USRE21245E - Process of producing expanded - Google Patents

Process of producing expanded Download PDF

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USRE21245E
USRE21245E US21245DE USRE21245E US RE21245 E USRE21245 E US RE21245E US 21245D E US21245D E US 21245DE US RE21245 E USRE21245 E US RE21245E
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dough
expanded
rubber
gas
pressure
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/14Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
    • C08J9/141Hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C67/00Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/24Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 characterised by the choice of material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/08Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L21/00Compositions of unspecified rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2321/00Characterised by the use of unspecified rubbers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T152/00Resilient tires and wheels
    • Y10T152/10Tires, resilient
    • Y10T152/10279Cushion
    • Y10T152/10378Casing enclosed core
    • Y10T152/10387Separate core
    • Y10T152/10396Removable
    • Y10T152/10405Sponge rubber

Definitions

  • the material comprising the basic substance of my invention consists of rubber or a rubber composition with any suitable vulcanizing material,
  • inert gas has been expanded w thin successive containers or moulds under heat and pressure.
  • I may treat a blob of suitable as dough in successive containers or moulds whereby the desired form is imparted to the finished article.
  • I may make them so that the body of the finished article is divided up by bulkheads of homogeneous skins of material. This result may be attained in any 5 desired suitable manner. For instance I may in a 1 suitable mould or container make a number of comparatively thin slabs, strips or the like of the expanded material, each having an outer homogeneous skin enclosing an inflated cellular body, 10
  • dough containing a very large proportion of rubber with the necessary amount of sulphur for so vulcanization.
  • other ingradients may frequently be introduced into the mix or dough, e. g. hydro-carbons, antimony sulphide, magnesium carbonate, dark substitute,- white substitute (vulcanized oil), zinc oxide, magnesium oxide and other known suitable material.
  • the expansion may be eifected by air or by an ino ert gas such as nitrogen.
  • I employ a dough consisting of rub- 'ber, 25% sulphur, 6% hydro-carbon, 3% calcined 45 magnesia, 1% ceresine wax, and 5% colouring matter. If less than 5% colouring matter be required the percentage of rubber may correspond ingly be increased.
  • I place this dough in, a container and insert this in an autoclave to the steam Jacket of which I" admit steam so that in a period of about 30 minutes a gauge pressure of about 8 lbs. is reached, and I inject an inert gas, such as nitrogen, into the autoclave or gassing cylinder, at a pressure of about 180 atmospheres; to permeate the dough within the container.
  • an inert gas such as nitrogen
  • the steam will heat the contents to about 113 C. and I maintained this for a period of about 400 minutes.
  • the pressure of the gas will have risen by the heat applied to it. 7
  • the apparatus may be of simple construction and comprises a'steam jacketed gassing cylinder or autoclave capable of withstanding the necessary gas pressure, one end of which'is fitted with a detachable door secured by nuts or, alternatively, a breech block may be employed in place of the door.
  • Tothe cylinder and jacket are connected inlet and outlet pipes for gas and steam and for water circulation, with appropriate valves and pressure gauges.
  • the apparatus and its contents having cooled down to normal temperature I open the gas valve to permit the gas to escape and having opened the gassing cylinder remove the container and open. it so as to remove from it the material which although it had already expanded so as to fill and exert considerable pressure in the container, will at once further expand to about 6 times or a little more its original volume.
  • buoyant blocks that is to say blocks of expanded rubber material which will retain almost indefinitely their original gas content; which are of very low specific gravity (a cubic foot made as aforesaid weighing not more than about five pounds or even less per cubic foot); the buoyancy of which is not materially affected even if they be punctured or cut, because only those cells the walls of which have thus been ruptured will admit water; the cellular body of which will neither be disrupted nor caused to collapse if the outerskin be removed; which are not liable to corrosion, and for the production of which very simple apgas pressure, which increases forces when in use.
  • the skin formed on the outside of the article by the two-stage procedure described is tough and hard and the walls also'of the cells are rendered more perfectly gas tight than by any method heretofore proposed. I therefore do not require to provide, as has been proposed, an outer skin of a special material or composition which does not itself retain gas under pressure for producing an outer skin, with the object of rendering the cellular body of the material gas tight.
  • the necessity, according to another prior proposed method of procedure, of carrying out the complete expansion whilst the froth. is hot, in order 1 to prevent collapse on further vulcanization is negatived by the results obtained by the procedure according to my invention, nor do I obtain thewhole of the expansion in a subsequent stage.
  • I may make the dough by mixing rubber 60%; sulphur 4%; antimony sulphide 14 /2%; ceresine wax 2 magnesium carbonate 19%.”
  • the material thus partly expanded-and vulcanized is then introduced to a second container or mould in which it is heated, conveniently as before described by steam which in this instance may be at gauge pressure of about 50 lbs this pressure being attained in a period of about 15 minutes and is maintained for a period of about minutes.
  • the subsequent cooling of the apparatus and its contents may be accelerated by circulating water through the jacket as already mentioned.
  • moulds or containers having the required dimensions of the finished material in the fiat.
  • I proceed by cutting astrip of the dough to the required dimensions and roll this upon itself.
  • I place the strip of dough on a strip of linen, canvas or thin metal and roll the two together into a compact roll which I bind round with several layers or turns of canvas, linen, or thin metal to withstand the pressure.
  • the outer binding layers of material serve in this instance as the container or mould in which the preliminary treatment is eifected. It will be necessary to coat or smear the strip of linen, canvas, or metal, with grease, French chalk or the like to prevent the rubber material adhering to it.
  • the partly expanded and vulcanized sheet 'or strip is again wound upon itself (with the strip of linen, canvas or thin metal) and an outer binding of several layers or turns of canvas, linen or thin metal, and the roll is then subjected to the action of heat whereby the further expansion'and the completion of the vulcanization of the material are eifected.
  • the partly expanded and vulcanized strip or sheet is cut into pieces of smaller strips of appropriate size and shape, and .these are placed insultable mouids, in which, by the application of heat they are further expanded, thereby imparting to them the shape of the mould, and the vulcanization completed.
  • the gaming chamber which has to withstand the high pressure gas may be made of much smaller dimensions than otherwise would be the case.
  • the importance of this will be appreciated when it is realized that not only is the first cost of a comparatively small gassing chamber and apparatus to withstand a pressure of 180 atmospheres very much less than a large chamber and apparatus to withstand the same high pressure, but the maintenance and working charges also are less, all this aiding in the-cheapening of the finished product.
  • the heating chamber or press wherein he final stage of the expansion (as well as the completion of vulcanization) is brought about by the application of heat, is a relatively inexpensive appa ratus.
  • my invention it is also made readily possible to produce articles having an interior of hard expanded rubber, and an outer fading of soft expanded rubber, or vice verse. by building up a mass composed of strips or layers of partly expanded and vulcanized-material from dough having the necessary diflerent compositions, and then After this the subjecting them together to further heat and pressure as described.
  • any known suitable accelerator may be mixed with the dough whereby the period of the treatment may be reduced.
  • expanded rubber made according to'my invention may be employed for many other purposes such for example as insulation for refrigerators, silencers, non-conductors of sound, as a non-absorbent medium and for various purposes in constructional work, and by suitably varying the composition of the doughas is well understoodthe finished articles or products may vary from extreme velvety softness to a hardness comparable with wood.
  • thedough consists of a basic mixture of rubber, sulphur and ceresine wax together with other substances that determine the character of the finished product, that is to say, when a hard finished product is required, hydro-carbon and calcined magnesia may be added to the basic mixture; when a soft resilient finished product is required, vulcanized oil, golden antimony and magnesium carbonate maybe added to the basic mixture, whereas when a soft finished product having less resilience is required,'
  • antimony and magnesium carbonate may be added to the basic mixture.
  • the dough is subjected to heat and gas pressure for a period to produce partial vulcanization and expansion, the thuspartly vulcanized and expanded material is then cooled down and then further expanded and its vulcanization completed by the application of heat. It is not necessary during the second stage of the process to inject gas into the partly vulcanized and expanded material; the application of heat alone sufiicing to. bring about its further expansion as well as effecting the completion of the vulcanization.
  • the process of. producing expanded rubber material which consists in placing the dough within a container, placing the container and dough within a gassing chamber, injecting gas under high pressure into the chamber, heating the cylinder to efiect partial vulcanization of the dough, cooling the chamber, releasing the pressure, removing the dough from the container and chamber whereupon it expands, placing the dough within a larger container, and heating the dough until its vulcanization is complete and until it has expanded to fill the said larger container.
  • closed cell expanded rubber material which consists in formingv innumerable gas cells in the dough by subjecting-it to gas under pressure; partially vulcanizing the dough; confining the rubber dough against any substantial expansion while it is being gassed; releasing the confining pressure from the dough, thereby permitting the dough to expand under the action of gas in the cells within it; and heating the dough to expand the gases within it and consequently also expanding the dough and simultaneously carrying vulcanization of the material to completion.
  • closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by introducing the rubber dough into a confining mold to maintain it under pressure against substantial expansion, gassing the rubber and heating the dough to expand the gases within it, and consequently also expanding the dough and simultaneously carryina the vulcanization of the material to completion.
  • closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by introducing the rubber. dough into a confining mold to maintain it under pressure against substantial expansion, partially vulcanizing and gassing the rubber dough so confined in the mold, releasing the pressure on the dough in the mold, thereby permitting th pand under the action of the gas n the closed cells within it, and heating the dough to expand the gases within it, and consequently also expending the dough and simultaneously carrying the vulcanization of the material to completion.
  • closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by introducing the rubber dough into a confining mold to maintain it under pressure against substantial expansion, heating the rubber dough to partially vulcanize it and gassing the dough to exthe pressure on the partially vulcanized dough in the mold, thereby permitting the partially rubber dough so confined m the mold, releasing vulcanized doughto expand under the action oi the gas in the closed cells within it, and heating the doimh to expand the gases within it, and consequently also expanding the dough and carrying the vulcanization oi the material to completion.
  • closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by partially vulcanizing the rubber dough, introducing the rubber dough into a confining mold to maintain it under pressure against substantial expansion, gassing the rubber dough so confined in the mold, removing the dough from the mold in order to release. the pressure on the dough, thereby permitting the dough to expand under the action of the gas in the closed cells within it, and heating the dough to expand the gases 'within it, and consequently also expanding the dough and simultaneously carrying the vulcanization of the material to completion.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)

Description

Reiuued on. 24, .1939
PATENT orrica PROCESS OF PRODUCING EXPANDED RUBBER MATERIAL Geofl'rey Price Denton, Broadlianger, Peter-afield Hants, England, assignor to Bubatex Products, -Inc., New York, N. Y., a corporation of Delaware N Drawing. Original N0; Lsosfiaa flltefl Apl'll 25, 1933, SEl'illl N0. 510,332, January 21, 1931. Application for reissue May 25, 1939, Serial No. 275,776. In Great Britain May 14, 1930 16 Claims. (01. 18-53) This invention has reference to improvements in the manufacture and use of expanded rubber material. I
,Themanufacture of expanded rubber'by subjecting the dough", i. e. the rubber or rubber composition, to heat and gas under high pressure has heretofore proved unsatisfactory in that it is found that the expanded material after a comparatively short period of time loses some of its contained gas and therefore is liable to collapse to some extent. Also that if the outer skin formed on the body of the expanded material be punctured or cut the collapsing of the material is accelerated.
For many purposes material possessing these defects is practically useless. v
For instance there has been a demand for an eflicient substitute for the metal air tanks employed for many years on life boats to ensure their 20 buoyancy (even after shipping considerable volumes of water), because the walls of said tanks are necessarily made very thin and are, therefore, fairly easily punctured and otherwise damaged rendering the tanks wholly or in part use.-
- less. Further they are liable to corrosion and owing to the difficulty of access to them for inspection not merely of the front; but of the side and rear walls also of these tanks, there is a more or less constant risk-after they have been installed for some timethat one or more of them may be in a useless or nearly useless condition at the time their useful service is most required.
Although it has been suggested or proposed to utilize expanded rubber for buoyancy blocks in 36 life jackets and otherwise they have not met with any practical success, probably for the reason above stated.
It is an object of my invention to produce an expanded rubber material which obviates the de- 40 fects of any heretofore known and which may be employed inter alia as an efllcient substitute for the metal air tanks referred to, although I wish it to be understood that the scope of my invention is not limited to this or any particularuse to be made of it.
The material comprising the basic substance of my invention consists of rubber or a rubber composition with any suitable vulcanizing material,
which rubber or compos tion (hereinafter re-' cu ferred to as the dough) by air or, preferably, an,
inert gas, has been expanded w thin successive containers or moulds under heat and pressure. Whencomparatively small blocks or articles are to be made, I may treat a blob of suitable as dough in successive containers or moulds whereby the desired form is imparted to the finished article. Whenlarger articles are to be made I may make them so that the body of the finished article is divided up by bulkheads of homogeneous skins of material. This result may be attained in any 5 desired suitable manner. For instance I may in a 1 suitable mould or container make a number of comparatively thin slabs, strips or the like of the expanded material, each having an outer homogeneous skin enclosing an inflated cellular body, 10
and from these ,build up the desired article, which is then subjected in another mould to heat and pressure thereby causing the contracting skins of adjacent slabs to unite so that the article now completely expanded and vulcanized is made to a 15 degree stiff by the bulkhead or bulkheads within its cellular body. Alternatively I may make the slabs or strips or the like in successive containers .and then secure them together-should this be desirable-by a suitable adhesive, for instance 80 rubber solution. The slabs or strips may be arranged in regular or irregular strata according to the purpose to which the finished article is to be applied.
The composition of the dough and the temperau ture. and pressure during treatment 'will depend of course upon various factors.
For. some purposes it may be desirable to utilize dough containing a very large proportion of rubber with the necessary amount of sulphur for so vulcanization. For reasons of economy, durability or to obtain hardness, colours etc.or to obtain soft material of less elasticity than pure rubber will give when highly expanded, other ingradients may frequently be introduced into the mix or dough, e. g. hydro-carbons, antimony sulphide, magnesium carbonate, dark substitute,- white substitute (vulcanized oil), zinc oxide, magnesium oxide and other known suitable material. The expansion may be eifected by air or by an ino ert gas such as nitrogen.
By way of example for producing ahard and rigid expanded rubber material for use as buoyant blocks, I employ a dough consisting of rub- 'ber, 25% sulphur, 6% hydro-carbon, 3% calcined 45 magnesia, 1% ceresine wax, and 5% colouring matter. If less than 5% colouring matter be required the percentage of rubber may correspond ingly be increased. I place this dough in, a container and insert this in an autoclave to the steam Jacket of which I" admit steam so that in a period of about 30 minutes a gauge pressure of about 8 lbs. is reached, and I inject an inert gas, such as nitrogen, into the autoclave or gassing cylinder, at a pressure of about 180 atmospheres; to permeate the dough within the container.
The steam will heat the contents to about 113 C. and I maintained this for a period of about 400 minutes. The pressure of the gas will have risen by the heat applied to it. 7
After the period stated I shut ofl the steam supply so that the apparatus with its contents will cool down somewhat during a period of about 60 minutes after which I may accelerate the cooling by circulating water through the jacket.
7 The apparatus may be of simple construction and comprises a'steam jacketed gassing cylinder or autoclave capable of withstanding the necessary gas pressure, one end of which'is fitted with a detachable door secured by nuts or, alternatively, a breech block may be employed in place of the door. Tothe cylinder and jacket are connected inlet and outlet pipes for gas and steam and for water circulation, with appropriate valves and pressure gauges.
The apparatus and its contents having cooled down to normal temperature I open the gas valve to permit the gas to escape and having opened the gassing cylinder remove the container and open. it so as to remove from it the material which although it had already expanded so as to fill and exert considerable pressure in the container, will at once further expand to about 6 times or a little more its original volume. I then put this expanded material into another container or mold of adequate size and having the desired internal form, and heat this, say, by ad-' mitting steam to a jacket around the mould, until in a periodof about 15 minutes a gauge pressure of about 85 lbs, is reached, equivalent to a temperature of about 163 0., which I maintain for about 45 minutes. This will cause the material to expand further by pressure of the gas until it has increased to about 13 times its original volume, and it will have been shaped or mouled to the form of the mould, and its vulcanization will be completed.
The above procedure is adopted when the article to be produced is say, 1%" thick. When an article of greater thickness is to be made I may adopt a similar procedure varying the heat and period according to its mass or I may produce slabs, strips or the like of expanded material as above described with reference to the first container or mould and insert a number of these in suitably arranged fashion in a second mould which I then heat about as above described. The material thereupon further expands and by the heat and pressure of the gas the outer skins of the several strips or the like will be caused to join or unite. The skins of the layers or strips which have become joined constitute bulkheads within the body of the article rendering this more stiff.
Proceeding as above described I am able to provide really efilcie'nt buoyant blocks, that is to say blocks of expanded rubber material which will retain almost indefinitely their original gas content; which are of very low specific gravity (a cubic foot made as aforesaid weighing not more than about five pounds or even less per cubic foot); the buoyancy of which is not materially affected even if they be punctured or cut, because only those cells the walls of which have thus been ruptured will admit water; the cellular body of which will neither be disrupted nor caused to collapse if the outerskin be removed; which are not liable to corrosion, and for the production of which very simple apgas pressure, which increases forces when in use.
paratus is required. Further, the skin formed on the outside of the article by the two-stage procedure described, is tough and hard and the walls also'of the cells are rendered more perfectly gas tight than by any method heretofore proposed. I therefore do not require to provide, as has been proposed, an outer skin of a special material or composition which does not itself retain gas under pressure for producing an outer skin, with the object of rendering the cellular body of the material gas tight. Further, the necessity, according to another prior proposed method of procedure, of carrying out the complete expansion whilst the froth. is hot, in order 1 to prevent collapse on further vulcanization, is negatived by the results obtained by the procedure according to my invention, nor do I obtain thewhole of the expansion in a subsequent stage.
Material, made according to my invention, in tended for buoyancy purposes, such as for life jackets, life boats, etc. has, therefore, an application of the first importance never hitherto employed.
To obtain, in accordance with my invention, a soft resilient expanded material of say 10 lbs. weight per cubic foot, I make a dough by mixing together rubber 55%, sulphur Ii vulcanized oil (Sub) 9%; golden antimony 13% (15 to 17% of free-sulphur); ceresine wax 2% and magnesium carbonate 1'7 /2%.
Or, to obtain a soft material of less resilience of say 17 lbs per cubic foot, I may make the dough by mixing rubber 60%; sulphur 4%; antimony sulphide 14 /2%; ceresine wax 2 magnesium carbonate 19%."
To obtain a finished material of about 4 thickness and 10 lbs. weight per cubic'foot, I heat the dough in a gassing container by steam as before described and maintain this for about 270 minutes. The gas is admitted to the container at a pressure of about 180 atmospheres. The
by theheat applied, is maintained throughout this period and, as in the former case, also during the period of say 60 minutes in which the apparatus with its contents is allowed tocool down and even, if desired, during any further period when by circulating water through the jacket, the cooling is accelerated.
The material thus partly expanded-and vulcanized is then introduced to a second container or mould in which it is heated, conveniently as before described by steam which in this instance may be at gauge pressure of about 50 lbs this pressure being attained in a period of about 15 minutes and is maintained for a period of about minutes. The subsequent cooling of the apparatus and its contents may be accelerated by circulating water through the jacket as already mentioned. i
In some cases it may be desirable to provide an outer covering of linen, canvas, metal or other suitable material to protect the expanded-rubber against abrasion or other abnormal external, In such a case I may cut the said material to shape and lay it in the second container or mould in the appropriate position against the top, bottom and/or other face or faces thereof. This material will be made strongly to adhere to the rubber material owing to'the great pressure with which this is forced against the faces of the mould when the final expansion and completion of the vulcanization are effected; If desired the metal sheets may be made with countersunk perforations so that the rubber material will become anchored theret although I have found that for most purposes the rubber material clinks sufliciently firmly to the plain metal sheets.
When longstrips or sheets of the expanded rubber material are required to be made it may not be possible or at any rate convenient to employ moulds or containershaving the required dimensions of the finished material in the fiat. In such a case I proceed by cutting astrip of the dough to the required dimensions and roll this upon itself. Preferably I place the strip of dough on a strip of linen, canvas or thin metal and roll the two together into a compact roll which I bind round with several layers or turns of canvas, linen, or thin metal to withstand the pressure. The outer binding layers of material serve in this instance as the container or mould in which the preliminary treatment is eifected. It will be necessary to coat or smear the strip of linen, canvas, or metal, with grease, French chalk or the like to prevent the rubber material adhering to it. I then place this roll in the gassing chamber and proceed as already described, the material being gassed and partly vulcanized. gassing chamber with its contained roll is allowed to cool down, the gas allowed to escape from the chamber, and the roll of material removed. The roll is then unwound and the'second step in the process will be carried out according to the use to which the finished product-is 'to be put. When a long strip or sheet of the finished material is required, the partly expanded and vulcanized sheet 'or strip is again wound upon itself (with the strip of linen, canvas or thin metal) and an outer binding of several layers or turns of canvas, linen or thin metal, and the roll is then subjected to the action of heat whereby the further expansion'and the completion of the vulcanization of the material are eifected. When mats or like articles are required to be made, the partly expanded and vulcanized strip or sheet is cut into pieces of smaller strips of appropriate size and shape, and .these are placed insultable mouids, in which, by the application of heat they are further expanded, thereby imparting to them the shape of the mould, and the vulcanization completed. i Y
By effecting the expansion (as distinct from the vulcanization) of the dough in'stages, the gaming chamber which has to withstand the high pressure gas may be made of much smaller dimensions than otherwise would be the case. The importance of this will be appreciated when it is realized that not only is the first cost of a comparatively small gassing chamber and apparatus to withstand a pressure of 180 atmospheres very much less than a large chamber and apparatus to withstand the same high pressure, but the maintenance and working charges also are less, all this aiding in the-cheapening of the finished product.
The heating chamber or press wherein he final stage of the expansion (as well as the completion of vulcanization) is brought about by the application of heat, is a relatively inexpensive appa ratus.
By my invention it is also made readily possible to produce articles having an interior of hard expanded rubber, and an outer fading of soft expanded rubber, or vice verse. by building up a mass composed of strips or layers of partly expanded and vulcanized-material from dough having the necessary diflerent compositions, and then After this the subjecting them together to further heat and pressure as described.
Then again, by my invention the production of single finished article.
It is to be borne in mind that when thin metal sheets or strips are employed temporarily to separate superimposed layers of the dough, they must be coated as above described to prevent adherences to them of the rubber material, whereas when thin metal sheets are employed to provide an outer protection covering to the finished article, they should be quite clean and free from grease, whereby the adherence of the rubber material to them is ensured. An advantage to be derived from the employment of thin metal sheets or strips between the superimposed layers of the dough during the gassing and vulcanization is that they readily conduct heat to the dough.
If desired any known suitable accelerator may be mixed with the dough whereby the period of the treatment may be reduced. Although I have given details as to times, temperatures and pressures I wish it to be understood that I do not limit myself to these and, further, that these will also vary accordingly as diiferent compositions of dough are employed, and also accordingly as the articles produced are thinner or thicker than hereinbefore mentioned by-way of example.
Apart from its use as a buoyant material or for mats and the like already referred to expanded rubber made according to'my invention may be employed for many other purposes such for example as insulation for refrigerators, silencers, non-conductors of sound, as a non-absorbent medium and for various purposes in constructional work, and by suitably varying the composition of the doughas is well understoodthe finished articles or products may vary from extreme velvety softness to a hardness comparable with wood.
'It will be seen from the description of expanded rubber material madein accordance with my invention that thedough consists of a basic mixture of rubber, sulphur and ceresine wax together with other substances that determine the character of the finished product, that is to say, when a hard finished product is required, hydro-carbon and calcined magnesia may be added to the basic mixture; when a soft resilient finished product is required, vulcanized oil, golden antimony and magnesium carbonate maybe added to the basic mixture, whereas when a soft finished product having less resilience is required,'
antimony and magnesium carbonate may be added to the basic mixture.
In every case the dough is subjected to heat and gas pressure for a period to produce partial vulcanization and expansion, the thuspartly vulcanized and expanded material is then cooled down and then further expanded and its vulcanization completed by the application of heat. It is not necessary during the second stage of the process to inject gas into the partly vulcanized and expanded material; the application of heat alone sufiicing to. bring about its further expansion as well as effecting the completion of the vulcanization.
The steam jacketed chambers or autoclaves as also the moulds or containers employed in the production of the expanded rubber material according to my invention, are so well known in.
the art that it is not necessary to illustrate any of them.
What I claim is:
1. The process of producing expanded rubber material which consists in subjecting the dough to gas under high pressure, effecting partial vulcanization of the dough by heat whilst the dough is in the said gas under high pressure, cooling the dough, releasing the said pressure, and subsequently completing vulcanization and simultaneously expanding the dough by reheating it.
2. The process of producing expanded rubber material which consists in subjecting the dough to gas under high pressure and simultaneously permitting only partial expansion of the dough,
is in the said gas under pressure, cooling the dough, releasing the said pressure, permitting further expansion of the dough, and finally complating vulcanization and expansion of the dough by a further heat treatment thereof in the absence of gas under high pressure.
4. The process of producing expanded rubber material which consists in placing the dough within a container, placing the container and dough within-a gassing chamber, injecting gasunder high pressure into the chamber, heating the cylinder to effect partial vulcanization of the dough. cooling the chamber, releasing the pressure, removing the dough from the container and chamber whereupon it expands, and finally completing vulcanization and simultaneously expanding the dough by reheating it.
5. The process of. producing expanded rubber material which consists in placing the dough within a container, placing the container and dough within a gassing chamber, injecting gas under high pressure into the chamber, heating the cylinder to efiect partial vulcanization of the dough, cooling the chamber, releasing the pressure, removing the dough from the container and chamber whereupon it expands, placing the dough within a larger container, and heating the dough until its vulcanization is complete and until it has expanded to fill the said larger container.
6. The process of producing expanded rubber material which consists in subjecting dough to gas under high pressure, effecting partial vulcanization of the dough by heat whilst the dough is in the said gas under pressure, cooling the dough, releasing the pressure, placing the dough together with at least. one further portion vof dough--similarly partially vulcanized under pressure-in a container that is large enoughto permit expansion of the portions of dough, and heating the said portions of dough so that they become expanded and pressed together and completely vulcanized and united together.
7. The process of producing expanded rubber material which consistsinsubjecting the dough to gas under high pressure, effecting partial vulcanization oi the dough by heat whilst the dough is in the gas under pressure, cooling the dough, releasing the said pressure, permitting further expansion of the dough, placing the dough together with at least one other similarly treated portion of dough (i. e. partially vulcanized and partially expanded) in a container large enough to, permit further expansion of the portions of dough, and heating the portions of dough so that they are expanded within the container and completely vulcanized.
8. The process of producing expanded rubber" material which consists in placing the dough within a container, placing the container and dough within a gassing chamber, injecting gas under high .pressure into the chamber, heating the cylinder to effect partial vulcanization of the dough, cooling the chamber, releasing the pressure, removing the dough from the container and chamber whereupon it expands, placing the dough together with at least one similarly prepared portion of dough within a container large enough to permit further expansion of the portions of dough, and heating the said portions of dough so that they become expanded and pressed together and completely vulcanized and united together.
9. The process of producing expanded rubber 1 material which consists in forming innumerable gas cells in the dough by subjecting it to gas underpressure, partially vulcanizing the dough, releasing the pressure from the dough, permitting the dough to expand under the action of the gas in the cells within it, and heating the dough to expand the gases within it and consequently also expanding the dough and simultaneously carrying vulcanization of the material to completion.
10. The process as in claim 9 wherein the dough is partially vulcanized by heat whilst subjected to :as under pressure.
11. The process of producing expanded rubber canization of the dough by heat which simultaneously further expands the dough.
12. The process of producing closed cell expanded rubber material which consists in formingv innumerable gas cells in the dough by subjecting-it to gas under pressure; partially vulcanizing the dough; confining the rubber dough against any substantial expansion while it is being gassed; releasing the confining pressure from the dough, thereby permitting the dough to expand under the action of gas in the cells within it; and heating the dough to expand the gases within it and consequently also expanding the dough and simultaneously carrying vulcanization of the material to completion.
13. The process of producing closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by introducing the rubber dough into a confining mold to maintain it under pressure against substantial expansion, gassing the rubber and heating the dough to expand the gases within it, and consequently also expanding the dough and simultaneously carryina the vulcanization of the material to completion.
14. The process or producing closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by introducing the rubber. dough into a confining mold to maintain it under pressure against substantial expansion, partially vulcanizing and gassing the rubber dough so confined in the mold, releasing the pressure on the dough in the mold, thereby permitting th pand under the action of the gas n the closed cells within it, and heating the dough to expand the gases within it, and consequently also expending the dough and simultaneously carrying the vulcanization of the material to completion.
15. The process of producing closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by introducing the rubber dough into a confining mold to maintain it under pressure against substantial expansion, heating the rubber dough to partially vulcanize it and gassing the dough to exthe pressure on the partially vulcanized dough in the mold, thereby permitting the partially rubber dough so confined m the mold, releasing vulcanized doughto expand under the action oi the gas in the closed cells within it, and heating the doimh to expand the gases within it, and consequently also expanding the dough and carrying the vulcanization oi the material to completion.
16. The process of producing closed cell gas expanded rubber material which consists in forming innumerable closed gas cells in the rubber dough by partially vulcanizing the rubber dough, introducing the rubber dough into a confining mold to maintain it under pressure against substantial expansion, gassing the rubber dough so confined in the mold, removing the dough from the mold in order to release. the pressure on the dough, thereby permitting the dough to expand under the action of the gas in the closed cells within it, and heating the dough to expand the gases 'within it, and consequently also expanding the dough and simultaneously carrying the vulcanization of the material to completion.
GEOFFREY PRICE DENTON.
US21245D 1930-05-14 Process of producing expanded Expired USRE21245E (en)

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GB1480530A GB358967A (en) 1937-03-31 1930-05-14 Improvements in or relating to the manufacture and use of expanded rubber material
GB917837A GB495021A (en) 1937-03-31 1937-03-31 Improvements in or relating to the production of gas expanded rubber

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2422797A (en) * 1941-03-08 1947-06-24 Rubatex Products Inc Leakproof fuel tank
US5608017A (en) * 1992-01-29 1997-03-04 Tomoegawa Paper Co., Ltd. Suspension polymerization method
US5717041A (en) * 1992-01-29 1998-02-10 Tomoegawa Paper Co., Ltd. Suspension polymerization method and particles obtained therewith

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2452999A (en) * 1944-06-28 1948-11-02 Us Rubber Co Method of making cellular thermoplastic receptacles
US2531665A (en) * 1946-07-04 1950-11-28 Expanded Rubber Co Ltd Manufacture of expanded thermoplastic materials
US2785440A (en) * 1951-10-26 1957-03-19 Ohio Commw Eng Co Method of manufacturing cushions

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2422797A (en) * 1941-03-08 1947-06-24 Rubatex Products Inc Leakproof fuel tank
US5608017A (en) * 1992-01-29 1997-03-04 Tomoegawa Paper Co., Ltd. Suspension polymerization method
US5717041A (en) * 1992-01-29 1998-02-10 Tomoegawa Paper Co., Ltd. Suspension polymerization method and particles obtained therewith

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