Prefoamed particles of crosslinked propylene-type resin and molded article prepared therefrom

This invention relates to prefoamed cross-linked propylene-type resin particles, and a molded article prepared therefrom.
Generally, propylene-type resins have superior thermal and chemical resistances and high mechanical strength, higher flexibility than polystyrene and higher rigidity than polyethylene. The present inventors previously succeeded in developing prefoamed non-crosslinked propylene-type resin particles and a molded article ("molded article" in this specification means an article obtained by filling prefoamed particles into a mold capable of enclosing the particles but allowing escape of gases thereform, and heating the particles to expand them to the configuration of the mold) having superior properties produced by foaming these prefoamed particles under heat in a mold. It is not always easy, however, to obtain prefoamed non-crosslinked propylene-type resin particles having a uniform expansion ratio stably because the non-crosslinked structure of the propylene-type resin results in abrupt changes in viscoelasticity at temperatures in the vicinity of the foaming temperature. Accordingly, the above prior technique leaves room for improvement. If prefoamed particles having greatly varying expansion ratios are used in fabrication within mold, the cushioning properties of the resulting molded articles vary, and also the foamed articles become, or tend to become, open-cellular so that it is difficult to obtain stable properties. Moreover, the non-crosslinked articles are still desired to be improved in regard to compression set, dimensional change upon heating, compression hardness, etc.
Extensive investigations made by the present inventors in view of the above state of the art have now led to the discovery that prefoamed particles having a gel fraction of 1 to 65% prepared by using a specific crosslinked random propylene as a base resin, and a molded article prepared from the prefoamed particles have improved properties.
According to this invention, there are provided prefoamed crosslinked propylene-type resin particles prepared by using as a base resin a propylene random copolymer whose amount of heat of crystallization determined by a DSC method is 19 to 10 cal/g, said prefoamed particles having a gel fraction of 1 to 65%.
There is also provided a molded article of a crosslinked propylene-type resin which is a fused aggregate of the aforesaid prefoamed particles wherein the number of cells, N per mm.sup.3, and the density, d (g/cm.sup.3), have the relation represented by the expression 2<N.sup.1/2 /d.sup.1/3 <45.
Examples of the propylene random copolymer whose amount of heat of crystallization determined by a DSC method is 19 to 10.0 cal/g are an ethylene/propylene random copolymer and ethylene/propylene/1-butene random copolymer. The ethylene/propylene random copolymer produces a particularly excellent effect.
The amount of heat of crystallization of the base resin used in this invention is 19 to 10 cal/g, preferably 17.5 to 10 cal/g. The use of a propylene random copolymer whose amount of heat of crystallization is larger than 19 cal/g reduces the post-expanding ability of the prefoamed particles during fabrication in a mold and leads to the necessity of using high vapor pressures for molding, and moreover give brittle molded articles. If the amount of heat of crystallization is smaller than 10 cal/g, the resulting prefoamed particles and a molded article obtained by molding the prefoamed particles in a mold have reduced rigidity.
The amount of heat of crystallization can be determined by the DSC method as follows: By using a differential scanning calorimeter, about 6 mg of the sample is put in an aluminum cell, crimped, heated to 220.degree. C. at a rate of 10.degree. C./min. and thereafter cooled to about 50.degree. C. at a rate of 10.degree. C./min. in nitrogen gas. The amount of heat of crystallization is calculated from the resulting thermogram.
In the propylene random copolymer of this invention, the proportions of propylene and another olefin are preferably such that it comprises 90 to 99% by weight of the propylene component and 1 to 10% by weight of the other olefin component. If the proportion of the propylene component is less than 90% by weight, rigidity and strength characteristics of the propylene resin are reduced. If the other olefin is, for example, ethylene, the properties of the resulting copolymer are undesirably close to those of low-density polyethylene. On the other hand, if the proportion of the other olefin component is less than 1% by weight, the effect of modification is small.
The prefoamed particles and the molded article of this invention are composed of a resin obtained by crosslinking the propylene random copolymer as a base resin. When a crosslinked resin mixture is used as the base resin, it may be a mixture of the crosslinked propylene random copolymer and a crosslinked or non-crosslinked other resin. Or it may be a mixture obtained by mixing the propylene random copolymer and another resin and crosslinking the mixture. Examples of the other resin, crosslinked or non-crosslinked, include rubbers such as ethylene/propylene rubber and ethylene/1-butene rubber; polyethylenes such as low-density polyethylene, high-density polyethylene and linerar low-density polyethylene; thermoplastic elastomers; propylene homopolymer, propylene/ethylene block copolymer; and mixtures of these. Preferably, the proportion of the other resin is not more than 50% by weight.
The prefoamed particles and the molded article of this invention comprise the foresaid crosslinked propylene random copolymer, and have a gel fraction of 1 to 65%.
The gel fraction of the molded article is determined as follows: A portion of the molded article is boiled for 8 hours in boiling xylene. The xylene-insoluble portion obtained at this time is dried at a temperature of 80.degree. C. under a reduced pressure of 2 mmHg or below for 8 hours. The percentage of the dry weight based on the weight of the sample before boiling is defined as the gel fraction.
The gel fraction of the prefoamed particles denotes that of aged prefoamed particles obtained by leaving the prefoamed particles to stand under atmospheric pressure thereby substituting air for the blowing agent contained in them, and is determined in the same way as described above for the molded article by using such aged prefoamed particles. The gel fraction of the prefoamed particles remains unchanged even when they have been expanded and fused under heat in a mold to produce a fushed aggregate, namely a molded article.
Prefoamed particles having a gel fraction over 65% have poor post-expanding ability, and the state of fusion of the prefoamed particles to one another in the resulting molded article becomes poor, and the molded article has a high water absorption. Furthermore, the surface of the molded article is remarkably uneven. On the other hand, if the gel fraction is less than 1%, the resulting molded article has the same defects as a molded article obtained from a non-crosslinked propylene random copolymer.
Preferably, the prefoamed particles of this invention have the following relation
2<E.sup.1/3 .times.n.sup.1/2 <45
wherein E is the true expansion ratio of the prefoamed particles and n is the average number of cells per mm.sup.2 of cross section.
Prefoamed particles having an E.sup.1/3 .times.n.sup.1/2 value of 2 or less give an in-mold foamed article having coarse cells, and the state of fusion of the particles to one another is not good. Prefoamed particles having an E.sup.1/3 .times.n.sup.1/2 value of 45 or more tend to shrink during fabrication in a mold, and moreover causes a decrease in the proportion of closed cells. The true expansion ratio of the prefoamed particles, E, can be determined by putting prefoamed particles of a known weight in a fixed amount of water in a measuring cylinder, measuring the entire volume of the contents of the cylinder, subtracting the volume of water from the entire volume of the contents to calculate the volume of the prefoamed particles and dividing the weight of the prefoamed particles by their volume. The average number of cells, n, can be determined by observing the cross section of the prefoamed particles under a microscope, measuring the number of cells per mm.sup.2, and averaging the results.
Preferably, the prefoamed particles of the invention have an internal pressure decreasing speed coefficient, k, at 25.degree. C. and 1 atm. of K.ltoreq.0.30 (1/hr). Prefoamed particles having a k of more than 0.30 (1/hr) tend to give resulting molded article which has large shrinkage with respect to the mold, and is brittle.
The internal pressure decreasing speed coefficient, k, denotes the coefficient of the speed at which the internal pressure of the prefoamed particles decreases at 25.degree. C. by the escaping of air from their inside when an internal pressure of 2 to 5 kg/cm.sup.2 -G has been applied to the prefoamed particles with air. It is determined by the following method.
Prefoamed particles having a known expansion ratio and weight are filled in a polyethylene bag having a size of, for example, 70 mm.times.100 mm, and containing numerous pinholes. While maintaining a temperature of 25.degree. C., a pneumatic pressure is applied to impart an internal pressure of 2 to 5 kg/cm.sup.2 -G to the prefoamed particles. Then, the weight of the prefoamed particles is measured. The prefoamed particles are then maintained at a temperature of 25.degree. C. and a pressure of 1 atm., and after the lapse of 10 minutes, the weight of the prefoamed particles is measured. The internal pressure, P.sub.o (kg/cm.sup.2 -G), of the prefoamed particles immediately after application of the internal pressure and the internal pressure, P.sub.1 (kg/cm.sup.2 -G), of the prefoamed particles after they have been maintained for 10 minutes at 25.degree. C. and 1 atm. are calculated in accordance with the following equation. ##EQU1##
The weight of air increased is the difference between the weight of the particles at the time of measuring their internal pressure and the weight of the particles before the pressurizing treatment. T is the temperature of the atmosphere. The volume of air within the particles is calculated from the expansion ratio of the foamed particles.
The internal pressure decreasing speed coefficient, k, is calculated in accordance with the following equation using P.sub.o and P.sub.1 determined as above. ##EQU2## wherein t is the time in hours, and in the above case, t is 1/6.
The foamed condition of the molded article of this invention, namely a fused aggregate of the prefoamed particles, is such that the average number of cells per mm.sup.2 of cross section (N/mm.sup.2) and the density of the molded article (d in g/cm.sup.3) have the relation represented by the expression 2<N.sup.1/2 /d.sup.1/3 <45. If N.sup.1/2 /d.sup.1/3 is 2 or less, the surface of the molded article is harder than is necessary, and the fused condition of the prefoamed particles is poor. Consequently, the various properties of the molded article will be undesirably deteriorated. If, on the other hand, N.sup.1/2 /d.sup.1/3 is at least 45, the resulting molded article is brittle and susceptible to breakage and develops creases on its surface.
The average number of cells, N, is determined by observing the cross section of the molded article under a microscope, measuring the number of cells per mm.sup.2 of the cross section, and averaging the results.
One example of the production of a molded article from the prefoamed particles of the invention will be described below with reference to the case of using a propylene random copolymer alone as a base resin.
Crosslinked resin particles are produced by suspending 100 parts by weight of particles of the propylene random copolymer, 0.05 to 5 parts by weight of an organic peroxide as a crosslinking agent, 0.01 to 10 parts by weight of a dispersant, and 0.05 to 5 parts by weight of divinylbenzene in water, and heating the aqueous suspension to a temperature at which the resin particles are impregnated with the crosslinking agent and divinylbenzene and crosslinked. Alternatively, they can be obtained by kneading 0.2 to 1 part by weight of p,p'-dibenzoyl quinonedioxime into 100 parts by weight of the propylene random copolymer at a temperature below the decomposition temperature of p,p'-dibenzoyl quinonedioxime, then converting the mixture into particles, introducing 100 parts by weight of the resulting particles, 0.05 to 5 parts by weight of a crosslinking agent and 0.01 to 10 parts by weight of a dispersing agent into a closed vessel, and heating the mixture with stirring to a temperature at which the resin particles are impregnated with the crosslinking agent and crosslinked.
Prefoamed particles are produced by dispersing 100 parts by weight of the crosslinked propylene random copolymer particles obtained as above, 5 to 50 parts of a blowing agent and 0.1 to 10 parts by weight of a dispersing agent in a dispersion medium such as water in a closed vessel, heating the mixture with stirring to impregnate the copolymer particles with the blowing agent, opening one end of the vessel while the pressure of the inside of the vessel is maintained constant by using nitrogen gas or the like at a predetermined temperature, and releasing the copolymer particles and the dispersion medium into an atmosphere (usually under atmospheric pressure) having a lower pressure than the pressure of the inside of the vessel, thereby expanding the copolymer particles. The gel fraction of the prefoamed particles can be adjusted to a suitable value within the range of 1 to 65% by adjusting the amounts of the crosslinking agent and the crosslinking aid during the crosslinking. As stated hereinabove, the gel fraction of the prefoamed particles still remains unchanged even when they have been foamed and fused under heat within a mold to produce a molded article.
The blowing agent used in the prefoaming is usually a volatile organic blowing agent. Examples include aliphatic hydrocarbons such as propane, butane, pentane, hexane and heptane; cycloaliphatic hydrocarbons such as cyclobutane and cyclopentane; and halogenated hydrocarbons such as trichlorofluoromethane, dichlorodifluoromethane, dichlorotetrafluoroethane, methyl chloride, ethy chloride and methylene chloride. These blowing agents may be used as a mixture. The amount of the blowing agent used is about 0.04 to 0.20 mole per 100 g of the propylene-type resin particles. An inorganic blowing agent such as carbon dioxide may also be used either alone or with the organic blowing agent. The amount of the inorganic blowing agent added is 5 to 50 parts by weight per 100 parts by weight of the copolymer particles. When the inorganic blowing agent is used for the foaming of a non-crosslinked propylene-type resin, the resulting cells tend to become small. But when it is used for the expanding of a crosslinked propylene random copolymer, there is no likelihood of the cells becoming too small.
Illustrative of the dispersing agent are fine particulate aluminum oxide, titanium oxide and basic zinc carbonate. Its amount is generally 0.1 to 10 parts by weight per 100 parts by weight of the copolymer particles.
The expanding temperature at which the copolymer particles are prefoamed by releasing them from the closed vessel is preferably at least Tm-10 (.degree.C) in which Tm is the temperature at which the propylene random copolymer particles before crosslinking have been melted. (Tm is determined as follows: By using a differential scanning calorimeter, the sample (6 to 8 mg) is heated to 220.degree. C. at a rate of 10.degree. C./min., then cooled to about 40.degree. C. at a rate of 10.degree. C./min., and again heated to 220.degree. C. at a rate of 10.degree. C./min. Tm is defined as the temperature at which the bottom of the endothermic peak of the DSC curve obtained by the second temperature elevation has returned to the position of the base line on a higher temperature side.) If the foaming temperature is below Tm-10 (.degree.C.), prefoamed particles cannot be obtained, or prefoamed particles having a nonuniform expansion ratio are obtained.
The prefoamed particles can be further expanded in order to increase their expansion ratio. This may be effected by a method which comprises pressurizing the prefoamed particles obtained as above with an inorganic gas such as air or nitrogen and/or the volatile blowing agent described above to apply an internal pressure higher than the atmospheric pressure, and thereafter heating the prefoamed particles at a temperature above their softening temperature. This additional expanding step may be repeated a plurality of times.
The prefoamed particles of this invention obtained as above usually have an apparent expansion ratio of 3 to 100.
The molded article of the invention can be obtained by filling the prefoamed particles having imparted thereto post-expanding ability in a mold, and molding them under heat.
Since the prefoamed crosslinked propylene-type resin particles of the invention are produced by using as a base resin the propylene random copoymer whose amount of heat of crystallization is 19 to 10 cal/g and by the crosslinking of the base resin, the gel fraction of the prefoamed particles or the foamed article is adjusted to 1 to 65%, the prefoamed particles have excellent post-expanding ability and can be easily molded within a mold without the need to supply steam having so high a pressure.
The molded article finally obtained from the prefoamed particles of this invention shows excellent fusion among the particles, is free from surface unevenness, and has excellent strength and rigidity.
The following Examples and Comparative Examples illustrate the present invention in more detail.
All parts in these examples are by weight.

EXAMPLES 1-3 AND COMPARATIVE EXAMPLE 1
One hundred parts of particles of ethylene/propylene random copolymer (Tm=155.degree. C.) having an amount of heat of crystallization of 15.5 cal/g, 0.3 part of fine particulate aluminum oxide as a dispersing agent and each of the crosslinking agents and crosslinking aids shown in Table 1 in the amounts indicated were suspended in 300 parts of water (p,p'-dibenzoyl quinonedioxime had been incorporated in the resin particles beforehand). The suspension was heated to 100.degree. C. with stirring, and maintained at this temperature for 1 hour. Furthermore, it was maintained at each of the temperatures indicated in Table 1 for each of the periods of time indicated in Table 1 to crosslink the polymer particles.
A closed vessel was then charged with 100 parts of the crosslinked resin particles, 300 parts by weight of water, 0.3 part of fine particulate aluminum oxide and 17 parts of dichlorodifluoromethane. With stirring, these materials were heated to each of the temperatures shown in Table 1 to impregnate the resin particles with the blowing agent. At the same temperature, one end of the vessel was opened while maintaining the internal pressure of the vessel at 30 kg/cm.sup.2 -G with nitrogen gas, and the resin particles and water were released into the open atmosphere. Thus, the resin particles were expanded to give prefoamed resin particles. The gel fraction and the internal pressure reducing speed coefficient k of the resulting prefoamed particles are shown in Table 1. Table 1 also shows the E.sup.1/3 .times.n.sup.1/2 value of the prefoamed particles calculated from the true expansion ratio E and the number of cells per mm.sup.2.
The prefoamed particles were then pressurized with air to impart an internal pressure of 1.5 kg/cm.sup.2 -G, then filled in a mold having an inside size of 300 mm.times.300 mm.times.50 mm, and heated with steam under 3.3 kg/cm.sup.2 -G to expand and fuse them to one another and to obtain a molded article. The properties of the molded article are shown in Table 2.
Comparative Example 1 shows the production of prefoamed particles having a gel fraction and an E.sup.1/3 .times.n.sup.1/2 value outside the scope of this invention, and an in-mold foamed article prepared therefrom. The results are also shown in Tables 1 and 2.
COMPARATIVE EXAMPLE 2
The same ethylene/propylene random copolymer particles as used in Examples 1 to 3 were not crosslinked but directly expanded by the same method as described in Examples 1 to 3 to form prefoamed particles. The properties of the prefoamed particles are also shown in Table 1. The prefoamed particles were then molded with steam under a pressure of 4 kg/cm.sup.2 -G (which is industrially feasible) in the same way as in Examples 1 to 3 to obtain a molded article. The properties of the molded article are also shown in Table 2.
EXAMPLES 4-7 AND COMPARATIVE EXAMPLES 3-4
One hundred parts of the resin particles indicated in Table 3, 0.48 part of dicumyl peroxide as a crosslinking agent and 0.6 part of divinylbenzene as a crosslinking aid were suspended in 300 parts of water. The suspension was heated to 100.degree. C. with stirring and maintained at this temperature for 1 hour. Then, it was heated to 150.degree. C. and maintained for 1 hour to crosslink the resin particles. The crosslinked resin particles were expanded in the same way as in Examples 1 to 3 using each of the blowing agents indicated in Table 3 to obtain prefoamed particles. The properties of the prefoamed particles are shown in Table 3.
The prefoamed particles were then molded in the same way as in Examples 1 to 3 to obtain a molded article. The properties of the molded article are shown in Table 4.
Comparative Examples 3 and 4 show the use of resin particles having the amount of heat of crystallization outside the scope of the invention. The results are also shown in Tables 3 and 4.
As a reference, the properties of a molded article of crosslinked low-density polyethylene (Mirablock, a brand name for a product of Japan Styrene Paper Co., Ltd.) are also shown in Table 4.
EXAMPLES 8-10
One hundred parts of mixed resin particles having each of the compositions indicated in Table 5, 0.3 part of fine particulate aluminum oxide and each of the crosslinking agents and crosslinking aids shown in Table 5 in the amounts indicated were suspended in 300 parts of water. The suspension was maintained at 100.degree. C. for 1 hour, and further maintained for 1 hour at each of the temperatures indicated in Table 5 to crosslink the resin particles. The crosslinked resin particles were expanded in the same way as in Examples 1 to 3 to obtain prefoamed particles. The properties of the resulting prefoamed particles are also shown in Table 5.
The prefoamed particles were molded in the same way as in Examples 1 to 3 to obtain a molded article. The properties of the molded article are shown in Table 6.
TABLE 1__________________________________________________________________________ Ex- Prefoamed particles Crosslinking conditions panding Ex- Crosslinking agent Crosslinking aid Temper- temper- Gel pansion Amount Amount ature ature fraction k E.sup.1/3 .times. n.sup.1/2 ratio Type (parts) Type (parts) (.degree.C.) (.degree.C.) (%) (l/hr) value (E)__________________________________________________________________________Example 1 Dicumyl 0.48 p,p'-Dibenzoyl 0.3 150 .times. 1 hr 150 5 0.28 3 19.4 peroxide quinoneoxime 2 Dicumyl 0.48 Divinylbenzene 0.3 140 .times. 3 hr 152 30 0.18 10 20.0 peroxide 3 Dicumyl 0.48 Divinylbenzene 2.0 150 .times. 1 hr 152 45 0.21 40 18.8 peroxideComparative 1 Dicumyl 0.48 p,p'-Dibenzoyl 0.9 160 .times. 30 min 153 68 0.31 50 20.6Example peroxide quinoneoxime 2 -- -- -- -- -- 145 0 0.22 15 18.8__________________________________________________________________________
TABLE 2__________________________________________________________________________ Dimensional Compression Expansion Dimensional change upon hardness Compression Water Surface ratio of accuracy heating (%) (g/cm.sup.2 -G) set (%) absorption condition the foamed (*1) (*2) (*3) (*4) (*5) (*6) article__________________________________________________________________________Example 1 O -2.0 1.2 7.0 O O 30 2 O -1.5 1.3 5.5 O O 31 3 O -1.2 1.3 5.0 O O 30Comparative 1 .DELTA. -1.2 1.3 8.8 X X 32Example 2 O -2.6 1.2 9.0 O O 30__________________________________________________________________________
TABLE 3__________________________________________________________________________ Ex- Prefoamed particles panding Ex- Propylene random copolymer Blowing agent temper- Gel pansion Tm Amount ature fraction k E.sup.1/3 .times. n.sup.1/2 ratio Type(*) (.degree.C.) Type (parts) (.degree.C.) (%) (1/hr) value (E)__________________________________________________________________________Example 4 Ethylene/propylene 165 Dichloro- 15 165 29 0.28 25 19.4 random copolymer difluoro- (18.9 cal/g) methane 5 Ethylene/propylene 158 Dichlorodifluoro- 10 155 35 0.23 30 20.0 random copolymer methane & (18.4 cal/g) carbon dioxide 5 6 Ethylene/propylene 153 carbon dioxide 12 160 40 0.21 35 18.1 random copolymer (15.5 cal/g) 7 Propylene/1-butene 155 Dichloro- 15 150 39 0.18 10 18.9 random copolymer difluoro- (12.3 cal/g) methaneComparative 3 Propylene/1-butene 145 Dichloro- 16 145 38 0.23 15 18.8Example random copolymer difluoro- (8.9 cal/g) methane 4 Ethylene/propylene 165 Dichloro- 16 165 25 0.28 35 17.5 random copolymer difluoro- (20 cal/g) methane__________________________________________________________________________ (*)The parenthesized figures show the amount of heat of crystallization
TABLE 4__________________________________________________________________________ Compression Dimensional hardness Compression Water Surface Fused accuracy (g/cm.sup.2 -G) set (%) absorption condition Expansion condition (*1) (*3) (*4) (*5) (*6) ratio (*7)__________________________________________________________________________Example 4 O 1.8 7.6 O O 31 .DELTA. 5 O 1.6 6.2 O O 31 O 6 O 1.2 5.6 O O 29 O 7 O 0.8 4.2 O O 30 OComparative 3 .DELTA. 0.7 5.1 O O 30 OExample 4 O 1.8 8.3 O O 28 XReference .DELTA. 0.65 3.9 O O 26 O__________________________________________________________________________
TABLE 5__________________________________________________________________________ Crosslinking Conditions Cross- Ex- linking agent Crosslinking aid Tem- Prefoamed particles Ex- pandingResin composition A- A- per- Gel pansion temper-Ex- Amount mount mount ature fraction k E.sup.1/3 .times. n.sup.1/2 ratio atureample Type(*) (wt. %) Type (parts) Type (parts) (.degree.C.) (%) (1/hr) value (E) (.degree.C.)__________________________________________________________________________8 Ethylene/propylene 70 Dicumyle 0.48 Divinyl- 0.8 150 43 0.23 18 17.5 150 random copolymer perpxide benzene (15.5 cal/g) Ethylene/propylene 30 rubber9 Ethylene/propylene 90 Dicumyl 0.48 Divinyl- 0.6 150 38 0.26 10 15.6 150 random copolymer peroxide benzene (15.5 cal/g) High-density 10 polyethylene10 Propylene/1-butene 90 Dicumyl 0.48 Divinyl- 0.6 150 36 0.20 25 21.1 160 random copolymer peroxide benzene (14.5 cal/g) Ethylene/propylene 10 block copolymer having an ethylene content 20 wt. %__________________________________________________________________________ (*)The parenthesized figures show the amount of heat of crystallization.
TABLE 6__________________________________________________________________________ Compression Dimensional hardness Compression Water SurfaceEx- accuracy (g/cm.sup.2 -G) set (%) absorption condition Expansionample (*1) (*3) (*4) (*5) (*6) ratio__________________________________________________________________________8 O 0.7 2.9 O O 289 O 1.0 5.8 O O 2410 O 0.9 6.0 O O 33__________________________________________________________________________(*1): Dimensional accuracyEvaluated as follows by the shrinkage of amolded article molded in a mold having an inside size of300 mm .times. 300 mm .times. 50 mm, with respect to the planardirection of the mold.O: the shrinkage is less than 3%.DELTA.: the shrinkage is 3 to less than 4%X: the shrinkage is at least 4%(*2): Dimensional change upon heatingMeasured at 110.degree. C. in accordance with JISK-6767.(*3): Compression hardnessMeasured in accordance with JIS K-6767.(*4): Compression setMeasured in accordance with JIS K-6767.(*5): Water absorptionMeasured in accordance with JIS K-6767B, andevaluated as follows:O: the water absorption is less than 0.003 g/cm.sup.2.DELTA.: the water absorption is from 0.003 to less than 0.03 g/cm.sup.2X: the water absorption is at least 0.03 g/cm.sup.2(*6): Surface conditionThe surface of the molded article is observed,and the surface condition is evaluated as follows:O: the surface is smooth with very littleunevennessX: the surface has poor smoothness with greatunevenness(*7): Fused conditionThe molded article is broken by pulling, andthe fractured condition of its fractured surface isobserved. The fused condition is evaluated as follows:X: at least 70% of the article is broken amongthe particles(not acceptable).DELTA.: less than 70% to 40% of the article isbroken among the particles(acceptable without any particular problem)O: less than 40% of the article is brokenamong the particles(acceptable with no problem)
EXAMPLES 11-16 AND COMPARATIVE EXAMPLES 5-8
A closed vessel was charged with 100 parts of particles of each of the ethylene/propylene random copolymers shown in Table 7, 300 parts of water, 0.3 part of fine particulate aluminum oxide, and each of the crosslinking agents and crosslinking aids shown in Table 7, and with stirring, these materials were maintained at 100.degree. C. for 1 hour. Then, the suspension was further maintained at 150.degree. C. for 1 hour to crosslink the copolymer particles. The gel fraction of the resulting crosslinked resin particles is shown in Table 7. When p,p'-dibenzoyl quinonedioxime was used as the crosslinking aid, it was kneaded into the resin particles before charging into the closeed vessel.
One hundred parts of the resulting crosslinked resin particles, 300 parts of water, 0.3 part of fine particulate aluminum oxide and each of the blowing agents indicated in Table 7 were blended in a closed vessel, and with stirring, the mixture was heated to each of the temperatures shown in Table 7 to impregnate the resin particles with the blowing agent. Then, one end of the closed vesssel was opened, and the resin particles and the dispersion medium were released into the open atmosphere to obtain prefoamed resin particles. The expansion ratio and the number of cells of the resulting prefoamed resin particles were measured, and are shown in Table 7.
The prefoamed resin particles were pressurized with air to impart an internal pressure of 1.5 kg/cm.sup.2 -G to the particles, filled in a mold, and molded by heating them with steam under a pressure of 2.5 to 4 kg/cm.sup.2 -G. The resulting molded article was aged in an oven at 80.degree. C. for 24 hours, and then the shrinkage, flexibility, surface condition, surface protecting property, dimensional change upon heating, compression hardness and compression set of the molded article were measured. The results are shown in Table 8.
Comparative Examples 5 to 8 were outside the scope of the invention in respect of the olefin component (No. 5), gel fraction (No. 6) and N.sup.1/2 /d.sup.1/3 value (Nos. 7 and 8). The results are shown in Tables 7 and 8.
Table 8 also shows the properties of non-crosslinked expanded articles obtained from the materials used in Examples 12 and 13 (Comparative Examples 9 and 10). These results demonstrate the superiority of the crosslinked expanded articles to the non-crosslinked expanded articles in respect of dimensional change upon heating, compression hardness and compression set.
TABLE 7__________________________________________________________________________ Ethylene propylene random copolymer Crosslinking conditions Amount of heat of Crosslinking agent Crosslinking aid Ethylene content crystallization Amount Amount Gel fraction (wt. %) (cal/g) Type (parts) Type (parts) (%)__________________________________________________________________________Example 11 1.5 17.2 Dicumyl peroxide 0.48 Divinylbenzene 0.15 25 12 2.8 16.8 " 0.68 Divinylbenzene 0.2 33 13 4.2 15.8 " 0.72 Divinylbenzene 0.2 35 14 4.2 15.8 " 0.48 p,p'-Dibenzoyl 0.3 5 quinonedioxime 15 4.2 15.8 " 0.48 p,p'-Dibenzoyl 0.8 60 quinonedioxime 16 5.3 11.0 " 0.48 Divinylbenzene 0.5 41Comparative 5 0.8 17.8 " 0.48 Divinylbenzene 0.3 30Example 6 4.2 15.8 " 0.48 p,p'-Dibenzoyl 0.9 70 quinonedioxime 7 4.2 15.8 " 0.72 Divinylbenzene 0.2 35 8 4.2 15.8 " 0.72 Divinylbenzene 0.2 35 9 2.8 16.8 -- -- -- -- -- 10 4.2 15.8 -- -- -- -- --__________________________________________________________________________ Prefoamed particle Blowing agent Expanding Expansion ratio Number of cells Type Amount (parts) temperature (.degree.C.) (E) (n) E.sup.1/3 .times. n.sup.1/2__________________________________________________________________________ valueExample 11 Dichlorodifluoro- 18 160 25 26 15 methane 12 Carbon dioxide 10 155 19 260 43 13 Dichlorodifluoro- 10 150 17 94 25 methane & carbon dioxide 5 14 Dichlorodifluoro- 10 150 28 24 15 methane & trichlorofluoromethane 10 15 Dichlorodifluoro- 8 157 22 11 3 methane & trichlorofluoromethane 8 16 Dichlorodifluoro- 10 145 9 208 30 methane & carbon dioxide 5Comparative 5 Dichlorodifluoro- 16 155 19 88 25Example methane 6 Dichlorodifluoro- 18 150 19 224 40 methane 7 Dichlorodifluoro- 20 148 25 292 50 methane 8 Dichlorodifluoro- 8 155 22 0.29 1.5 methane & trichlorofluoromethane 8 9 -- -- -- -- -- -- 10 -- -- -- -- -- --__________________________________________________________________________
TABLE 8__________________________________________________________________________ Dimen- sional Dimen- Surface change Compres- Surface Compres- Overall- Number sional Flexi- condi- upon sion protect- sion evalu- Expansion of cells accuracy bility tion heating hardness ability set ation ratio (N) N.sup.1/2 /d.sup.1/3 (*8) (*9) (*10) (*11) (*12) (*13) (*14) (*15)__________________________________________________________________________Example 11 40 19 15.4 O O O -0.8 2.0 O O O 12 30 191 44.5 O O O -1.3 1.8 O O O 13 27 69 25.8 O O O -1.5 1.4 O O O 14 45 18 15.6 O O O -2.0 0.8 O O O 15 35 0.84 3.1 O O O -1.5 1.3 O O O 16 15 148 31 O O O -2.0 2.6 O O OComparative 5 30 15 25.9 O X O -0.5 2.0 O O XExample 6 30 166 41.5 O O X -1.5 1.4 O O X 7 38 221 51.8 X .DELTA. O -3.1 0.8 O .DELTA. X 8 35 0.21 1.6 O O .DELTA. -1.6 1.3 X O X 9 30 -- -- -- O O -2.2 1.5 O .DELTA. -- 10 27 -- -- -- O O -2.7 1.2 O .DELTA. --__________________________________________________________________________(*8): Dimensional accuracySame as the note (*1) to Table 1.(*9): FlexibilityA rectangular parallelpipedal sample, 20 mm .times.40 mm .times. 300 mm, cut out from the molded article is bent,and the angle of bending which causes breakage of thesample is measured. The flexibility is evaluated asfollows:O: Not broken even when the angle is at least135.degree..DELTA.: Broken when the angle is at least 90.degree.and less than 135.degree.X: Broken when the angle is less than 90.degree.(*10): Surface conditionEvaluated as follows by the number of depressedportions at least 2 mm deep from the surface per 50 mm .times.50 mm.O: not more than 2.DELTA.: 3 to 5X: 6 or more(*11): Dimensional change upon heatingSame as the note (*2) to Table 1.(*12): Compression hardnessSame as the note (*3) to Table 1.(*13): Surface protectabilityThe occurrence of injury on the surface of adecorative sheet of a melamine resin or the like byrubbing it with the molded particle was observed, and thesurface protectability is evaluated as follows:-O: No injuryX: Injury occurred(*14): Compression setMeasured in accordance with JIS K-6767, andevaluated as follows:O: less than 8%.DELTA.: 8 to 15%X: more than 15%(*15): Overall evaluationO: excellent in regard to all of the abovepropertiesX: inferior in regard to at least one of theabove properties
The results in the foregoing Examples demonstrate that the molded articles of the invention comprising the crosslinked ethylene/propylene random copolymers have excellent properties in regard to shrinkage, flexibility, surface condition, dimensional change upon heating, compression hardness, surface protectability, compression set, etc.

Number	Name	Date
4379859	Hirosawa et al.	Apr 1983
4399087	Akiyama et al.	Aug 1983
4415680	Ushirokawa	Nov 1983
4436840	Akiyama et al.	Mar 1984
4448901	Senda et al.	May 1984
4464484	Yoshimura et al.	Aug 1984
4504534	Adachi et al.	Mar 1985

Prefoamed particles of crosslinked propylene-type resin and molded article prepared therefrom

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