Heat-sealable biodegradable packaging material, a package made thereof, and use of a resin in extrusion coating

Abstract

The invention concerns a heat-sealable biodegradable packaging material, which comprises a fibrous substrate and one or more polymer coating layers extruded onto said substrate. According to the invention the packaging material includes at least one polymer coating layer containing polylactide and at least about 1 weight-% of terpene phenolic resin blended therewith. The invention further concerns a heat-sealed product package made from the packaging material, as well as uses of the resin as blends with polylactide in extrusion coating, for improving line speed and neck-in in extrusion, adhesivity of the coating to the fibrous substrate, and heat-sealability of the coating.

Claims

1. A method of manufacturing a heat-sealed biodegradable container or package, comprising the steps of (a) extruding a polymer blend consisting of polylactide and at least about 1 weight-% and at most 10 weight-% of terpene phenolic resin as a melt onto a fibrous board base having a basis weight of 170 to 350 g/m.sup.2 on a moving line, to produce a heat-sealable board comprising a coating layer of said polymer blend on said board base, wherein said coating layer of said polymer blend is a monolayer having a basis weight of 10 to 30 g/m.sup.2, and (b) forming the container or package from the polymer coated board thus obtained by introduction of heat to melt said polymer coating and by heat sealing the board sides or surfaces together.

2. The method of claim 1, wherein said polymer coating layer contains polylactide and at least about 2 weight-% of terpene phenolic resin blended therewith.

3. The method of claim 1, wherein said polymer coating layer contains at least 4 weight-% of terpene phenolic resin blended with polylactide.

4. The method of claim 1, wherein said polymer coating layer contains at least 10 weight-% of terpene phenolic resin blended with polylactide.

5. The method of claim 1, wherein said polymer coating layer contains at most 20 weight-% of terpene phenolic resin blended with polylactide.

6. The method of claim 1, wherein said polymer coating layer is in a direct contact with the fibrous board base.

7. The method of claim 1, wherein said polymer coating layer is the uppermost surface layer of a multilayer coating coextruded at step (a) onto the fibrous board base.

8. The method of claim 1, wherein the terpene phenolic resin is made from -pinene and phenol.

9. The method of claim 1, wherein the heat sealability of said polymer coating layer is improved by blending the minor share of terpene phenolic resin with a share of at least 80 wt-% of polylactide.

10. The method of claim 1, wherein the line speed in extrusion of said polymer coating layer is increased by blending the minor share of terpene phenolic resin with a share of at least 80 wt-% of polylactide.

11. The method of claim 1, wherein the neck-in in extrusion of said polymer coating layer is reduced by blending the minor share of terpene phenolic resin with a share of at least 80 wt-% of polylactide.

12. The method of claim 1, wherein adhesion of said polymer coating layer to the fibrous board base is improved by blending the minor share of terpene phenolic resin with a share of at least 80 wt-% of polylactide.

13. The method of claim 1, wherein said package is a heat-sealed product package.

14. The method of claim 1, wherein said container is a disposable drinking cup.

15. The method of claim 1, wherein the polymer coating is heat sealed by use of hot air.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 shows the effect of the blended terpene phenolic resin on the line speed in extrusion.

(2) FIGS. 2 and 3 show the effect of the blended terpene phenolic resin on adhesion of the extruded polylactide coatings to the board substrate.

(3) FIG. 4 shows the effect of the blended terpene phenolic resin on the neck-in in extrusion.

(4) FIG. 5 shows the effect of the blended terpene phenolic resin on the uncoated topside of the fibrous board substrate at low air temperature.

(5) FIGS. 6-9 show, as examples, four structural embodiments of the packaging material according to the invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(6) The terpene used to produce the resin is a low-cost, coniferous wood-based material. To the applicant's knowledge such resin has not been previously used for polymer blend coatings of biodegradable paper or board packages. Examples of the terpenes are a-pinene and p-pinene. Combined with the use of polylactide terpene phenolic resin increases the share of biorenewable materials contained in the biodegradable packages.

(7) The invention covers use of terpene phenolic resins made from at least phenol and terpene monomers. One or more further monomers may be used for the resin. As noted above, the terpene monomer may be for instance a-pinene or p-pinene.

(8) Examples of the phenol monomer are phenol and various alkyl and alkoxyphenols, and examples of the further monomers are cyclic or acyclic unsaturated olefins, such as e.g. diisobutylene and cyclopentadiene. Manufacture of such products has been described in the patent literature, the patents U.S. Pat. Nos. 5,457,175, 5,723,566, 5,844,063 and 6,160,083 being cited as examples, Terpene phenolic resins useful in the invention are available as commercial products.

(9) Preferably the biodegradable polymer coating layer contains at least 2 weight-%, more preferably at least 4 weight-%, and most preferably at least 10 weight-% of terpene phenolic resin blended with polylactide. The share of polylactide in said blends would be at most 98 weight-%, more preferably at most 96 weight-%, and most preferably at most 90 weight-%, respectively.

(10) The upper limit for the share of terpene phenolic resin in the blend may be 20 weight-%, preferably 15 weight-%, the remaining 80 weight-%, preferably 85 weight-%, being polylactide. Suitably the blend would substantially consist of 5-15 weight-% of terpene phenolic resin and 85-95 weight-% of polylactide.

(11) The fibrous substrate in the packaging material may be paper or board, paperboard as well as cardboard.

(12) The biodegradable polymer coating layer as discussed above may be in a direct contact with the fibrous substrate of the packaging material. The terpene phenolic resin serves to improve adhesion of the coating layer to the underlying fibrous substrate. In case of a multilayer coating said coating layer would be the lower-most layer.

(13) The biodegradable polymer coating layer as discussed above may also form the uppermost surface layer of the coated packaging material. In this case the terpene phenolic resin serves to improve the heat-sealability of the polymer coated packaging material. If the coating is a monolayer coating its aim is to improve both adhesion to the fibrous substrate and heat-sealability.

(14) In case of a multilayer coating each layer should consist of biodegradable polymers so as to secure biodegradability of the packaging material as a whole. The material may have a polymer coating on one side or on both sides thereof. The coatings on the opposite sides of the fibrous substrate may be similar or differ from each other.

(15) The heat-sealed product package according to the invention is a closed package partially or, preferably, completely made of the packaging material as described above. Such sealed packages may be carton packages for dry products such as chocolate, tobacco, cosmetics, bottled alcoholic beverages, etc., in which at least the outer surface is polymer coated, the heat seal having the coated outer side of the package sealed to the coated or uncoated inner side of the package.

(16) The invention also includes heat-sealed liquid packages, in which at least the inner surface of the package has a polymer coating to prevent wetting of the fibrous substrate. Preferably the fibrous substrate is polymer coated on both sides. The inner side of the package may have a multilayer coating including at least one oxygen barrier layer and an innermost heat-seal layer.

(17) The invention even comprises heat-sealed containers made of the packaging material according to the invention, such as disposable drinking cups for hot or cold drinks such as coffee, juice etc., in which the polymer coating lies in the inside of the container in contact with the drink.

(18) The invention includes use of terpene phenolic resin as a blend with polylactide to improve the heat-sealability of an extruded polymer coating layer made from said blend. An addition of 2 weight-% of the resin brought a clear improvement in terms of the hot air temperature needed for the heat-sealing, and increasing the share of the resin to 10 weight-% produced a progressively improving result as decreasing sealing air temperatures required.

(19) The invention further includes use of terpene phenolic resin as a blend with polylactide for increased line speed in extrusion of a polymer coating layer comprising said blend. An addition as small as 1 weight-% of the resin allows nearly doubling the line speed as compared to pure polylactide, and additions in the range of 1-10 weight-% have been found to yield good results.

(20) The invention even includes use of terpene phenolic resin as a blend with polylactide for reduced neck-in in extrusion of a polymer coating layer comprising said blend. A clear reduction is achieved by adding 2 weight-% of the resin to the blend, and an addition of 10 weight-% brings a significant further improvement.

(21) In each case the blend is preferably used for extrusion of a polymer coating layer onto a fibrous paper or board substrate of a packaging material.

(22) Furthermore, the invention includes use of terpene phenolic resin as a blend with polylactide for improved adhesion as a polymer coating layer comprising said blend is extruded onto a fibrous paper or board substrate of a packaging material. A significant improvement as compared to pure polylactide was found with additions of 4 to 10 weight-% of the resin in the blend. Due to the improvement the weight of the polymer coating layer may be reduced, with material savings as a result.

EXAMPLES

(23) In the following the invention is illustrated by means of laboratory tests. Extrusion grade polylactide was used as the basic coating polymer, which was blended with various amounts of terpene phenolic resin Sylvares TP 2040E by Arizona Chemicals. 47 to 49 weight-% of the resin was first compounded with 53 to 51 weight-% of polylactide, respectively, to form a masterbatch, and 2, 4, 8 and 20 weight-% of the masterbatch was then blended with polylactide to obtain the test materials. Thus the shares of the resin in the test materials were about 1, 2, 4 and 10 weight-%, respectively.

(24) The blended test materials were then extruded as monolayers onto one side of a cupboard substrate having a weight of 210 g/m.sup.2, by varying the extruded coating weights and the line speed in extrusion. The results are shown in FIGS. 1-5.

(25) The effect of the blended terpene phenolic resin on the line speed in extrusion can be seen from the measured results in FIG. 1. By way of trials the maximal line speed for each blend was determined, and the corresponding polymer coating weight was measured. Due to the technique the amounts of extruded polymer, measured as coating weights, varied slightly for the different blends. However, the improvement as compared to the highest possible line speed with pure polylactide was remarkable even with the lowest terpene phenolic resin content of 1 weight-%, and was maintained throughout the tested range of 1-10 weight-%. The working properties of polylactide are thus significantly improved by the blending according to the invention.

(26) FIGS. 2 and 3 show the effect of the blended terpene phenolic resin on adhesion of the extruded polylactide coatings to the board substrate. Adhesion is classified on a scale of 0 to 5, wherein adhesion level 0 represents no adhesion at all. At level 1 the coating is slightly sticking to the board surface, not loose any more, while level 5 represents the best possible adhesion. Coating weight of about 22 g/m.sup.2 was used in the test series of FIG. 2. A 4 weight-% share of the resin in the blend brought a rise of the adhesion level from 2 to 3.

(27) The test series of FIG. 3 sought out the minimum amount of extruded polymer in order to achieve the adhesion level 3. It is seen that increase of the blended terpene phenolic resin progressively improves adhesion, as demonstrated by the diminishing amount of the polymer required.

(28) FIG. 4 shows the effect of the blended terpene phenolic resin on the neck-in in extrusion. A minor improvement was achieved with smaller amounts of blended resin, whereas a share of 10 weight-% of the resin produced a considerable improvement. Reduction of neck-in helps the control of the extrusion process.

(29) In the test series of FIG. 5 the lowest hot air temperature for achieving complete heat-sealing of the coating layer to the uncoated top side of the fibrous board sustrate was determined. From an addition of 2 weight-% on blended terpene phenolic resin progressively improved the heat-sealability of polylactide as demonstrated by the decreasing sealing temperature required.

(30) FIGS. 6-9 show as examples four structural embodiments of the packaging material according to the invention. There are extruded or coextruded monolayer or multilayer coatings of a blend of polylactide and a terpene phenolic resin (PLA blend) and mere polylactide (PLA) on one side or on both sides of a fibrous paper or board base (board). The share of the terpene phenolic resin in the blend may vary from 2 to 20 weight-%. The base may be paper, paperboard or cardboard of a weight of 40 to 350 g/m.sup.2, preferably a cupboard or a liquid package board of 170 to 350 g/m.sup.2.

(31) More particularly, FIG. 6 shows the base 1 with a single extruded coating layer 2 of the PLA blend. The weight of this monolayer 2 may be from 10 to 30 g/m.sup.2. In FIG. 7 there is such a PLA blend layer 2 on both sides of the base 1. FIG. 8 shows a coextruded multilayer coating with an innermost PLA blend layer 2, a middle layer of PLA 3, and an outermost PLA blend layer 2. The weight of each of the three layers 2, 3 and 2 may be from 4 to 13 g/m.sup.2. The total weight of the multilayer coating is thus 12-39 g/m.sup.2. PLA is the cheaper polymer material in the blend, and including a middle layer 3 of PLA serves to add to the total thickness of the coating while reducing its cost. FIG. 9 shows similar multilayer coatings on both sides of the base 1.

(32) If the packaging material has extruded polymer coatings on both sides, the coatings on the opposite sides need not be identical. There may be a monolayer coating on one side and a multilayer coating on the other side of the fibrous base. It is also possible to include in multilayer coatings layers of other biodegradable polymers suitable for extrusion coating, preferably in blends with polylactide. Examples of such other polymers are PBAT (polybutylene adipate terephtalate), PBSA (polybutylene succinate adipate), PBS (polybutylene succinate), PHA (polyhydroxy alkanoate), PHB (polyhydroxy butyrate), PHBV (polyhydroxybutyrate hydroxyvalerate), PGA (polyglycolic acid), PEG (polyethylene glycol), PCL (polycaprolactane), and starch based biopolymers. The innermost and/or the outermost layer of the multilayer structure shall be of the blend of PLA and the terpene phenolic resin, however.