CA1171620A - Method for manufacturing low density rubber foamed body - Google Patents
Method for manufacturing low density rubber foamed bodyInfo
- Publication number
- CA1171620A CA1171620A CA000383063A CA383063A CA1171620A CA 1171620 A CA1171620 A CA 1171620A CA 000383063 A CA000383063 A CA 000383063A CA 383063 A CA383063 A CA 383063A CA 1171620 A CA1171620 A CA 1171620A
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- Prior art keywords
- mold
- weight
- parts
- rubber
- foamed body
- Prior art date
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Abstract
Abstract of the Disclosure A method for manufacturing a low density rubber foamed body is provided which comprises the steps of forming a sheet from a mixture of 100 parts by weight of natural rubber or a synthetic rubber, 10 to 80 parts by weight of a foaming agent, and 0.5 to 15% by weight of a crosslinking agent; enclosing said sheet within a mold and heating said mold under pressure from the exterior to thereby foam said sheet; forcibly cooling said mold; and releasing a foamed body from said mold.
When 10 to 60 parts by weight of a thermoplastic synthetic resin are further added to the mixture, a rubber foamed body of still lower density and lower shrinking property is obtained.
When 10 to 60 parts by weight of a thermoplastic synthetic resin are further added to the mixture, a rubber foamed body of still lower density and lower shrinking property is obtained.
Description
7~
Background of the Invention The present invention relates to a method for manufacturing a low density foamed body containing rubber as a main constituent.
A conventional method for manufacturing foamed rubber is known according to which a mixture containing rubber,~a foaming agent, and a crosslinking agent is fed into a mold, the mold is heated to foam the mixture, and the produced foamed body is released from the mold.
However, with a foamed body manufactured according to this method, an expansion ratio of only about 3 to 6 and a density of about 0.15 to 0.3 are obtainable. It has thus been difficult with this method to either increase the expansion ratio or to decrease the density.
When the foaming agent is used in a great amount to raise the expansion ratio, the foaming pressure within the mold rises excessively when the mold is heated.
Then, when the mold is opened, the foamed body immedi-ately expands, explodes, and is scattered away.
Summary of the Invention~ ;~
It~is an object o the present invention to provide a method for manufac~uring a low density rùbber~foamed body.~ ~
It is another ob~ect of the present invention to provide a method~for~manufacturing a rubber foamed body which has a low density as well as a low shrinking property.
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.
In order to achieve these and other objects, khere is provided according to the present invention, a method for manufacturing a low density rubber foamed body com-prising the steps of forming a sheet or sheets from a mixture of 100 parts by weight of natural rubber or a synthetic rubber, 10 to 80 parts by weight of a foaming agent, and 0.5 to 15 parts by weight of a crosslinking agent; enclosing said sheet or sheets within a mold so as substantially to fill the mold, and heating said mold under pressure from the exterior to thereby foam said ~sheet or sheets; forcibly cooling said mold; and releas-ing a foamed body from said mold. When 10 to 60 parts by weight of a thermoplastic synthetic resin are further added to the mixture in the method of the present inven-tion described above, a rubber foamed body of low densityand low shrinking property is obtainable.
In accordance with the present invention, a large amount of the foaming agent may be used while preventing the drawbacks of the prior art technique such as explosion or scattering of the foamed body when the mold is opened, so that a low density rubber foamed body may be provided.
A lower shrinking property may be achieved by further adding a thermoplastic synthetic resin to the raw material mixture containing natural or the synthetic rubber, the foaming agent and the crosslinking agent.
The low densit~ rubber foamed bodies obtained according to the present inven-tion are preferably used for various kinds of cushion materials, substitutes for springs, buoys, automobile partsl heat insulators, impact absorbers, and so on.
Detailed Description of the Preferred Embodiments The raw material rubber to be used in this inven-tion may be natural rubber or any kind o synthetic rubber.
Examples of such synthetic rubbers include acrylonitrile-butadiene rubber (NBR), chIoroprene rubber (CR),isoprene rubber (IR), styrene-butadiene rubber (SBR), and ethylene-propylenediene copolymer rubber (EPDM).
The foaming agent to be mixed with the rubber material : .
.,~
- , : .
- : , , , , ~ , - ~ . . , ' ` ~ , :
may be any foaming agent which is used for manufacturing conventional rubber foamed bodies and may, for example, include azodicarbonamide, dinitrosopentamethylenetetramine, p-toluenesulfonylhydrazine, azobisisobutyronitrile, diazoaminobenzene, and toluenesulfonyl semicarbazide.
The foaming agent is used in the amount of 10 to 80 parts by weight based on 100 parts by weight of the raw material rubber, although the preerred amount varies depending upon the kind of natural or synthetic rubber to be used as the main constituent and the density of the desired foamed body. When this amount is smaller than 10 parts by weight, a sufficiently highly foamed body may not be obtained. When this amount exceeds 80 parts by weight, the foamed body may cause breakdown, or a foamed body having adequate impact resilience may not be obtained. The method also requires a crosslinking agent in addition to the foaming agent. Preferable crosslinking agents may include sulfur, zinc oxide, and organic peroxides. Examples of organic peroxides may include dicumylperoxide, 2,5-dimethyl-2,5 di(tert.-butyl)peroxide, 1,3-bis(tert.-butylperoxy-isopropyl)benzene, m-octaldecylazidoformate, and tert.-butylperoxycumene. Although the amount of the crosslinking agent as mentioned above may differ depending upon the raw material rubber used, the kind and amount of foaming agent used and other conditions, it is preferably within the range of 0.5 to 15 parts by weight based on 100 parts of the raw material rubber.
In addition to the foaming agent and the crosslinking agent, various other additives may optionally be added. `
For example, there may be added a filler such as carbon black, clay, and calcium carbonate; a foaming auxiliary such as urea, stearic acid, lauric acid, and salicylic acid; a metal oxide such as zinc oxide; and a colorant.
An antioxidant may also be included. The thermoplastic synthetic resin preferably used in the present invention may include polyethylene, polypropylene, polystyrene, .~..
.
, ~ ' ,' ' .
polyvinyl chloride, an ethyl~ne-vinyl acetate copolymer resin, a polyamide resin and an acrylic resin. If the amount of the thermoplastic synthetic resin does not reach 10 parts by weight, satisfactory prevention of shrinkage may not be achieved. If this amount exceeds 60 parts by weight, the rubbery resilience is degraded, resulting in an unsatisfactory product.
The raw material mixture is well kneaded in a kneader such as a roll or a mixer and is formed into a sheet. For kneading the raw material, the components other than the crosslinking agent are first well kneaded with a roll at a surface temperature of 20 to 120C for about 15 to 60 minutes. After the crosslinking agent is added to the mixture, further kneading is performed for 5 minutes to provide a final raw material rubber sheet. Although the rubber sheet must have a thickness such that it may be put in a mold, a plurality of such rubber sheets may also be put in a single mold. There-fore, the thickness of the rubber sheet need not be the same as the size of the cavity of the mold.
The raw material rubber sheet thus obtained is p aced in a mold, the lid of the mold is closed, and the mold is pressed from the upper and lower sides.
The raw material rubber sheet is placed in the mold so that the rubber sheet substantially fills the cavity of the mold. The shape of the mold may oe arbitrary.
However, after the mold is heated under pressure for foaming the sheet and the mold is opened, the foamed body abruptly pops out of the mold while expanding in volume. Therefore, the mold preferably does not have ~-projections within the cavity and has an upwardly flared opening. ~or pressing the mold from the upper and lower sides thereof, a press machine may be used.
According to a further preferable method, the upper and lower halves of the mold are prefixed to the press machine, and the opening and closing of the mold is performed by vertically displacing these upper and '.:'" ' . "' ' " '': ", ., .,.. ,,.~, ' , .
- 5 - ~ ~7~
lower halves. When placiny the raw material rubber sheet which has been subjected to kneading into the mold, the sheet need not be aged in advance. Thus, the sheet may be placed directly in the mold where it is subjected to heat and pressure according to the present invention.
According to the conventional method for manufacturing the rubber foamed body, in order to foam the rubber sheet which has been kneaded, aging for about 24 hours has been required before the sheet may be heated under pressure as an essential step of the method. However, this aging step is not necessary according to the present invention.
Even when the raw material rubber sheet is subjected to the foaming step immediately after kneading, phenomena such as foam nonuniformity and breakdown do not occur, and continuous production is possible. After the raw material has been placed within the mold, the mold is then heated under pressure for crosslinking and foaming.
Although the heating temperature is mainly determined by the decomposition temperature of the foaming agent used, it is usually 130 to 200C. The pressure exerted on the mold is typically within a range of 100 to 200 kg/cm2.
After foaming has proceeded substantially, the mold is cooled. The cooling temperature changes according to the raw material rubber used, the kind and amount of the foam-ing agent used, the kind and amount of the crosslinking agant used, and other conditions. ~owever, typically it is within the range of about 50 to 100C. The cooling step utilizes forcible cooling rather than natural cooling and may, for example, adopt the process of circulating water through the jacket of the mold. Circulation of air may alternatively be adopted for this purpose. As this cooling is performed, the gas pressure generated within the mold during the heating and foaming step is reduced and the bonding between the polymer molecules is also sufficiently maintained. The mold is then opened. Upon opening the .....
, .
' mold, the rubber foamed body pops out of tlle mold without exploding, ~nd the volume of the foamed body instantaneously increases more than about 15 times the original volume. Thus, the low density rubber foamed body of the present invention is obtained. The density of the resultant rubber foamed body is reduced to about 0.12 or lower.
The present invention will be more clearly under-stood from the ~ollowing description made with reference to the examples.
Example 1 Acrylonitrile-butadiene rubber (NBR) 100 parts by weight Carbon black 20 parts by weight Stearic acid 3.0 parts by weight Process oil 10 parts by weight Dioctylphthalate 10 parts by weight Azodicarbonamide 25 parts by weight Zinc oxide 5 parts by weight Antioxidant (*) 1.5 parts by weight Sulfur 0.5 part by weight * 2,2,4-trimethyl-1,2-dihydroquinoline The components above excluding sulfur were kneaded-for S5 minutes with a roll having a surface temperature of 30C. Sulfur was then added, and the mixture was kneaded for 5 minutes to provide a rubber sheet 5 mm in thickness. The sheet was cut into pieces of appropriate size. Three such pieces were placed in a mol~ having a cavity 150 mm in length, 230 mm in width, and 12 mm in depth. After closing the mold with a lid, the mold was pressed from the upper and lower sides thereof at a pressure of 170 kg/cm2 with a press machine. Heated vapor was introduced in the jacket of the mold to heat the sides of the mold to 170C, and the mold was kept at this temperature for 10 minutes. The heated vapor in the jacket was removed; and water was then introduced.
After 5 minutes, the mold temperature was ~5C. The ,. ..
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mold was then opened, and the ~oamed body immediately popped out of the mold, providing the Eoamed body of the present invention. The density of this foamed body was 0.031. The outer appearance of the foamed body corresponded to that of the cavity of the mold, and no cracks or explosions were observed. The cushion property and resilience of the foamed body were excellent.
Example 2 Chloroprene rubber 100 parts by weight Carbon black 20 parts by weight Stearic acid 3.0 parts by weight Dioc-tylphthalate 10 parts by weight ~zodicarbonamide 16 parts by weight Zinc oxide 7 parts by weight Antioxidant (*) 1.0 part by weight Filler (Calcium carbonate)10 parts by weight Magnesia 4.0 parts by weight * N-phenyl-N'-isopropyl-p-phenylenediamine A rubber sheet 5.5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 40 minutes and the roll temperature was 40C. This rubber sheet - was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example 1.
Ths heating temperature was 170C, the pressure was 170 kg/cm2, and the heating time was 8 minutes. The mold was cooled in a simiIar manner as in Example 1.
The cooling time was 5 minutes and the temperature of the mold after cooling was 85C.
The press machine was released and a low density foamed body of 0.050 density was instantaneously obtained.
The outer appearance of the obtained foamed body was the same as in Example 1. The foamed body had excellent 1mpact resilience.
.
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Example 3 Styrene-butadiene rubber (SBR~ 100 parts by weight Carbon black40 parts by weight Stearic acid3.0 parts ~y weight Process oil20 parts by weight Azodicarbonamide18 parts by weight zinc oxide 5 parts by weight Antioxidant (*)1.5 parts by weight Sulfur 1.2 parts by weight * N-phenyl-N'-isopropyl-p-phenylenediamine A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 30 minutes and the roll temperature was 40C. The rubber sheet was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example 1. The heating temperature was 150C, the pressure was 170 kg/cm2, and the heating time was 12 minutes. The mold was cooled.in a similar manner as in Example 1.
The cooling time was 12 minutes, and the temperature of the cooled mold was 50C.
When the press machine was released, a low density foamed body of 0.044 density was instantaneously obtained.
The outer appearance and impact resilience were like those of the foamed body obtained in Example 1.
Example 4 Isoprene rubber (IR)100 parts by weight Carbon black40 parts by weight Stearic acid3.0 parts by weight Process oil. 20 parts by weight Azodicarbonamide18 parts b~ weight Zinc oxide 5 parts by weight Antioxidant (*)1.5 parts by weight Sulfur 1.2 parts by weight * N-phenyl-N'-isopropyl-p-phenylenediamine :
A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 20 minutes and the roll temperature was 50C. The rubber sheet was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example l. The heating temperature was 160C, the pressure was 170 kg/cm2, and the heating time was 8 minutes. The mold was then cooled in a similar manner as in Example 1, except that the cooling time was 7 minutes and the temperature of the cooled mold was 80C.
The press machine was then released, thus providing a low density foamed body of 0.032 density. The obtained foamed bod~ had an outer appearance and impact resilience comparable to those of the foamed body obtained in Example 1.
Example 5 Ethylene-propylenediene copolymer rubber 100 parts by weight Carbon black 15 parts by weight Stearic acid 2.0 parts by weight Process oil 10 parts by weight Azodicarbonamide 25 parts by weight Zinc oxide 5 parts by weight Dicumylperoxide 5.3 parts by weight A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 30 minutes and the roll temperature was 50C. The rubber sheet was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example 1. The heating temperature was 165C, the pressure was 170 kg/cm2, and the heating time was 14 minutes. The mold was then cooled in a similar manner as in Example l, except that the cooling time was 3 minutes and the . .~
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temperature o~ the cooled mold was 100C.
The press machine was released and a low density foamed body of 0.033 density was instantaneously obtained.
Example 6 Ethylene-propylenediene copolymer rubber 100 parts by weight Carbon black 15 parts by weight Stearic acid 2.0 parts by weight Process oil 15 parts by weight Azodicarbonamide 35 parts by weight Zinc oxide 3.0 parts by weight Dicumylperoxide 5.3 parts by wei~ht A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 30 minutes and the roll surface temperature was 50C. The rubber sheet was cut into pieces o~ predetermined size. Three such pieces were placed in a mold and the mold was cooled in a similar manner an in Example 1, except that the cooling time was 10 minutes and the temperature of the cooled mold was 90C.
The press machine was released and a low density foamed body of 0.02 density was instantaneously obtained~
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,. . ' ' Rubber sheets 2 mm in thickness were obtained from the above compositions by kneading at 50C for composi-tion A and at 100C for composition B. The kneading time was 25 minutes in each case. The two rubber sheets were separately placed into molds having dimensions of 25 cm x 25 cm x 1.5 cm and having an opening flaring at an angle of 60C, to occupy substantially 95~ of the cavity of each mold. The molds were heated and pressed by press machines for 10 minutes at a heating temperature of 170C and a pressure of 150 kg/cm2.
Water was circulated in the jackets of the molds to drop the temperature of the molds to 85C and this temperature was maintained for 6 minutes. The foamed bodies were then released from the molds. The foamed body of the composition A had a density of 0.048, and the foamed body of the composition B had a density of 0.052; neither foamed body exhibited cracks or foam nonuniformity. The shrinkage as measured over time was as follows. For measuring the shrinkage, a mark 10 cm in length was made on the surface of the foamed body immediately after it was released from the mold, and the shrinkage of this line was measured.
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. : : '' '~ ' ' '~ . ': ' ~ 7~;213 Rubber sheets 2 mm in thickness were obtained from the above compositions C and D by kneading the component mixtures at 35C for 35 minutes for both of the composi-tions. The rubber sheets were separately placed in molds as used in Example 7 to fill substantially 95% of the cavities of the molds. After heating the molds at 170C and at a pressure of 150 kg/cm2, cold water was passed through the jackets of the molds to lower the temperature to 85C. The molds were maintained at this temperature for 6 minutes. The foamed bodies were released from the molds. The foamed body of the compo- -sition C had a density of 0.038 and the foamed body of the composition D had a density of 0.04. The outer appearance of the foamed bodies was the same as that of the foamed bodies obtained in Example 7. The shrinkage of the foamed bodies was measured in a similar manner an in Example 7, and the obtained results are shown in Table 2 below:
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Rubber sheets ~ mm in thickness were obtained by kneading the above components at 50C for composition E
and at 110C for composition F for 25 minutes each.
These rubber sheets were placed in molds as used in Example 7 to occupy substantially 95% of the cavities of these molds. The molds were then heated at 170C
and pressed at 150 kg/cm2 for 6 minutes. Cold water was then passed through the jackets of the molds to cool them to 85C. The molds were maintained at this temperature for 6 minutes. The density of the obtained product was 0.07 for the composition E and 0.073 for the composition F. The outer appearance of the foamed bodies was the same as that obtained in Example 7. The shrinkage of the foamed bodies was measured in a similar manner as in Example 7, and the obtained results are - shown in-Table 3 below:
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Rubber sheets 2 mm in thickness were obtained by kneading the above components by a roll at 50C for composition G and at 100C for composition H for 30 minutes each. These rubber sheets were separately placed in molds as used in Example 7 to occupy substan-tially 95% of the cavities of the molds. The molds were heated and pressed at 170C and 150 kg/cm2 for 10 minutes by a press machine. Cold water was passed through the jackets of the molds to cool the molds to 85C. The molds were kept at this temperature for 6 minutes. The foamed bodies were released from these molds. The density of the foamed body of the composi-tion G was 0.12 and the density of the foamed body of the composition H was 0.12O The outer appearance of these foamed bodies was the same as that obtained in Example 7. The shrinkage of these foamed bodies was measured in a similar manner as in Example 7, and the obtained results are shown in table 4 below:
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Background of the Invention The present invention relates to a method for manufacturing a low density foamed body containing rubber as a main constituent.
A conventional method for manufacturing foamed rubber is known according to which a mixture containing rubber,~a foaming agent, and a crosslinking agent is fed into a mold, the mold is heated to foam the mixture, and the produced foamed body is released from the mold.
However, with a foamed body manufactured according to this method, an expansion ratio of only about 3 to 6 and a density of about 0.15 to 0.3 are obtainable. It has thus been difficult with this method to either increase the expansion ratio or to decrease the density.
When the foaming agent is used in a great amount to raise the expansion ratio, the foaming pressure within the mold rises excessively when the mold is heated.
Then, when the mold is opened, the foamed body immedi-ately expands, explodes, and is scattered away.
Summary of the Invention~ ;~
It~is an object o the present invention to provide a method for manufac~uring a low density rùbber~foamed body.~ ~
It is another ob~ect of the present invention to provide a method~for~manufacturing a rubber foamed body which has a low density as well as a low shrinking property.
.... ... - - -:-:
'` ~ ''.- . .
~ . .
.
.
In order to achieve these and other objects, khere is provided according to the present invention, a method for manufacturing a low density rubber foamed body com-prising the steps of forming a sheet or sheets from a mixture of 100 parts by weight of natural rubber or a synthetic rubber, 10 to 80 parts by weight of a foaming agent, and 0.5 to 15 parts by weight of a crosslinking agent; enclosing said sheet or sheets within a mold so as substantially to fill the mold, and heating said mold under pressure from the exterior to thereby foam said ~sheet or sheets; forcibly cooling said mold; and releas-ing a foamed body from said mold. When 10 to 60 parts by weight of a thermoplastic synthetic resin are further added to the mixture in the method of the present inven-tion described above, a rubber foamed body of low densityand low shrinking property is obtainable.
In accordance with the present invention, a large amount of the foaming agent may be used while preventing the drawbacks of the prior art technique such as explosion or scattering of the foamed body when the mold is opened, so that a low density rubber foamed body may be provided.
A lower shrinking property may be achieved by further adding a thermoplastic synthetic resin to the raw material mixture containing natural or the synthetic rubber, the foaming agent and the crosslinking agent.
The low densit~ rubber foamed bodies obtained according to the present inven-tion are preferably used for various kinds of cushion materials, substitutes for springs, buoys, automobile partsl heat insulators, impact absorbers, and so on.
Detailed Description of the Preferred Embodiments The raw material rubber to be used in this inven-tion may be natural rubber or any kind o synthetic rubber.
Examples of such synthetic rubbers include acrylonitrile-butadiene rubber (NBR), chIoroprene rubber (CR),isoprene rubber (IR), styrene-butadiene rubber (SBR), and ethylene-propylenediene copolymer rubber (EPDM).
The foaming agent to be mixed with the rubber material : .
.,~
- , : .
- : , , , , ~ , - ~ . . , ' ` ~ , :
may be any foaming agent which is used for manufacturing conventional rubber foamed bodies and may, for example, include azodicarbonamide, dinitrosopentamethylenetetramine, p-toluenesulfonylhydrazine, azobisisobutyronitrile, diazoaminobenzene, and toluenesulfonyl semicarbazide.
The foaming agent is used in the amount of 10 to 80 parts by weight based on 100 parts by weight of the raw material rubber, although the preerred amount varies depending upon the kind of natural or synthetic rubber to be used as the main constituent and the density of the desired foamed body. When this amount is smaller than 10 parts by weight, a sufficiently highly foamed body may not be obtained. When this amount exceeds 80 parts by weight, the foamed body may cause breakdown, or a foamed body having adequate impact resilience may not be obtained. The method also requires a crosslinking agent in addition to the foaming agent. Preferable crosslinking agents may include sulfur, zinc oxide, and organic peroxides. Examples of organic peroxides may include dicumylperoxide, 2,5-dimethyl-2,5 di(tert.-butyl)peroxide, 1,3-bis(tert.-butylperoxy-isopropyl)benzene, m-octaldecylazidoformate, and tert.-butylperoxycumene. Although the amount of the crosslinking agent as mentioned above may differ depending upon the raw material rubber used, the kind and amount of foaming agent used and other conditions, it is preferably within the range of 0.5 to 15 parts by weight based on 100 parts of the raw material rubber.
In addition to the foaming agent and the crosslinking agent, various other additives may optionally be added. `
For example, there may be added a filler such as carbon black, clay, and calcium carbonate; a foaming auxiliary such as urea, stearic acid, lauric acid, and salicylic acid; a metal oxide such as zinc oxide; and a colorant.
An antioxidant may also be included. The thermoplastic synthetic resin preferably used in the present invention may include polyethylene, polypropylene, polystyrene, .~..
.
, ~ ' ,' ' .
polyvinyl chloride, an ethyl~ne-vinyl acetate copolymer resin, a polyamide resin and an acrylic resin. If the amount of the thermoplastic synthetic resin does not reach 10 parts by weight, satisfactory prevention of shrinkage may not be achieved. If this amount exceeds 60 parts by weight, the rubbery resilience is degraded, resulting in an unsatisfactory product.
The raw material mixture is well kneaded in a kneader such as a roll or a mixer and is formed into a sheet. For kneading the raw material, the components other than the crosslinking agent are first well kneaded with a roll at a surface temperature of 20 to 120C for about 15 to 60 minutes. After the crosslinking agent is added to the mixture, further kneading is performed for 5 minutes to provide a final raw material rubber sheet. Although the rubber sheet must have a thickness such that it may be put in a mold, a plurality of such rubber sheets may also be put in a single mold. There-fore, the thickness of the rubber sheet need not be the same as the size of the cavity of the mold.
The raw material rubber sheet thus obtained is p aced in a mold, the lid of the mold is closed, and the mold is pressed from the upper and lower sides.
The raw material rubber sheet is placed in the mold so that the rubber sheet substantially fills the cavity of the mold. The shape of the mold may oe arbitrary.
However, after the mold is heated under pressure for foaming the sheet and the mold is opened, the foamed body abruptly pops out of the mold while expanding in volume. Therefore, the mold preferably does not have ~-projections within the cavity and has an upwardly flared opening. ~or pressing the mold from the upper and lower sides thereof, a press machine may be used.
According to a further preferable method, the upper and lower halves of the mold are prefixed to the press machine, and the opening and closing of the mold is performed by vertically displacing these upper and '.:'" ' . "' ' " '': ", ., .,.. ,,.~, ' , .
- 5 - ~ ~7~
lower halves. When placiny the raw material rubber sheet which has been subjected to kneading into the mold, the sheet need not be aged in advance. Thus, the sheet may be placed directly in the mold where it is subjected to heat and pressure according to the present invention.
According to the conventional method for manufacturing the rubber foamed body, in order to foam the rubber sheet which has been kneaded, aging for about 24 hours has been required before the sheet may be heated under pressure as an essential step of the method. However, this aging step is not necessary according to the present invention.
Even when the raw material rubber sheet is subjected to the foaming step immediately after kneading, phenomena such as foam nonuniformity and breakdown do not occur, and continuous production is possible. After the raw material has been placed within the mold, the mold is then heated under pressure for crosslinking and foaming.
Although the heating temperature is mainly determined by the decomposition temperature of the foaming agent used, it is usually 130 to 200C. The pressure exerted on the mold is typically within a range of 100 to 200 kg/cm2.
After foaming has proceeded substantially, the mold is cooled. The cooling temperature changes according to the raw material rubber used, the kind and amount of the foam-ing agent used, the kind and amount of the crosslinking agant used, and other conditions. ~owever, typically it is within the range of about 50 to 100C. The cooling step utilizes forcible cooling rather than natural cooling and may, for example, adopt the process of circulating water through the jacket of the mold. Circulation of air may alternatively be adopted for this purpose. As this cooling is performed, the gas pressure generated within the mold during the heating and foaming step is reduced and the bonding between the polymer molecules is also sufficiently maintained. The mold is then opened. Upon opening the .....
, .
' mold, the rubber foamed body pops out of tlle mold without exploding, ~nd the volume of the foamed body instantaneously increases more than about 15 times the original volume. Thus, the low density rubber foamed body of the present invention is obtained. The density of the resultant rubber foamed body is reduced to about 0.12 or lower.
The present invention will be more clearly under-stood from the ~ollowing description made with reference to the examples.
Example 1 Acrylonitrile-butadiene rubber (NBR) 100 parts by weight Carbon black 20 parts by weight Stearic acid 3.0 parts by weight Process oil 10 parts by weight Dioctylphthalate 10 parts by weight Azodicarbonamide 25 parts by weight Zinc oxide 5 parts by weight Antioxidant (*) 1.5 parts by weight Sulfur 0.5 part by weight * 2,2,4-trimethyl-1,2-dihydroquinoline The components above excluding sulfur were kneaded-for S5 minutes with a roll having a surface temperature of 30C. Sulfur was then added, and the mixture was kneaded for 5 minutes to provide a rubber sheet 5 mm in thickness. The sheet was cut into pieces of appropriate size. Three such pieces were placed in a mol~ having a cavity 150 mm in length, 230 mm in width, and 12 mm in depth. After closing the mold with a lid, the mold was pressed from the upper and lower sides thereof at a pressure of 170 kg/cm2 with a press machine. Heated vapor was introduced in the jacket of the mold to heat the sides of the mold to 170C, and the mold was kept at this temperature for 10 minutes. The heated vapor in the jacket was removed; and water was then introduced.
After 5 minutes, the mold temperature was ~5C. The ,. ..
.. . ...
~ 7 ~ 7~2~
mold was then opened, and the ~oamed body immediately popped out of the mold, providing the Eoamed body of the present invention. The density of this foamed body was 0.031. The outer appearance of the foamed body corresponded to that of the cavity of the mold, and no cracks or explosions were observed. The cushion property and resilience of the foamed body were excellent.
Example 2 Chloroprene rubber 100 parts by weight Carbon black 20 parts by weight Stearic acid 3.0 parts by weight Dioc-tylphthalate 10 parts by weight ~zodicarbonamide 16 parts by weight Zinc oxide 7 parts by weight Antioxidant (*) 1.0 part by weight Filler (Calcium carbonate)10 parts by weight Magnesia 4.0 parts by weight * N-phenyl-N'-isopropyl-p-phenylenediamine A rubber sheet 5.5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 40 minutes and the roll temperature was 40C. This rubber sheet - was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example 1.
Ths heating temperature was 170C, the pressure was 170 kg/cm2, and the heating time was 8 minutes. The mold was cooled in a simiIar manner as in Example 1.
The cooling time was 5 minutes and the temperature of the mold after cooling was 85C.
The press machine was released and a low density foamed body of 0.050 density was instantaneously obtained.
The outer appearance of the obtained foamed body was the same as in Example 1. The foamed body had excellent 1mpact resilience.
.
, .. .. . . .. .....
Example 3 Styrene-butadiene rubber (SBR~ 100 parts by weight Carbon black40 parts by weight Stearic acid3.0 parts ~y weight Process oil20 parts by weight Azodicarbonamide18 parts by weight zinc oxide 5 parts by weight Antioxidant (*)1.5 parts by weight Sulfur 1.2 parts by weight * N-phenyl-N'-isopropyl-p-phenylenediamine A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 30 minutes and the roll temperature was 40C. The rubber sheet was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example 1. The heating temperature was 150C, the pressure was 170 kg/cm2, and the heating time was 12 minutes. The mold was cooled.in a similar manner as in Example 1.
The cooling time was 12 minutes, and the temperature of the cooled mold was 50C.
When the press machine was released, a low density foamed body of 0.044 density was instantaneously obtained.
The outer appearance and impact resilience were like those of the foamed body obtained in Example 1.
Example 4 Isoprene rubber (IR)100 parts by weight Carbon black40 parts by weight Stearic acid3.0 parts by weight Process oil. 20 parts by weight Azodicarbonamide18 parts b~ weight Zinc oxide 5 parts by weight Antioxidant (*)1.5 parts by weight Sulfur 1.2 parts by weight * N-phenyl-N'-isopropyl-p-phenylenediamine :
A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 20 minutes and the roll temperature was 50C. The rubber sheet was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example l. The heating temperature was 160C, the pressure was 170 kg/cm2, and the heating time was 8 minutes. The mold was then cooled in a similar manner as in Example 1, except that the cooling time was 7 minutes and the temperature of the cooled mold was 80C.
The press machine was then released, thus providing a low density foamed body of 0.032 density. The obtained foamed bod~ had an outer appearance and impact resilience comparable to those of the foamed body obtained in Example 1.
Example 5 Ethylene-propylenediene copolymer rubber 100 parts by weight Carbon black 15 parts by weight Stearic acid 2.0 parts by weight Process oil 10 parts by weight Azodicarbonamide 25 parts by weight Zinc oxide 5 parts by weight Dicumylperoxide 5.3 parts by weight A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 30 minutes and the roll temperature was 50C. The rubber sheet was cut into pieces of predetermined size. Three such pieces were placed in a mold and the mold was heated under pressure in a similar manner as in Example 1. The heating temperature was 165C, the pressure was 170 kg/cm2, and the heating time was 14 minutes. The mold was then cooled in a similar manner as in Example l, except that the cooling time was 3 minutes and the . .~
,: i .
- 10 - ~ ~7~
temperature o~ the cooled mold was 100C.
The press machine was released and a low density foamed body of 0.033 density was instantaneously obtained.
Example 6 Ethylene-propylenediene copolymer rubber 100 parts by weight Carbon black 15 parts by weight Stearic acid 2.0 parts by weight Process oil 15 parts by weight Azodicarbonamide 35 parts by weight Zinc oxide 3.0 parts by weight Dicumylperoxide 5.3 parts by wei~ht A rubber sheet 5 mm in thickness was obtained from the above components in a similar manner as in Example 1, except that the kneading time was 30 minutes and the roll surface temperature was 50C. The rubber sheet was cut into pieces o~ predetermined size. Three such pieces were placed in a mold and the mold was cooled in a similar manner an in Example 1, except that the cooling time was 10 minutes and the temperature of the cooled mold was 90C.
The press machine was released and a low density foamed body of 0.02 density was instantaneously obtained~
6~
~l ~1 3 3 ~1 . .,1 - 3 3 >~ 3 3 Q ~ ~, ,, ~ r4 .
m u, ~ ~ h u~ 0 u~ S I
Q~ ~ o o ~ ~ ~ o o ~ O
o ~ r~
~ .C
''I 3 3 ` 3 ,,, ~, 3 3 3 3 Q
" R ~ ~ R R rq ~
h ~ Ql h h h ~4 O O ~ S:4 ~ ~ O
o ~ u~ o In o ,i o ~ ~: ~
.
`
.' o ` #
~m U~ o .. _ p, .
o a) u a.) fd aJ o . r~ ~ I
:~ o ~ o ~ 0 h ~. ~ ~ o ~
x :: ~ 3 c~ v o ~ u~
....
:
`: ~
. . . ` ` ~ : ` ` ; . . ~
, . ' `
,. . ' ' Rubber sheets 2 mm in thickness were obtained from the above compositions by kneading at 50C for composi-tion A and at 100C for composition B. The kneading time was 25 minutes in each case. The two rubber sheets were separately placed into molds having dimensions of 25 cm x 25 cm x 1.5 cm and having an opening flaring at an angle of 60C, to occupy substantially 95~ of the cavity of each mold. The molds were heated and pressed by press machines for 10 minutes at a heating temperature of 170C and a pressure of 150 kg/cm2.
Water was circulated in the jackets of the molds to drop the temperature of the molds to 85C and this temperature was maintained for 6 minutes. The foamed bodies were then released from the molds. The foamed body of the composition A had a density of 0.048, and the foamed body of the composition B had a density of 0.052; neither foamed body exhibited cracks or foam nonuniformity. The shrinkage as measured over time was as follows. For measuring the shrinkage, a mark 10 cm in length was made on the surface of the foamed body immediately after it was released from the mold, and the shrinkage of this line was measured.
.. ..
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, ~ ': ' ' ' :' .
Q
~) ~
3 3 3 ~ ~ 3 3 R R R ~ ~ R ~.Q
au~
S~ ~ h __ ~ 4 0 o ~, o ~
U~ o o u~
s~ ~ o ~1 ~1 ~-1 C~
----co c~ :3: 3 a i~ 3 3 3 >1 ~ :~ R::~
n ~ .~) R ~ ~ ~ ~ R
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_ ~ ~ Q~ ~ oQ, S~ ~ o o r~
~r ~1 co ~ .
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/ ~ ~1 ~ o u~ g __ ~ : ~d O o :~ : :
.
:
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- - : . ., : . . ` .:
- ~
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' :
. : : '' '~ ' ' '~ . ': ' ~ 7~;213 Rubber sheets 2 mm in thickness were obtained from the above compositions C and D by kneading the component mixtures at 35C for 35 minutes for both of the composi-tions. The rubber sheets were separately placed in molds as used in Example 7 to fill substantially 95% of the cavities of the molds. After heating the molds at 170C and at a pressure of 150 kg/cm2, cold water was passed through the jackets of the molds to lower the temperature to 85C. The molds were maintained at this temperature for 6 minutes. The foamed bodies were released from the molds. The foamed body of the compo- -sition C had a density of 0.038 and the foamed body of the composition D had a density of 0.04. The outer appearance of the foamed bodies was the same as that of the foamed bodies obtained in Example 7. The shrinkage of the foamed bodies was measured in a similar manner an in Example 7, and the obtained results are shown in Table 2 below:
.
- 15 - ~t7~6;~
.a) a) 3 3 a) a~
3 3 ~ ~ 3 3 3 3 Q rq R
~ O O ~
S~ ~ O ~ o O ~ 1 ~
3 " ~ ~ 3 3 3 3 o ~ oo U~
~7 OD C~
U~ O ~el~ O O O O
S-l ~1 O ~
: :
~1 ~ ~: a~
~ _ : :
Q s~s~ `:
E~ ~ ~. ~r :
~-1 ` ~ ~ ~9 _ ~ ~: ~ : ' ':
~ ~ .Y ,4 ~ ~
a~ ~ ~
,~ o ~ ~ x ~ ~ ~ 3 , ~ ~ ~ ; ~ ~ o ~ ~ _ ~ 1~ ~ O ~ 1 N
.~
, . ' :
-, ' :
: ~ ` :
?
- 16 ~
Rubber sheets ~ mm in thickness were obtained by kneading the above components at 50C for composition E
and at 110C for composition F for 25 minutes each.
These rubber sheets were placed in molds as used in Example 7 to occupy substantially 95% of the cavities of these molds. The molds were then heated at 170C
and pressed at 150 kg/cm2 for 6 minutes. Cold water was then passed through the jackets of the molds to cool them to 85C. The molds were maintained at this temperature for 6 minutes. The density of the obtained product was 0.07 for the composition E and 0.073 for the composition F. The outer appearance of the foamed bodies was the same as that obtained in Example 7. The shrinkage of the foamed bodies was measured in a similar manner as in Example 7, and the obtained results are - shown in-Table 3 below:
S ~ ,C
3 'a~ 3 3 3 R ~ 3 3 , ,4 ~ Q
S~ h Q. Q, h h 5-1 _ P~ ~, o o Q~ . o IQ O ~ o o ~ ,i U~ ,~
CO o ~'1 1~ a~ .
E~--o ~1 ~ 3 3 ,~
..~H 00 ~ a) a) O a~ 3 . 3 ~ ~ 3 3 3 s:: _ ~ ~ ~ ~ R
D ~ ~ R ~, .,, .4 .4 a~ ~ ~ ~ ~ to I s~
. .
co ~ Q~ ~ h S~ ~ o ~ U~ o o .
~o oo cn :
Q _ E~ ~ ~1 ~ C~ ~
. _ m ~ ~
h ~ u~ u~ O ::
u a~ ~ S~ O
_ ~ ` O O rl r~
H 111 L ~ ~ ( o :
L
`
.
:
: ~ . . . . .. ......... , .. .,.. , .. _, . .:
.` ~ ~ . , . .:
'~
.' ' . . ' . ~ ' i .: ~ ' ', . i , .
Rubber sheets 2 mm in thickness were obtained by kneading the above components by a roll at 50C for composition G and at 100C for composition H for 30 minutes each. These rubber sheets were separately placed in molds as used in Example 7 to occupy substan-tially 95% of the cavities of the molds. The molds were heated and pressed at 170C and 150 kg/cm2 for 10 minutes by a press machine. Cold water was passed through the jackets of the molds to cool the molds to 85C. The molds were kept at this temperature for 6 minutes. The foamed bodies were released from these molds. The density of the foamed body of the composi-tion G was 0.12 and the density of the foamed body of the composition H was 0.12O The outer appearance of these foamed bodies was the same as that obtained in Example 7. The shrinkage of these foamed bodies was measured in a similar manner as in Example 7, and the obtained results are shown in table 4 below:
- 19 - ~ 2~
~ ~ _ N
Q~ ~ .
~ co a~
~ ~ _ _ ~ ~a . .
.. ~1 CO
~ _ _ $~
~ CO
~ ,, ~ .' Q~ ~ f~ N cn a~
~ ~ _ _ ,~ I ~ :
~'Ul _ _ , ~ :~D ~ ' _ _ :
~: ~1 H ,a _ __ :
:
,~
-:
`
:
:,: : ` .'' : : . . ':, , ~ , , , ~ , , , :
~' ' '
Claims (8)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A method for manufacturing a low density rubber foamed body comprising the steps of forming a sheet or sheets from a mixture of 100 parts by weight of natural rubber or a synthetic rubber, 10 to 80 parts by weight of a foaming agent, and 0.5 to 15 parts by weight of a crosslinking agent; enclosing said sheet or sheets within a mold so as substantially to fill the mold, and heating said mold under pressure from the exterior to thereby foam said sheet; forcibly cooling said mold; and releas-ing a foamed body from said mold.
2. A method according to Claim l, wherein said mixture further contains 10 to 60 parts by weight of a thermoplastic synthetic resin.
3. A method according to Claim 1 or 2, wherein said heating is performed at a temperature of about 130 to 200°C.
4. A method according to Claim 1 or 2, wherein said cooling is performed at a temperature of about 50 to 100°C.
5. A method according to Claim 1 or 2, wherein said pressure is about 100 to 200 kg/cm2.
6. A method according to Claim l or 2, wherein said foaming agent is one member selected from the group consisting of azodicarbonamide, dinitrosopentamethylene-tetramine, p-toluenesulfonylhydrazine, azobisisobutyro-nitrile, diazoaminobenzene, and toluenesulfonyl semi-carbazide.
7. A method according to Claim l or 2, wherein said crosslinking agent is one member selected from the group consisting of sulfur, zinc oxide, dicumylperoxide, 2,5-dimethyl-2,5-di(tert.-butyl)peroxide, 1,3-bis(tert.-butylperoxy-isopropyl)benzene,m-octadecylazidoformate, and tert.-butylperoxycumene.
8. A method according to Claim 2, wherein said thermoplastic synthetic resin is polyethylene, polypropy-lene, polystyrene, polyvinyl chloride, an ethylene-vinyl acetate copolymer, a polyamide resin, or an acrylic resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000383063A CA1171620A (en) | 1981-07-31 | 1981-07-31 | Method for manufacturing low density rubber foamed body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000383063A CA1171620A (en) | 1981-07-31 | 1981-07-31 | Method for manufacturing low density rubber foamed body |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1171620A true CA1171620A (en) | 1984-07-31 |
Family
ID=4120592
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000383063A Expired CA1171620A (en) | 1981-07-31 | 1981-07-31 | Method for manufacturing low density rubber foamed body |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1171620A (en) |
-
1981
- 1981-07-31 CA CA000383063A patent/CA1171620A/en not_active Expired
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