US2731370A - Package coated with paraffin and a polymerized product of a cyclopentadiene - Google Patents
Package coated with paraffin and a polymerized product of a cyclopentadiene Download PDFInfo
- Publication number
- US2731370A US2731370A US353662A US35366253A US2731370A US 2731370 A US2731370 A US 2731370A US 353662 A US353662 A US 353662A US 35366253 A US35366253 A US 35366253A US 2731370 A US2731370 A US 2731370A
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- United States
- Prior art keywords
- paper
- paraffin
- package
- melting point
- containers
- Prior art date
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- Expired - Lifetime
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- 239000012188 paraffin wax Substances 0.000 title claims description 19
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 title claims description 13
- 238000002844 melting Methods 0.000 claims description 24
- 230000008018 melting Effects 0.000 claims description 20
- 238000000576 coating method Methods 0.000 claims description 16
- 239000011248 coating agent Substances 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 15
- 238000006116 polymerization reaction Methods 0.000 claims description 11
- 239000007787 solid Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 239000000123 paper Substances 0.000 description 27
- 229930195733 hydrocarbon Natural products 0.000 description 17
- 150000002430 hydrocarbons Chemical class 0.000 description 17
- 239000001993 wax Substances 0.000 description 10
- 239000000203 mixture Substances 0.000 description 9
- 239000011087 paperboard Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- 230000001954 sterilising effect Effects 0.000 description 6
- 238000004659 sterilization and disinfection Methods 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 235000013305 food Nutrition 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000155 melt Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000008267 milk Substances 0.000 description 4
- 210000004080 milk Anatomy 0.000 description 4
- 235000013336 milk Nutrition 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 230000035515 penetration Effects 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 239000004753 textile Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 2
- 239000000975 dye Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 230000035900 sweating Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000001680 brushing effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 125000000753 cycloalkyl group Chemical group 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 208000001848 dysentery Diseases 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011874 heated mixture Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 235000021056 liquid food Nutrition 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009183 running Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000010454 slate Substances 0.000 description 1
- 235000021055 solid food Nutrition 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- A23L3/00—
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D65/00—Wrappers or flexible covers; Packaging materials of special type or form
- B65D65/38—Packaging materials of special type or form
- B65D65/40—Applications of laminates for particular packaging purposes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/10—Coatings without pigments
- D21H19/14—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
- D21H19/18—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising waxes
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31801—Of wax or waxy material
- Y10T428/31804—Next to cellulosic
- Y10T428/31808—Cellulosic is paper
Definitions
- This invention relates to an improved package. it more particularly relates to a package for liquid or solid consumer goods, and in particular foods, which is capable of being sterilized.
- Solid and liquid foods are preferably packaged in a form in which they may be distributed and stored and sold to the individual consumer.
- the coating of the packages to render the same impermeable to microorganisms such as germs followed by sterilization insures that the contents will remain in unobjectionable and stable condition.
- Packing methods of this type are absolutely essential in the sale and distribution of milk and other foods and goods which must be kept free from contamination for hygienic purposes.
- glass containers Up to the present, glass containers have received the most wide-spread use for this purpose since the same will stand up under any sterilization temperatures. Glass containers, however, have the disadvantage in that their relatively high cost often prohibit their use as a throw-away container and the empty containers must be returned and collected.
- Paper and paper-board packages and containers have been used in the food and related industries. These containers have their inner and/or outer surfaces coated with paraifin or artificial resin varnishes. The cost of these air-tight packages is so relatively small that the be thrown away or destroyed as a useless waste material.
- One object of this invention is a package which may be produced in a simple manner at low cost and which will not deteriorate at sterilization temperatures. This and still further-objects will become apparent from the following description:
- paraflins of a very high melting point and of a low melting point from the catalytic hydrogenation of carbon monoxide may be combined to form sizes and coatings for packages which will meet all the requirements as to use with respect to temperature resistance and hardness. It has been found that it is possible to increase the adhesiveness of the parafiin mixture to the walls of the package which may, for example, consist of metal, paper or textile by adding conventional ma terials such as esters, resins or gelatines.
- the high softening temperatures or" the hard waxes and their chemical resistance permit sterilization temperatures of as high as approximately 98 C.
- Milk and similar foods which are conventionally sterilized and pasteurized at about to C. may be freed from microorganisms in the usual manner after being filled into the package which has been made liquid-tight with the hard parafiins.
- the use of the hard wax in accordance with the invention, is not limited to the coating and/or impregnation ofpackages of paper, paper-board and similar materials. It may be used in an analogous manner to coat the inner surfaces of metal containers such as of cans or tubes. Containers so coated may be sterilized with their contents at temperatures of as high as C. Without alfecting the taste of the contents or injuring the inner coating layer.
- hydrocarbons which are produced by polymerizing cyclopentadicn or dicyclopentadien.
- the high melting hydrocarbons of this type may be produced from cyclopentadien or dicyclopentadien which are presfor example, in the first runnings of the distillation of raw benzene, by heating them to elevated temperatures with or Without the use of catalysts. It .has been found particularly advantageous to heat the starting material to about 150 to 250 C. without the use of catalysts. This results in the production of hydrocarbons which contain several five membered rings and have a melting point which ranges above C., and, in some cases, even in excess of 200 C. A still further improvement of these high-melting hydrocarbons is possible by fractional distillation in vacuo,-by selective extraction and/or hydrogenation.
- high-melting point hydrocarbons obtained by the polymerization of cyclopentadien or dicyclopentadien should be mixed with the parafiin hydrocarbon of a high melting point, i. e., the hard Waxes.
- polymerization product may be mixed the hard wax, such as slate parafiin, hard parafi'in, or other waxes. It is preferable to use mixtures contain of the polymerization productof the cyclopentadien or dicyclopentadien, and 80-95% of the high melting paratfins.
- The'high-melting parafiins i. e. the hard waxes
- the lining and/or coating of metal containers may be effected by immersing, brushing, or spraying. Even very thin layers of, for example, 30-40 grams of paraffin per square meter provide a sufficient and durable protection of the surface of, for example, sheet iron against corrosion from the contents of the package.
- the process uses hydrocarbons for the temperature-resistant impregnation of containers produced from paper, paper-board, textiles, or for the coating of containers produced from metal and other materials.
- the melting point of the hydrocarbon mixtures used must be so high that it is possible to sterilize the filled package. For this reason the hydrocarbon mixture used must contain larger portions of high molecular weight aliphatic or cyclic hydrocarbons. Low molecular weight hydrocarbons should be present only to the extent that the melting point will not range below 90 C.
- the adhesiveness of the mixtures of high melting point hydrocarbons used in accordance with the invention is largely dependent on the brittleness of the material. Soft hydrocarbons adhere better in and to the surfaces to be coated therewith. The adhesiveness of the hydrocarbon mixtures used in accordance with the invention may considerably be improved by softeners of the conventional type and, for example, by polyethylene.
- Example 1 By means of the catalytic carbon monoxide hydrogenation there was produced a hard parafiin which substantially contained only hydrocarbons boiling above 460 C. It had a solidification point of 98 C., a penetration number of 1.1 and an average molecular size of Cara. This hard paraffin was melted and a paper cup was immersed into the melt. The paraffin-coated paper cup was subsequently put into a drying chamber heated to 120 C. where it was left for several hours. During this time, part of the paraffin coating was sweated off. Approximately 15 grams of paraffin per square meter of paper remained back. A paper cup thus impregnated with paraffin resisted temperatures of as high as 100 C.
- Example 2 A melt of hard parafiin produced by the Fischer- Tropsch synthesis and substantially containing only hydrocarbons boiling above 380 C. and having a solidification point of 95 C., a penetration number of 1.9 and an average molecular size of C41 was used for the impregnation of paper.
- the paper to be impregnated was immersed into the paraffin melt and subsequently sweated off at 120 C. for a longer period. "From the paper thus treated there were produced paper bags which during the sterilization of milk previously filled in resisted temperatures of as high as 95 C.
- Example 3 The hard paraffin used in Example 1 was extracted by means of a heptane fraction. This resulted in an extracted fraction which had a solidification point of 110 C. and a penetration number of 0.1. A paper cup was immersed into the melt of this paraffin and subsequently placed for a longer period into a drying chamber heated to 130 C. A part of the paraffin was thereby removed by sweating off. The paper cup thus treated was completely temperature-resistant up to C.
- Example 4 70 parts byweight of the petroleum slab paraffin used in Example 4 were mixed with 30 parts by weight of the hard parafiin used in Example 1. A paper cup was immersed into the melted paraffin mixture and subsequently heated for a longer period at C. in a drying cham' ber thereby sweating off part of the parafiin. Thereafter, the paper cup was completely temperature-resistant up to 70 C.
- Example 6 A web of paper was passed through a heated mixture consisting of 40 parts by weight of the petroleum slab paraffin used in Example 4 and 60 parts by weight of the hard paraffin used in Example 1. Following this treatment, the paper was conducted for a longer period through a drying chamber heated to 120 C. The paper thus impregnated was used for the production of bags which were filled with milk. The filled containers could be heated to temperatures of as high as 80 C. without detrimentally affecting their contents.
- Example 7 Dicyclopentadien was heated for about 10 hours at approximately 200 C. This resulted in the formation of polymerization products of dicyclopentadien which were hydrogenated at -150 C. and slightly. elevated pressure with the use of nickel catalysts. The hydrogenated polymerization product was dissolved in hot benzene and separated from insoluble products by filtration. By cooling the filtrate, hydrogenated pentameric cyclopentadien was obtained in the form of a white powder the melting point of which was 290310 C.
- Example 8 A wax having a melting point of 102 C. was obtained tion product.
- a sterilizable package for solid and liquid consumer goods comprising a base material defining the package and a surface coating of paraflin having a melting point of above 90 C., said coating additionally containing from 2-70% of a polymerization product having a melting point in excess of 100 C. and selected fromthe group consisting of polymerization products of cyclopentadien, dicyclopentadien and hydrogenated polymerization products of cyclopentadien and dicyclopentadien.
- Sterilizable package according to claim 1 in which said coating contains from 5-20% of said polymeriza- 3. Sterilizable package according to claim 1, in which said group member is refined.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Paper (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Description
empty packages may United States Patent Ofi 2,731,370 Patented Jan. 17, 1956 ice PACKAGE COATED WITH PARAFFIN AND A POLYMERIZED PRUDUCT OF A CYCLO- PENTADIENE Heinrich Tramm, Mulheim-Ruhr-Speldorf, and (ltto Roelen, Oberhausen-Holten, Germany, assignors t Ruhrchemie Aktiengesellschaft, Uberhausen-loiten, Germany, a German corporation 1 No Drawing. Application May 7, 1953, Serial No. 353,662
Claims priority, application Germany May 14, 1952 5 Claims. (Cl. 117 155) This invention relates to an improved package. it more particularly relates to a package for liquid or solid consumer goods, and in particular foods, which is capable of being sterilized.
Solid and liquid foods are preferably packaged in a form in which they may be distributed and stored and sold to the individual consumer. The coating of the packages to render the same impermeable to microorganisms such as germs followed by sterilization insures that the contents will remain in unobjectionable and stable condition. Packing methods of this type are absolutely essential in the sale and distribution of milk and other foods and goods which must be kept free from contamination for hygienic purposes. Up to the present, glass containers have received the most wide-spread use for this purpose since the same will stand up under any sterilization temperatures. Glass containers, however, have the disadvantage in that their relatively high cost often prohibit their use as a throw-away container and the empty containers must be returned and collected.
Paper and paper-board packages and containers have been used in the food and related industries. These containers have their inner and/or outer surfaces coated with paraifin or artificial resin varnishes. The cost of these air-tight packages is so relatively small that the be thrown away or destroyed as a useless waste material.
Low-cost packages and containers produced from waxed paper and waxed paper-board materials are very advantageous in view of their extremely low cost and the easy manner in which they may be produced. These Waxed paper and paper-board packages and containers, however, have the disadvantage that they will only withstand temperatures up to approximately 50 C. due to the low melting point of the parifiin grades conventionally used. At temperaturesin excess of this, leakages and a detrimental influence on the taste of the content of the package must be expected. Thus, it is impossible to sterilize the filled, sealed package of this type. tails the necessity of a prior sterilization of the material to be packed which has the disadvantage that mold or other harmful micro-organisms may be introduced into the material to be packed by both the empty package and the filling operation.
One object of this invention is a package which may be produced in a simple manner at low cost and which will not deteriorate at sterilization temperatures. This and still further-objects will become apparent from the following description:
It has now been found that the disadvantages of the prior art are not encountered if the sizing, lining and/or coating of packages consisting of paper, paper-board or similar material is effected with paraflin grades having a melting point which ranges above about 90 to 120 C., i. e. hard waxes.
It has been found that paratiins of high melting point produced by the catalytic hydrogenation of carbon monoxide are particularly well suited for this purpose.
It has further been found, in accordance with the invention, that paraflins of a very high melting point and of a low melting point from the catalytic hydrogenation of carbon monoxide may be combined to form sizes and coatings for packages which will meet all the requirements as to use with respect to temperature resistance and hardness. It has been found that it is possible to increase the adhesiveness of the parafiin mixture to the walls of the package which may, for example, consist of metal, paper or textile by adding conventional ma terials such as esters, resins or gelatines.
It is possible to produce the containers in accordance with the invention in the identical manner that the containers with the paratfin grades of the low melting point previously used were produced. The impregnation and/ or coating of the paper, paper-board, textile and similar materials with the hard waxes, in accordance with the invention, is effected in the identical manner as the coating was with the paraffin grades of the lower melting points previously used except that a corresponding increase in the operating temperature is necessary. in addition, the manufacture, the handling and sealing of the packages in accordance with the invention requires no change of equipment from the conventional equipment and procedures used at the present time.
The high softening temperatures or" the hard waxes and their chemical resistance permit sterilization temperatures of as high as approximately 98 C. Milk and similar foods which are conventionally sterilized and pasteurized at about to C. may be freed from microorganisms in the usual manner after being filled into the package which has been made liquid-tight with the hard parafiins.
The use of the hard wax, in accordance with the invention, is not limited to the coating and/or impregnation ofpackages of paper, paper-board and similar materials. It may be used in an analogous manner to coat the inner surfaces of metal containers such as of cans or tubes. Containers so coated may be sterilized with their contents at temperatures of as high as C. Without alfecting the taste of the contents or injuring the inner coating layer.
It is of particular advantage, in accordance with the invention, to use hydrocarbons which are produced by polymerizing cyclopentadicn or dicyclopentadien. The high melting hydrocarbons of this type may be produced from cyclopentadien or dicyclopentadien which are presfor example, in the first runnings of the distillation of raw benzene, by heating them to elevated temperatures with or Without the use of catalysts. It .has been found particularly advantageous to heat the starting material to about 150 to 250 C. without the use of catalysts. This results in the production of hydrocarbons which contain several five membered rings and have a melting point which ranges above C., and, in some cases, even in excess of 200 C. A still further improvement of these high-melting hydrocarbons is possible by fractional distillation in vacuo,-by selective extraction and/or hydrogenation.
These high-melting point hydrocarbons obtained by the polymerization of cyclopentadien or dicyclopentadien should be mixed with the parafiin hydrocarbon of a high melting point, i. e., the hard Waxes. polymerization product may be mixed the hard wax, such as slate parafiin, hard parafi'in, or other waxes. It is preferable to use mixtures contain of the polymerization productof the cyclopentadien or dicyclopentadien, and 80-95% of the high melting paratfins.
with 98-30% of 270% of this The'high-melting parafiins, i. e. the hard waxes, exhibit a certain brittleness at low temperatures, which, in certain cases, is undesirable for production of the containers in accordance with the invention. It has been found that this disadvantage may be overcome, if necessary or desired, by mixing the high-melting parafi'ins with softening materials prior to use. Examples of materials which are suitable for this purpose include highboiling hydrocarbons which have been found in small quantities to impart a sufficient elasticity to the highmelting paraflins without detrimentally influencing the contents of the package due to their completely inert properties.
The lining and/or coating of metal containers may be effected by immersing, brushing, or spraying. Even very thin layers of, for example, 30-40 grams of paraffin per square meter provide a sufficient and durable protection of the surface of, for example, sheet iron against corrosion from the contents of the package.
The process, according to the invention, uses hydrocarbons for the temperature-resistant impregnation of containers produced from paper, paper-board, textiles, or for the coating of containers produced from metal and other materials. The melting point of the hydrocarbon mixtures used must be so high that it is possible to sterilize the filled package. For this reason the hydrocarbon mixture used must contain larger portions of high molecular weight aliphatic or cyclic hydrocarbons. Low molecular weight hydrocarbons should be present only to the extent that the melting point will not range below 90 C.
The adhesiveness of the mixtures of high melting point hydrocarbons used in accordance with the invention is largely dependent on the brittleness of the material. Soft hydrocarbons adhere better in and to the surfaces to be coated therewith. The adhesiveness of the hydrocarbon mixtures used in accordance with the invention may considerably be improved by softeners of the conventional type and, for example, by polyethylene.
Further details are to be seen from the following examples which are given for illustration and not limitation.
Example 1 By means of the catalytic carbon monoxide hydrogenation there was produced a hard parafiin which substantially contained only hydrocarbons boiling above 460 C. It had a solidification point of 98 C., a penetration number of 1.1 and an average molecular size of Cara. This hard paraffin was melted and a paper cup was immersed into the melt. The paraffin-coated paper cup was subsequently put into a drying chamber heated to 120 C. where it was left for several hours. During this time, part of the paraffin coating was sweated off. Approximately 15 grams of paraffin per square meter of paper remained back. A paper cup thus impregnated with paraffin resisted temperatures of as high as 100 C.
Example 2 A melt of hard parafiin produced by the Fischer- Tropsch synthesis and substantially containing only hydrocarbons boiling above 380 C. and having a solidification point of 95 C., a penetration number of 1.9 and an average molecular size of C41 was used for the impregnation of paper. The paper to be impregnated was immersed into the paraffin melt and subsequently sweated off at 120 C. for a longer period. "From the paper thus treated there were produced paper bags which during the sterilization of milk previously filled in resisted temperatures of as high as 95 C.
Example 3 The hard paraffin used in Example 1 was extracted by means of a heptane fraction. This resulted in an extracted fraction which had a solidification point of 110 C. and a penetration number of 0.1. A paper cup was immersed into the melt of this paraffin and subsequently placed for a longer period into a drying chamber heated to 130 C. A part of the paraffin was thereby removed by sweating off. The paper cup thus treated was completely temperature-resistant up to C.
Example 4 Example 5 70 parts byweight of the petroleum slab paraffin used in Example 4 were mixed with 30 parts by weight of the hard parafiin used in Example 1. A paper cup was immersed into the melted paraffin mixture and subsequently heated for a longer period at C. in a drying cham' ber thereby sweating off part of the parafiin. Thereafter, the paper cup was completely temperature-resistant up to 70 C.
Example 6 A web of paper was passed through a heated mixture consisting of 40 parts by weight of the petroleum slab paraffin used in Example 4 and 60 parts by weight of the hard paraffin used in Example 1. Following this treatment, the paper was conducted for a longer period through a drying chamber heated to 120 C. The paper thus impregnated was used for the production of bags which were filled with milk. The filled containers could be heated to temperatures of as high as 80 C. without detrimentally affecting their contents.
Example 7 Dicyclopentadien was heated for about 10 hours at approximately 200 C. This resulted in the formation of polymerization products of dicyclopentadien which were hydrogenated at -150 C. and slightly. elevated pressure with the use of nickel catalysts. The hydrogenated polymerization product was dissolved in hot benzene and separated from insoluble products by filtration. By cooling the filtrate, hydrogenated pentameric cyclopentadien was obtained in the form of a white powder the melting point of which was 290310 C.
By mixing 90 parts by weight of the hard paraffin used in Example 1 and 10 parts by weight of the hydrogenated pentameric cyclopentadien, a hydrocarbon mixture was obtained the pour point of which was C. This wax was melted and a paper cup was immersed into the melt and thereafter placed for a longer period in a drying chamber heated to 120C. Thereafter, the paper cup was filled with a solution of dye stuff and exposed for an hour to the action of a stream of water vapor which was heated to 110 C. The mixture of hard parafiin and hydrogenated pentacyclopentadien was found to be completely impermeable at this temperature since no solution of dye stuff had leaked through the paper cup.
Example 8 A wax having a melting point of 102 C. was obtained tion product.
from the impregnated sheets of paper withstood temperatures of as high as 100 C.
We claim:
1. A sterilizable package for solid and liquid consumer goods comprising a base material defining the package and a surface coating of paraflin having a melting point of above 90 C., said coating additionally containing from 2-70% of a polymerization product having a melting point in excess of 100 C. and selected fromthe group consisting of polymerization products of cyclopentadien, dicyclopentadien and hydrogenated polymerization products of cyclopentadien and dicyclopentadien.
2. Sterilizable package according to claim 1, in which said coating contains from 5-20% of said polymeriza- 3. Sterilizable package according to claim 1, in which said group member is refined.
4. Sterilizable package according to claim 1, in which said base material consists of paper material.
5. Sterilizable package according to claim 1, in which said coating is mixed with a material to increase the adhesiveness of said coating to a coated surface.
References Cited in the file of this patent UNITED STATES PATENTS 2,594,547 Fischer Apr. 29, 1952
Claims (1)
1. A STERILIZABLE PACKAGE FOR SOLID AND LIQUID CONSUMER GOODS COMPRISING A BASE MATERIAL DEFINING THE PACKAGE AND A SURFACE COATING OF PARAFFIN HAVING A MELTING POINT OF ABOVE 90* C., SAID COATING ADDITIONALLY CONTAINING FROM 2-7% OF A POLYMERIZATION PRODUCT HAVING A MELTING POINT IN EXCESS OF 100* C. AND SELECTED FROM THE GROUP CONSISTING OF POLYMERIZATION PRODUCTS OF CYCLOPENTADIEN, DICYCLOPENTADIEN AND HYDROGENATED POLYMERIZATION PRODUCTS OF CYCLOPENTADIEN AND DICYCLOPENTADIEN.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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DE2731370X | 1952-05-14 |
Publications (1)
Publication Number | Publication Date |
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US2731370A true US2731370A (en) | 1956-01-17 |
Family
ID=7997374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US353662A Expired - Lifetime US2731370A (en) | 1952-05-14 | 1953-05-07 | Package coated with paraffin and a polymerized product of a cyclopentadiene |
Country Status (2)
Country | Link |
---|---|
US (1) | US2731370A (en) |
NL (1) | NL178288B (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2967781A (en) * | 1959-10-07 | 1961-01-10 | Atlantic Refining Co | Wax coating composition and paperboard coated therewith |
US3084147A (en) * | 1958-06-27 | 1963-04-02 | Velsicol Chemical Corp | Thermal polymerization of dicyclopentadiene |
US3090698A (en) * | 1961-02-14 | 1963-05-21 | Standard Oil Co | Process for irradiating high hydrocarbon coatings on metal to form polymeric coatings and resultant article |
US3321428A (en) * | 1963-11-04 | 1967-05-23 | Du Pont | Composition containing wax and an ethylene-unconjugated diolefin interpolymer |
US3398020A (en) * | 1961-02-08 | 1968-08-20 | Eastman Kodak Co | Hydrophobic polyhydrocarbon substrates coated with cyclopentadiene homopolymer |
US4010130A (en) * | 1973-10-24 | 1977-03-01 | Arakawa Rinsan Kagaku Kogyo Kabushiki Kaisha | Hydrogenated resin and compositions containing the same |
US20050158442A1 (en) * | 2003-12-19 | 2005-07-21 | Werner Westermann | Wax-coated cheese |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2594547A (en) * | 1948-05-14 | 1952-04-29 | Karl A Fischer | Fabric material provided with paraffin coating |
-
0
- NL NLAANVRAGE7414629,A patent/NL178288B/en unknown
-
1953
- 1953-05-07 US US353662A patent/US2731370A/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2594547A (en) * | 1948-05-14 | 1952-04-29 | Karl A Fischer | Fabric material provided with paraffin coating |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3084147A (en) * | 1958-06-27 | 1963-04-02 | Velsicol Chemical Corp | Thermal polymerization of dicyclopentadiene |
US2967781A (en) * | 1959-10-07 | 1961-01-10 | Atlantic Refining Co | Wax coating composition and paperboard coated therewith |
US3398020A (en) * | 1961-02-08 | 1968-08-20 | Eastman Kodak Co | Hydrophobic polyhydrocarbon substrates coated with cyclopentadiene homopolymer |
US3090698A (en) * | 1961-02-14 | 1963-05-21 | Standard Oil Co | Process for irradiating high hydrocarbon coatings on metal to form polymeric coatings and resultant article |
US3321428A (en) * | 1963-11-04 | 1967-05-23 | Du Pont | Composition containing wax and an ethylene-unconjugated diolefin interpolymer |
US4010130A (en) * | 1973-10-24 | 1977-03-01 | Arakawa Rinsan Kagaku Kogyo Kabushiki Kaisha | Hydrogenated resin and compositions containing the same |
US20050158442A1 (en) * | 2003-12-19 | 2005-07-21 | Werner Westermann | Wax-coated cheese |
Also Published As
Publication number | Publication date |
---|---|
NL178288B (en) |
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