles. United States Patent No. 3,167,520 relates to cellular articles prepared from polystyrene by extruding polystyrene resin containing an alkali metal borohydride which decomposes during extrusion to form a cellular article. This invention is directed to an improvement in the technique of the aforesaid United States Patent No. ),167,520. The invention relates to the use of an alkali metal borohydride such as sodium or potassium borohydride as a blowing agent in connection with the production of articles having a foamed or cellular structure. One particularly advantageous embodiment of the invention relates to the use of a stable borohydride concentrate mixture containing from about 0.5fix to 20/ó by weight of an alkali metal borohydride with a dry inert resinous polymer. The concentrate should contain not more than about 0.1 of adsorbed water or the borohydride will hydrolyze. Such water may be adsorbed upon the surface of the borohydride and/or upon the surface of the resinous polymer. The concentrates used in the method of the invention may be made by dry blending from 0.5% to 20% by weight of powdered alkali metal borohydride with a dry inert thermoplastic resinous polymer to form a mixture containing less than about 0.1 by weight of water; heating the dry blended mixture to a temperature above that of the melting point of the resin to fdrm a molten mixture; extruding the molten mixture and then cooling the extrudate to form a solid, stable concentrate; and then forming the cooled extruded concentrate into pellets by conventional techniques such as chopping or grinding. In one embodiment of the invention the method of making cellular articles comprises contacting a mixture of alkali metal borohydride and a thermoplastic resinous polymer with a high surface area silica activating agent having a proton source adsorbed upon its surface so as to cause said alkali metal borohydride to hydrolyze and thus cause said resinous polymer to have a foamed cellular structure. The alkali metal borohydride may be in the form of the concentrate described above or zs neat powdered alkali metal borohydride. The above described concentrates may be used to incorporate low levels of alkali metal borohydride into the same or different resins with the object of utilising the incorporated borohydride to foam the resin when an additional proton providing activator such as water, alcohol or acid is also added to the resin to react with the borohydride and liberate hydrogen. When used as a blowing agent for thermoplastic resins, up to 0.5% of NaBH4 may be incorporated into the resin from the concentrate. The preferred proportion is up to 0.25%. The use of a concentrate to incorporate low levels of borohydride into the resins has several advantages. First of all, the concentrates protect the borohydride from adventitious hydrolysis during handling and may be stored for periods of the order of a year without the occurrence of significant hydrolysis. Secondly, it is much easier to incorporate the borohydride at very low levels such as less than 1 wt.% into the resin by using such concentrates. Thirdly, overall handling such as weighing and making uniform mixtures is much easier using the concentrates than using neat borohydride. Because such highly reactive material has been concentrated and rendered substantially inert, employee safety is enhanced. In addition, very uniform dispersions of borohydride in the resin are obtained using the concentrates. The stable borohydride concentrate used preferably comprises from about 0.5to to 20% by weight of an alkali metal borohydride and less than about 0.1% of adsorbed water, the balance being essentially dry inert resinous polymer. The 0.5% lower limit for borohydrides is preferred primarily because lower concentrations necessarily involve the use of excessive amounts of the concentrate and the 20% upper limit is preferred because higher levels involve using excessively small amounts of the concentrate and thus hamper the attainment of a uniform dispersion of borohydride in the thermoplastic polymer to be foamed. It is preferred to include the alkali metal borohydride in amounts between 2 and 10% because such range permits let-down ratios of the order of about 20:1 as are normally desired in the industry. Sodium and potassium borohydrides are contemplated for use in such concentrates. The concentrate should contain no more than about 0.1% by weight of adsorbed water, preferably not more than about 0.01%, in order to prevent hydrolysis of the borohydride. Thus, the borohydride and resin must be very dry when mixed to form the concentrate and moisture pick-up should be avoided during such mixing. The inert resinous polymer component of the concentrate comprises a resin or resins from which reactive protonic hydrogen atoms are substantially absent. Such resins include polyolefins, polydienes, polystyrene, polyphenylene-oxidestyrene, polyacrylates, polyvinylchloride and polyvinylacetate. The alkali metal borohydride concentrates are prepared by dry blending from about 0.5 to 20 by weight of the borohydride with the inert thermoplastic resinous polymer to form a dry mixture thereof. The mixture should contain less than about 0.1 to of adsorbed water. The mixture is then subjected to a temperature in excess of the melting point of the resin, extruded, cooled, and formed into pellets. As mentioned previously, the alkali metal borohydride is useful as a blowing agent in connection with the manufacture of cellular or foamed resinous articles. Typical resinous polymers that may be foamed using the concentrate include but are not limited to polyolefins, polydienes, polystyrenes, polyphenyleneoxide-styrenes, polyacrylates, polyvinyl chloride and polyvinylacetate. Cellular articles may be manufactured by mixing the alkali metal borohydride concentrate described above with a resinous polymer and an effective amount of an activating agent capable of donating acidic protons to the alkali metal borohydride so as to hydrolyse substantially all of the alkali metal borohydride whilst the resinous polymer is molten and thus form a cellular article. The activating agent may comprise a finely divided high surface area solid having a proton source adsorbed on its surface. A preferred activating agent is finely divided high surface area silica. An example of a form of silica suitable for use in the method of the invention is that manufactured by Cabot Corporation under the designation "CAB-O-SIL Such type of silica is manufactured by fuming. It is preferred to utilize silica having a surface pH of less than 7 because acidic materials aid in the decomposition of alkali metal borohydrides. It is especially preferred to have a pH of 4 or lower. Finely divided, high surface area activating agents function to provide nucleation sites for foam to form. These materials have a very high capacity for adsorbing liquids such as water and yet remain a free-flowing solid and thus aid in the promotion of uniformity during the blending or mixing stage of the method. Suitable proton sources include water, mineral acids, carboxylic acids, alcohols, sulfonic acids, polyacrylic acid and polystyrene sulfonic acid. Water is preferred due to its relatively low cost, availability, and low corrosivity. It has also been found that the silica activators described above may be used in admixture with alkali metal borohydride materials other than the concentrates described above. For example, powdered alkali metal borohydrides may be used together with the silica activators to produce foamed polymers. As in the case of the concentrate additions, the alkali metal borohydride and a resinous polymer are contacted with a sufficient amount of activating agent to cause substantially all of the borohydride to hydrolyse. The following preparations and examples further illustrate the invention. PREPARATION OF BOROHYDRIDE CONCENTRATES PREPARATION A Sodium borohydride was concentrated in polypropylene by the following procedure. Ninety parts by weight of previously dried, powdered, unstabilized polypropylene resin (melt index 12) and 10 parts by weight of NaBH4 that was previously dried for 24 hours at 1000C, were thoroughly mixed in a dry blender. The resultant mixture was extruded through a 0.318 cms diameter die at about 4500F. The extruded rod was pelletized in line with the extruder. The extruded concentrate was examined with a low power microscope and an extremely uniform dispersion of minute barohydride particles was found. Virtually no gas bubbles were observed in the resin pellets. PREPARATION B Sodium borohydride was concentrated in NORMS resins in the following manner. Ninety parts by weight of dry NORMS resin FN 215, a proprietary General Electric Co. blend of polyphenylene oxide and polystyrene in pellet form, was mixed with 0.1 part by weight of mineral oil and 10 parts by weight of NaBH4 powder, that was previously dried at 1000C for 8 hours. The resultant dry blended mixture was then extruded at about 4500F and pelletized as described in the previous example. The concentrate pellets were equivalent to the pellets of Preparation A. PREPARATION C Sodium borohydride was concentrated in polystyrene using the following procedure. Ninety parts by weight of previously dried high impact polystyrene pellets was blended with 0.1 part of mineral oil and 10 parts by weight of dry NaBH4 powder. The resultant mixture was then extruded at about 4500F and pelletized as described in Preparation A. As in Preparation A, an excellent dispersion of minute particles of NaBH4 in the resin was produced with virtually no gas bubbles observed. ACTIVATING AGENT CONCENTRATES PREPARATION D An activating agent concentrate was prepared by the following prcedure. 28.6 parts by weight of CAB-O-SIS fumed silica was intensively mixed with 71 parts by weight of a solution (65 solids) of polyacrylic acid in water for five minutes with use of a Renschel mixer. The resultant mixture was a "dry" free flowing powder. PREPARATION E The procedure described in Preparation D was also used to prepare an activator concentrate containing 71.4 parts by weight of water. The water was added slowly to 28.6 parts by weight of CAB-O-SIL fumed silica while mixing. The concentrate handled as a "dry" powder. Example 1 Polypropylene foamed fibres were prepared as follows. A series of blends of polypropylene resin powder, sodium borohydride, and CAB-O-SIL whose compositions are shown in Table I were prepared. The polypropylene powder was not dried prior to blending, but rather was blended in the "as-received" condition. TABlE I Polypropylene 99.89 99.75 .99.5 99.95 99.92 NaBH4 0.1 0.25 0.5 0.05 0.075 CAB-O-SIL 0.001 0.0025 0.005 0.005 0.00075 These mixtures of Table I were extruded through a 1.905 cms diameter die at 430-44G F to form filaments with varying amounts of oriented foamed cells. A 3.5:1 compression ratio was employed. The moisture present on the NaBH4 and the resin was sufficient to activate the release of hydrogen to foam the fibres as they passed through the melt phase in the extruder. Example 2 Foamed polypropylene structural parts were prepared by the following procedure. Blends of undried polypropylene resin powder, sodium borohydride, powdered stearic acid and CAB-O-SIS were prepared in a Henschel Mixer. Stearic acid functioned as the activator and CAB-O-SIT as the nucleating agent for bubble formation in this system. This system was limited to 1% of stearic acid activator due to the limited solubility of the acid in the solid resin and because the lubricity in the barrel of the extruder provided by the molten stearic acid causes slippage of the screw. Although good foams were prepared with good density reduction, stearic acid and other fatty acids are less than ideal activators because of the above mentioned factors. in any event, structural foam parts of good quality were produced on a reciprocating screw T/D 16:1, 100 ton, 141.75 gram injection moulding machine equipped with a cut-off nozzle. The compositions shown in Table II were so produced. All percentages are based on the weight of polypropylene resin. TABlE II SBH Fumed Silica Stearic Acid ?o' Wt.Reduction of Part * %0 %0 Part Due to Foam 0.06 0.1 1.U 20.2 b13 0.1 1.U 27.3 0.25 0.1 1.0 34.4 0.5 0.1 1.0 37.3 1.O 0.1 1.0 33.7 Example 5 Foamed polystyrene structural parts were prepared by the following procedure. Polystyrene resin powder, the sodium borohydride concentrate prepared in Preparation C, and either the activator of Preparation D or Preparation E were blended in the proportion shown in Table III. All percentages are based upon the weight of the resin. TABlE III So Conc. of % Conc. of % Conc. of Preparation C Preparation E Preparation D fio Part lT.a3H4 Chemical H20 Activator Polyacrylic Wt. reduction Blowing Agent Acid Activator 1 0.56 16 1 0.28 15.1 2 0.28 18.4 4 2.24 26.8 8 2.24 25.5 1.15 14.4 1 0.14 12 4 0.56 23.3 25 0.7 25.6 3excellent quality foams having very fine uniform pore size were produced using a structural foam injection machine. Density reductions of about 25% using only 4% of the blowing agent concentrate (0.4k WaBH4) and 2.24% of the silica/water activator concentrate are unusually high and very desirable for this type of structural foam. Normally, with nitrogen injection to provide cells, density reductions of less than 20% are achieved. Moreover, the borohydride blown foam was unusually white, whereas the nitrogen blown foams have a slightly yellow cast. These Activator concentrates such as water, organic acids, alcohols, etc. adsorbed on colloidal silica serve as ideal activators and nucleating agents for these systems because the activators can be premixed with blowing agent concentrates in the desired ratio with no reaction occurring. This mixture can then be blended with the resin to be foamed in the desired ratio and fed into the foaming machine to pro duce the foamed article. Example 4 Extruded foamed sheets of NORTh resin were manufactured by the following technique. NORTh resin was blended with the sodium borohydride blowing agent concentrate of Preparation C and an organic acid according to the percentages listed in Table IV. All percentages are based on the weight of NORYL resin. These mixtures were extruded with a 19.05 mm diameter extruder. TABlE IV Chemical % Chemical Acid/Sodium Blowing Blowing Acid Borohydride Degree of Agent Agent Activator Mole Ratio Foam Preparation C 1.0 Oleic 4/1 Highly Foamed Preparation C 1.0 Octanoic 4/1 Highly Foamed Neat NaBH4 0.1 Octanoic 4/1 Highly Foamed Preparation C 1.0 Stearic 4/1 Highly Foamed Preparation C 1.0 - - Very Slight It can be observed from this example that practically no foaming occurs where the chemical blowing agent is used in the absence of an activator. Furthermore, the NaBH4 concentrates are just as efficient as an equivalent amount of Neat NaBHg for blowing. Neat NaBH4 possesses many other deficiencies previously described which are overcome by use of the blowing agent concentrates.

Claims: CLAIMS: 1. A method of making a cellular thermoplastic resinous material from thermoplastic resin and a blowing agent characterised in that said method comprises preparing a mixture of a thermoplastic resinous polymer, a powdered alkali metal borohydride and an effective amount of a finely divided activating agent of high surface area having a proton source adsorbed upon its surface, heating said mixture until said thermoplastic resin is in molten condition so as to hydrolyse said alkali metal borohydride with consequent foaming of said molten resin and production of a cellular structure. 2. A method as claimed in claim 1 further characterised in that said activating agent is a finely divided high surface area silica. 3. A method as claimed in claim 1 or claim 2 further characterised in that said borohydride is sodium or potassium borohydride. 4. A method as claimed in any of claims 1-3 further characterised in that said alkali metal borohydride is introduced into said mixture in the form of a concentrate consisting essentially of 0.5 to 20.0%o by weight of powdered alkali metal borohydride, less than 0.1fix of adsorbed water, the balance being essentially inert thermoplastic resinous polymer. 5. A method as claimed in any of claims 1-4 further characterised in that said proton source is water, a mineral acid, a carboxylic acid, an alcohol, a sulphonic acid, polyacrylic acid or polystyrene sulphonic acid.

Inventors: WADE, ROBERT C.
Applicants: MORTON THIOKOL, INC.
Application year: 1982
Main classification: C08J9
IPC codes: C08J9