WO1997038043A1 - Polyamide film composition - Google Patents
Polyamide film composition Download PDFInfo
- Publication number
- WO1997038043A1 WO1997038043A1 PCT/KR1996/000047 KR9600047W WO9738043A1 WO 1997038043 A1 WO1997038043 A1 WO 1997038043A1 KR 9600047 W KR9600047 W KR 9600047W WO 9738043 A1 WO9738043 A1 WO 9738043A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- film
- polyamide film
- oil absorption
- mean particle
- slipperiness
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2377/00—Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2377/00—Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
- C08J2377/10—Polyamides derived from aromatically bound amino and carboxyl groups of amino carboxylic acids or of polyamines and polycarboxylic acids
Definitions
- the present invention elates to a polyamide film composition, more specifically, a polyamide film composi- tion having excellent slipperiness and excellent workabili ⁇ ty with no breakage occurred.
- slipperiness of polyamide film is an important property which controls the difficulty of the post-process ⁇ ing.
- Examples of the former group include the methods to provide unevenness to the surface by globular crystal growing by slow cooling in extruding film formation (Japa ⁇ nese Patent Publication No. Sho 51-7708, No. Sho 48-16986), or by crystal growing caused by an addition of crystal seeds(Japanese Patent Publication No. Sho 52-41925) , or the method by spreading silica or talc micro-powder to the film surface(Japanese Patent Publication No. Sho 48-33991), or incorporating the powder into the raw material so that the powder is to be protruded on the film surface after the film formation.
- methods of emboss processing, mat processing, surface roughening by chemicals have been known.
- the method for globular crystal growing by slow cooling restricts the condition for the film formation and deteriorates workability
- the spreading micro-powder method noticeably deteriorates the working environment and has difficulty to control the spreading quantity of the micro-powder.
- the emboss processing, mat processing or treatment with chemical agent includes complicated steps to cause the cost-rise, and deteriorates the transparency and the surface gloss.
- the present inventor has performed intensive study in order to solve the problems of the prior art as described above, and, as a result, found the fact that the oil absorption ability, the mean parti- cle diameter and the addition amount of silicon greatly affect on the slipperiness of the film, and thus completed the present invention of a polyamide film composition which has excellent slipperiness and no breakage during the work to give excellent workability.
- the present invention relates to a polyamide film composition which has improved slipperiness by virtue of the unevenness on the film surface by preparing the film from a polymer mixture admixed with silicsa as an anti ⁇ blocking agent.
- the present invention relates to a polyamide film composition of improved slip ⁇ periness, comprising aliphatic or aromatic diamine, dicarb ⁇ oxylic acid and amino acid, wherein the composition addi ⁇ tionally comprises 0.01 - 2.0 wt% by weight of silicon dioxide having mean particle diameter of 0.5 - 10 ⁇ m and oil absorption ability of 200 ml/100 g or less.
- Oil absorption ability of silica is preferably not more than 200 ml/100 g. If oil absorption ability is more than 200 ml/100 g, a viscous filtrate may clog the filter and form a hard cake so that the filtration can not be per ⁇ formed when the water slurry in which silica have been dis ⁇ persed is added and passed through 800 mesh filter. On the other hand, if the particle has oil absorption ability of 200 ml/100 g or less, the particles hardly aggregate between themselves and make a good dispersion, thus there happens no problem of filtration.
- Mean particle diameter of silica may be 0.5-10 ⁇ m, preferably 1 - 5 ⁇ m. If mean particle diameter is less than 0.5 ⁇ m, the effect of forming unevenness on the surface after film formation may be reduced so that im ⁇ provement of friction coefficient cannot be expected. On the other hand, if the diameter is more than 10 ⁇ m, the possibility of existence of large particles is increased so that the risk of breakage during the film formation may be increased.
- the amount of silica to be added is preferably 0.01 - 2.0 wt% by weight. If the amount is less than 0.01 % by weight, the formation of unevenness is insufficient so that improvement of friction coefficient cannot be expected. On the other hand, if the amount is more than 2.0 wt% by weight, a serious problem occurs because the possibility of aggregation and that of existence of large particles may be increased, whereby breakage may be caused.
- Example 1 Polyamide 6 resin, which had been polymerized by adding 0.2 wt% by weight of silica particles having mean particle diameter of 2.0 ⁇ m and oil absorption ability of 170 ml/lOOg to e-caprolactam, had relative viscosity of 3.45 measured by 96% sulfuric acid method.
- the resin was melted at 260°C, extruded through a loop die, and water cooled to prepare a non-stretched sheet.
- the sheet was stretched by stretching ratio 3.0 in length and width directions by simultaneous biaxial stretching with tubular type to prepare a film.
- the stretched film thus obtained was thermally set in a heat treatment roll and an oven at 140 - 210°C to prepare the film as a final product.
- Example 2 The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.1 wt % by weight of silicon dioxide particles having mean particle diameter of 3.0 ⁇ m and oil absorption ability of
- Example 2 The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.2 wt% by weight of silicon dioxide particles having mean particle diameter of 2.0 ⁇ m and oil absorption ability of 300 ml/lOOg to e-caprolactam to prepare a film.
- Example 2 The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.2 wt% by weight of silicon dioxide particles having mean particle diameter of 0.3 ⁇ m and oil absorption ability of
- Example 2 The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.1 wt% by weight of silicon dioxide particles having mean particle diameter of 12 ⁇ m and oil absorption ability of 300 ml/lOOg to e-caprolactam to prepare a film.
- Example 2 The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.005 wt% by weight of silicon dioxide particles having mean particle diameter of 3.0 ⁇ m and oil absorption ability of 300 ml/lOOg to e-caprolactam to prepare a film.
- Comparative Example 5 The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 3.0 % by weight of silicon dioxide particles having mean parti ⁇ cle diameter of 2.0 ⁇ m and oil absorption ability of 100 ml/lOOg to e-caprolactam to prepare a film.
- films were prepared according to the present invention using silicon oxide of certain mean particle diameter, oil absorption ability in a predeter- mined amount.
- the films had improved slipperiness with low friction coefficient, good filterability, and excellent workability with less than once/day of film breakage.
- the silicon dioxide having mean particle diameter of 0.5 - 10 ⁇ m and oil absorption ability of 200 ml/lOOg or less should be added in an amount of 0.01 - 2.0 wt% by weight when it is added in order to improve the slipperiness of the polyamide film.
- the polyamide films prepared according to the present invention has higher slipperiness than conventional films.
- high-speed productivity is achieved, post-processing such as slitting, printing and lamination are facilitated, and workability is improved with no breakage occurred, according to the present invention.
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
The present invention relates to a polyamide film composition having excellent slipperiness and excellent workability because breakage thereof hardly occurs. According to the present invention, a polyamide film composition comprising aliphatic or aromatic diamine, dicarboxylic acid and amino acid, wherein the composition additionally comprises 0.01 - 2.0 % by weight of silicon dioxide having mean particle diameter of 0.5 - 10 νm and oil absorption ability of 200 ml/100 g or less is provided.
Description
TITLE OF THE INVENTION
POLYAMIDE FILM COMPOSITION
TECHNICAL FIELD
The present invention elates to a polyamide film composition, more specifically, a polyamide film composi- tion having excellent slipperiness and excellent workabili¬ ty with no breakage occurred.
BACKGROUND ART
Besides the own characteristics of each plastic film, an additional requirements to the characteristics are high¬ speed productivity, and an easiness for the post-processing such as slitting, printing and lamination. Even though being a film having excellent quality, there occurs various problems in the industrial use unless it has high productivity and can be readily post-processed.
However, as the hygroscopicity of the polyamide film is increasing, the surface adsorbed water is increasing, and as a result, the slipperiness of the film is deterio- rated. The deterioration of slipperiness causes a serious problem in the post-processing such as slitting, printing and lamination, whereby resulting in a prominent deteriora¬ tion of workability and a reduce of yield owing to the occurrence of inferior goods to raise the cost for produc- tion. Thus, slipperiness of polyamide film is an important property which controls the difficulty of the post-process¬ ing.
Various methods have been developed to enhance the
slipperiness of polyamide film, and the methods are gener¬ ally divided into two groups, of which the one is to reduce the contact area by making minute unevennesε on the sur¬ face, and the other is to heterogenize the surface by using a highly slippery material.
Examples of the former group include the methods to provide unevenness to the surface by globular crystal growing by slow cooling in extruding film formation (Japa¬ nese Patent Publication No. Sho 51-7708, No. Sho 48-16986), or by crystal growing caused by an addition of crystal seeds(Japanese Patent Publication No. Sho 52-41925) , or the method by spreading silica or talc micro-powder to the film surface(Japanese Patent Publication No. Sho 48-33991), or incorporating the powder into the raw material so that the powder is to be protruded on the film surface after the film formation. Besides, methods of emboss processing, mat processing, surface roughening by chemicals have been known.
However, these methods cause some problems during the manufacturing or processing steps, or quality problems.
More specifically, the method for globular crystal growing by slow cooling restricts the condition for the film formation and deteriorates workability, the spreading micro-powder method noticeably deteriorates the working environment and has difficulty to control the spreading quantity of the micro-powder. In the method for film formation by mixing foreign material, it is difficult to disperse homogeneously not to cause a breakage at the stretching. The emboss processing, mat processing or treatment with chemical agent includes complicated steps to cause the cost-rise, and deteriorates the transparency and the surface gloss.
As the latter methods, a process of incorporating
highly slippery foreign materials such as wax, biεamide or the like to form a film, or directly coating on the surface has been known. However, these methods may cause adhesion inferiority during the course of printing or laminating. On the other hand, an attempt to overcome the disad¬ vantages of the prior art by adding silica during the preparation of polyamide film has been tried in Japanese Patent Publication sho 52-41925, however, satisfactory results could not be obtained because of problems such as clogging of filter, occurrence of cake, breakage, and bad workability.
DISCLOSURE OF INVENTION
Under such circumstances, the present inventor has performed intensive study in order to solve the problems of the prior art as described above, and, as a result, found the fact that the oil absorption ability, the mean parti- cle diameter and the addition amount of silicon greatly affect on the slipperiness of the film, and thus completed the present invention of a polyamide film composition which has excellent slipperiness and no breakage during the work to give excellent workability. The present invention relates to a polyamide film composition which has improved slipperiness by virtue of the unevenness on the film surface by preparing the film from a polymer mixture admixed with silicsa as an anti¬ blocking agent. More specifically, the present invention relates to a polyamide film composition of improved slip¬ periness, comprising aliphatic or aromatic diamine, dicarb¬ oxylic acid and amino acid, wherein the composition addi¬ tionally comprises 0.01 - 2.0 wt% by weight of silicon dioxide having mean particle diameter of 0.5 - 10 μm and
oil absorption ability of 200 ml/100 g or less.
In the preparation of this film, what is important is to perform intimate dispersion of the silica particles added so as to avoid film breakage during the process and other problems in workability.
Oil absorption ability of silica is preferably not more than 200 ml/100 g. If oil absorption ability is more than 200 ml/100 g, a viscous filtrate may clog the filter and form a hard cake so that the filtration can not be per¬ formed when the water slurry in which silica have been dis¬ persed is added and passed through 800 mesh filter. On the other hand, if the particle has oil absorption ability of 200 ml/100 g or less, the particles hardly aggregate between themselves and make a good dispersion, thus there happens no problem of filtration.
Mean particle diameter of silica may be 0.5-10 μm, preferably 1 - 5 μm. If mean particle diameter is less than 0.5 μm, the effect of forming unevenness on the surface after film formation may be reduced so that im¬ provement of friction coefficient cannot be expected. On the other hand, if the diameter is more than 10 μm, the possibility of existence of large particles is increased so that the risk of breakage during the film formation may be increased.
The amount of silica to be added is preferably 0.01 - 2.0 wt% by weight. If the amount is less than 0.01 % by weight, the formation of unevenness is insufficient so that improvement of friction coefficient cannot be expected. On the other hand, if the amount is more than 2.0 wt% by weight, a serious problem occurs because the possibility of aggregation and that of existence of large particles may be increased, whereby breakage may be caused.
BEST MODE FOR CARRYING OUT THE INVENTION
Here-in-after, the present invention will be described in more detail, referring to the Examples and Comparative Examples. However, it should be noted that the present invention is not restricted to these Examples.
Example 1 Polyamide 6 resin, which had been polymerized by adding 0.2 wt% by weight of silica particles having mean particle diameter of 2.0 μm and oil absorption ability of 170 ml/lOOg to e-caprolactam, had relative viscosity of 3.45 measured by 96% sulfuric acid method. The resin was melted at 260°C, extruded through a loop die, and water cooled to prepare a non-stretched sheet. The sheet was stretched by stretching ratio 3.0 in length and width directions by simultaneous biaxial stretching with tubular type to prepare a film. The stretched film thus obtained was thermally set in a heat treatment roll and an oven at 140 - 210°C to prepare the film as a final product.
Example 2
The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.1 wt % by weight of silicon dioxide particles having mean particle diameter of 3.0 μm and oil absorption ability of
100 ml/lOOg to e-caprolactam to prepare a film.
Comparative Example 1
The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.2 wt% by weight of silicon dioxide particles having mean particle diameter of 2.0 μm and oil absorption ability of
300 ml/lOOg to e-caprolactam to prepare a film.
Comparative Example 2
The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.2 wt% by weight of silicon dioxide particles having mean particle diameter of 0.3 μm and oil absorption ability of
300 ml/lOOg to e-caprolactam to prepare a film.
Comparative Example 3
The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.1 wt% by weight of silicon dioxide particles having mean particle diameter of 12 μm and oil absorption ability of 300 ml/lOOg to e-caprolactam to prepare a film.
Comparative Example 4
The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 0.005 wt% by weight of silicon dioxide particles having mean particle diameter of 3.0 μm and oil absorption ability of 300 ml/lOOg to e-caprolactam to prepare a film.
Comparative Example 5 The procedure same as Example 1 was repeated with a polyamide 6 resin, which had been polymerized by adding 3.0 % by weight of silicon dioxide particles having mean parti¬ cle diameter of 2.0 μm and oil absorption ability of 100 ml/lOOg to e-caprolactam to prepare a film.
Experiments
Methods and Results
Friction coefficient, film breakage frequency and Haze
of each film prepared by the Examples and Comparative Examples described above were measured. The results are shown in Table 1 and Table 2 below :
Table 1
Ex. Mean particle oil Amount 50% RH No. diameter(μm) absorption added Friction ability (wt%) coefficient (ml/lOOg)
Ex.l 2.0 170 0.2 0.34/0.29
Ex.2 3.0 100 0.1 0.37/0.33
Comp. 2.0 300 0.2 0.63/0.60 Ex.l
Comp. 0.3 300 0.2 0.89/0.90 Ex.2
Comp. 12.0 300 0.1 0.38/0.35
Ex.3
Comp. 3.0 300 1.48/1.80 Ex.4 0.005
Comp. 2.0 100 3.0 0.25/0.24 Ex.5
Table 2
Ex. 70% RH Filtration Film Haze No. Friction Breakage coefficient
Ex.l 0.48/0.43 Good < 1/day 3.0
Ex.2 0.5/0.45 Good < 1/day 2.5
Comp. 1.08/0.98 Caked < 3/day 2.0
Ex.l
Comp. 1.48/1.3 Caked < 2/day 0.5 Ex.2
Comp. 0.47/0.41 Caked < 5/day 6.0
Ex.3
Comp. 2.75/2.90 Good < 1/day 0.4
Ex.4
Comp. 0.28/0.29 Caked Continuous 70 Ex.5 breakage
[Methods for Measurements]
1) Mean particle diameter : Coulter Counter Method 2) Oil absorption ability : JIS K5101
3) Friction Coefficient : ASTM D1894
(In case of low friction coefficient, slipperiness is good, while in case of high friction coefficient, slipperiness is bad. ) 4) Haze : ASTM D1003
Results
In Examples 1 and 2, films were prepared according to the present invention using silicon oxide of certain mean particle diameter, oil absorption ability in a predeter-
mined amount. The films had improved slipperiness with low friction coefficient, good filterability, and excellent workability with less than once/day of film breakage.
In Comparative Example 1 in which oil absorption ability of silicon oxide exceeded the predetermined range, friction coefficient increased to be compared to Examples 1 and 2 so that slipperiness was lowered, cake occurred during the filtration, and workability was deteriorated (less than three times per day of film breakage) compared to the present invention.
In Comparative Example 2 in which both particle diameter and oil absorption ability were out of the prede¬ termined range of the present invention, slipperiness was bad because of high friction coefficient owing to the small particle size, cake occurred during the filtration owing to high oil absorption ability, and the frequency of film breakage was high.
In Comparative Example 3 in which both oil absoptivity and mean particle diameter of silicon dioxide were out of the predetermined range of the present invention, cake occurred during the filtration and Haze was increased to deteriorate transparency of the film though slipperiness had been improved with low friction coefficient. In addition, film breakage frequently occurred to deteriorate the workability.
In Comparative Example 4 in which both oil absoptivity and the amount of silicon dioxide were out of the predeter¬ mined range of the present invention, friction coefficient was highly raised to lower the slipperiness though the mean particle size was within the range.
In Comparative Example 5 in which the amount of silicon dioxide had been increased, slipperiness was im¬ proved with lower friction coefficient, however the work¬ ability was deteriorated by caking during the filtration
and continuous film breakage, and transparency of the film was also deteriorated. Thus, it was noted that the amount of silicon dioxide affects on the film formation.
What is demonstrated by the results of measuring friction coefficient, frequency of film breakage and Haze of the films prepared according to the Examples and Compar¬ ative Examples is that the silicon dioxide having mean particle diameter of 0.5 - 10 μm and oil absorption ability of 200 ml/lOOg or less should be added in an amount of 0.01 - 2.0 wt% by weight when it is added in order to improve the slipperiness of the polyamide film.
Thus, the polyamide films prepared according to the present invention has higher slipperiness than conventional films. In addition, high-speed productivity is achieved, post-processing such as slitting, printing and lamination are facilitated, and workability is improved with no breakage occurred, according to the present invention.
Claims
1. A polyamide film composition comprising aliphatic or aromatic diamine, dicarboxylic acid and amino acid, wherein the composition additionally comprises 0.1 - 2. Owt % by weight of silicon dioxide having mean particle diame¬ ter of 0.5 - 10 μm and oil absorption ability of 200 ml/100 g or less.
2. The polyamide film composition according to claim 1, wherein the mean particle diameter of silicon dioxide is 1 - 5 μm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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PCT/KR1996/000047 WO1997038043A1 (en) | 1996-04-08 | 1996-04-08 | Polyamide film composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/KR1996/000047 WO1997038043A1 (en) | 1996-04-08 | 1996-04-08 | Polyamide film composition |
Publications (1)
Publication Number | Publication Date |
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WO1997038043A1 true WO1997038043A1 (en) | 1997-10-16 |
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PCT/KR1996/000047 WO1997038043A1 (en) | 1996-04-08 | 1996-04-08 | Polyamide film composition |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0962145A1 (en) * | 1998-06-04 | 1999-12-08 | Naturin GmbH & Co | Biaxially oriented, by hand fillable, tubular film for packaging and food stuffs |
US8883917B1 (en) | 2012-09-10 | 2014-11-11 | Nylon Corporation Of America, Inc. | Nylon polymers having a low coefficient of friction and method for the manufacture thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3763082A (en) * | 1972-05-31 | 1973-10-02 | Milprint Inc | Nylon packaging film with thermally developable slip |
JPS62252452A (en) * | 1986-04-25 | 1987-11-04 | Ube Ind Ltd | Polyamide film |
JPH02133434A (en) * | 1988-11-14 | 1990-05-22 | Asahi Chem Ind Co Ltd | Highly slippery polyamide film and its production |
-
1996
- 1996-04-08 WO PCT/KR1996/000047 patent/WO1997038043A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3763082A (en) * | 1972-05-31 | 1973-10-02 | Milprint Inc | Nylon packaging film with thermally developable slip |
JPS62252452A (en) * | 1986-04-25 | 1987-11-04 | Ube Ind Ltd | Polyamide film |
JPH02133434A (en) * | 1988-11-14 | 1990-05-22 | Asahi Chem Ind Co Ltd | Highly slippery polyamide film and its production |
Non-Patent Citations (2)
Title |
---|
PATENT ABSTRACTS OF JAPAN, Vol. 012, No. 132, (C-490); & JP,A,62 252 452, (UBE IND. LTD.), 4 November 1987. * |
PATENT ABSTRACTS OF JAPAN, Vol. 014, No. 363, (C-746); & JP,A,02 133 434, (ASAHI CHEM. IND. CO. LTD.), 22 May 1990. * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0962145A1 (en) * | 1998-06-04 | 1999-12-08 | Naturin GmbH & Co | Biaxially oriented, by hand fillable, tubular film for packaging and food stuffs |
US8883917B1 (en) | 2012-09-10 | 2014-11-11 | Nylon Corporation Of America, Inc. | Nylon polymers having a low coefficient of friction and method for the manufacture thereof |
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