Smooth profiled food service articles

TECHNICAL FIELD

The present invention relates generally to disposable food service articles such as plates, trays and the like and in preferred embodiments to food serving plates and plates formed from high modulus, mineral-filled polyolefin sheet and most preferably mineral-filled polypropylene.

BACKGROUND

Disposable articles are commonly formed with a curled lip to impart strength to a cup, canister, or carton for example, as is seen in U.S. Pat. No. 5,184,995 to Kuchenbecker. The curl tends to give the article a utilitarian look and feel, not necessarily optimally aesthetically pleasing; especially for disposable articles which can be re-used on multiple occasions such as plastic articles.

There is shown in the U.S. Pat. No. 4,578,296 of Miyazaki et al. a thermoformed article manufactured from filled polyolefin sheet. The polyolefin resin composition includes from 30 to 80 percent of resin, from 19 to 69 percent by weight talc and from 1 to 10 percent by weight titanium dioxide. An article formed from the sheet typically includes a curled lip or a severely downwardly projecting outer lip. Note column 9, line 49 through column 10, line 38.

In accordance with the present invention, there are provided disposable service articles without a curled or severely downturned flange, which features are undesirable in terms of aesthetic qualities and brittleness.

SUMMARY OF THE INVENTION

The invention is described below with reference to the attached figures which show preferred shapes and dimensions.

The plates of the present invention include in a preferred embodiment a plastic plate with a four-radius profile which balances the need for increased rigidity (strength) and rim stiffness (sturdiness) per given material weight/cost. The ergonomic rim profile provides for ease of holding and carrying, consumer friendly shape denoting Permanentware qualities, without the negative side effect of brittleness encountered when using high modulus/stiffness construction materials. The four-radius disposable plastic plate design has a curvilinear rim surface onto which patterning can be applied for visual, tactile and strength purposes. The plate design is strong but not brittle during use even with the high modulus/stiffness mica filled polypropylene (PP) plastic material.

Plates produced with other shapes were rigid but often failed by brittle cracking in the flange and downturn areas. The stresses generated in the flange and downturn areas by deflection of the product during use apparently exceeded the highly filled material strength resulting in failure. It is possible that imperfections on the product's trimmed edge may contribute to brittle cracking by providing failure initiation points for the notch sensitive, highly filled materials preferably used in accordance with the invention.

It was discovered that plastic plates described in this invention disclosure still had exceptional strength per material weight, but also significantly reduced brittle cracking with the highly filled nonhomogeneous materials. The four-radius design, for example, would not build up the high stress levels during deflection even with trimmed edge may imperfections and was less prone to brittle cracking.

Plates having a circular configuration as illustrated employ the four-radius plastic plate design. The plastic articles of manufacture may also be square or rectangular in shape having angular corners, such as found in a tray. Further, additional plastic shapes such as triangular, multi-sided, polyhexal, etc. are contemplated including compartmented trays and oval platters.

It will be appreciated that a salient feature of the inventive articles is the smooth profile as described herein. In general, the transitions between the center, sidewall and flange of the plate are kept free of sharp bends or curves so that mechanical stresses are not concentrated beyond the ability of the material to withstand them. In addition to being operative to avoid undesirable stress regions, the profile is flowing in appearance and provides a pleasing, ergonomic hand feel.

In general, the invention is directed to disposable food contact articles formed of a polyolefin, mineral-filled sheet and have a characteristic diameter as well as a substantially planar central portion, a sidewall portion and a flange portion. For a circular article such as a plate, the characteristic diameter is simply the diameter of the plate as the term is ordinarily employed, i.e., the distance through the center between opposing outer edges of the flange. For non-circular articles, the characteristic diameter is the average distance through the center between opposing outer edges of the flange of the article. Thus, for a rectangular article the characteristic diameter is the average of the shorter side and the longer side, for an oval article the characteristic diameter is the average of the minor axis length and major axis length of the oval and so forth.

The inventive articles are characterized by a smooth profile wherein direction changes are accomplished by way of a plurality of arcuate portions, each of which has a radius of curvature. A particularly preferred embodiment is a four radius plate as described herein, characterized in that the ratio of the length of each radius of curvature to the diameter is at least about 0.02. A ratio of at least about 0.03 is preferred with a ratio of at least about 0.035 being still more preferred. Various details will become more understood by reference to the drawings and detailed description which follows.

BRIEF DESCRIPTION OF DRAWINGS

The invention is described in detail below with reference to the various drawings. In the drawings:

FIG. 1

is a view in perspective of a plate constructed in accordance with the present invention;

FIG. 2

is a view in cross-section and elevation of the plate of

FIG. 1

illustrating the profile of the plate; and

FIG. 3

is a schematic diagram illustrating the profile of the plate of FIGS.

1

and

2

.

DETAILED DESCRIPTION

The invention is described in detail below with reference to the figures. Such description is for purposes of illustration only and is not limitative of the invention in any way.

Illustrated in

FIGS. 1 through 3

, there is a plate

180

which includes a planar center

182

which, in turn, includes an outer peripheral surface

184

. This center region

182

may have a slight convex crown to improve plate stability during use. The planar center

182

forms a bottom for the plate

180

. An outwardly projecting sidewall

186

includes a first rim portion

188

which is joined to the outer peripheral surface

184

of the planar center

182

. A second rim portion

190

is joined to the first rim portion

188

. The first rim portion

188

and the second rim portion

190

form the outwardly projecting sidewall

186

which forms the sidewall of the plate

180

. A rim

192

includes a third rim portion

194

which is joined to the second rim portion

190

of the outwardly projecting sidewall

186

. A fourth rim portion

196

is joined to the third rim portion

194

. The fourth rim portion

196

forms the outer edge of the plate

180

.

FIG. 3

illustrates a partial cross-sectional view of a plate, diameter D, according to the present invention. The plate

180

defines a center line

204

. A base or bottom-forming portion

200

extends from the center line

204

to an outer peripheral surface

202

.

From the center line

204

a predetermined distance X

12

extends toward the outer peripheral surface forming portion

202

. A distance Y

12

extends a predetermined distance from the base or bottom-forming portion

200

upwardly therefrom. A radius R

12

extends from the intersection point of the distance X

12

and Y

12

to form a first rim portion

206

of the outwardly projecting sidewall

205

. The first rim portion

206

is defined by an arc A

12

which extends from a substantially vertical line defined at the outer peripheral surface

202

to a fixed point

210

. The arc A

12

may be approximately 60°.

A distance X

22

extends from the center line

204

to a predetermined point. A distance Y

22

extends from the base or bottom-forming portion

200

of the plate

180

downwardly a predetermined distance. A radius R

22

extends from the intersection of the lines X

22

and Y

22

to form a second rim portion

208

of the sidewall

205

. The radius R

22

extends from the first fixed point

210

to the second fixed point

212

through an arc A

22

. The arc A

22

may be approximately 4°.

A distance X

32

extends from the center line

204

to a predetermined distance. A distance Y

32

extends from the base or bottom-forming section

200

of the plate

180

to project upwardly a predetermined distance. A radius R

32

extends from the intersection of the lines X

32

and Y

32

to form the third rim portion

214

of the rim

216

. The radius R

32

extends from the second fixed point

212

to a third fixed point

218

. An arc A

32

is formed between the second fixed point

212

and the third fixed point

218

to extend a predetermined distance. The arc A

32

may be approximately 55°.

A distance X

42

extends a predetermined distance from the center line

204

. Similarly, a distance Y

42

extends from the base or bottom-forming section

200

of the plate

180

to project upwardly. A radius R

42

extends from the intersection of the lines X

42

and Y

42

to form a fourth rim portion

217

of the rim

216

. An arc A

42

is formed between the third fixed point

218

and a fourth fixed point

220

at diameter D from the center line. The arc A

42

may be approximately 60°. A section

220

forms the outer edge of the plate.

The article made according to the present invention may have any particular size as desired by the user so long as the relative profile dimensions are maintained. More specifically, square or rectangular with rounded corners, triangular, multi-sided, polyhexyl and similar shapes may be made having the profile described above, including compartmented trays and plates. In various embodiments of the present invention the container may be a 9-inch or 11-inch plate with profile coordinates as illustrated in

FIGS. 1 through 3

having the dimensions, angles, or relative dimensions enumerated in Tables 1 through 3.

TABLE 1

Dimensions and Angles For 9″ Plate

DIMENSION and ANGLES

VALUE (inches or degrees)

R12

0.537

X12

3.156

Y12

0.537

R22

2.057

X22

5.402

Y22

0.760

R32

0.564

X32

4.167

Y32

0.079

R42

0.385

X42

4.167

Y42

0.258

A12

60.00°

A22

4.19°

A32

55.81°

A42

60.00°

D

9.00

BOTTOM CONVEX CROWN

0.06

TABLE 2

Dimensions and Angles For 11′ PLATE

DIMENSION/ANGLES

VALUE (inches or degrees)

R12

0.656

X12

3.857

Y12

0.656

R22

2.514

X22

6.602

Y22

0.929

R32

0.689

X32

5.093

Y32

0.097

R42

0.470

X42

5.093

Y42

0.315

A12

60.00°

A22

4.19°

A32

55.81°

A42

60.00°

D

11.00

BOTTOM CONVEX CROWN

0.06

TABLE 3

Dimensions For 9 and 11 INCH PLATE

DIMENSION

RATIO OR

VALUES (Dimensionless or degrees)

ANGLE

PREFERRED

MINIMUM

MAXIMUM

R12/D

0.060

0.045

0.075

X12/D

0.351

0.280

0.420

Y12/D

0.060

0.045

0.075

R22/D

0.228

0.180

0.275

X22/D

0.600

0.480

0.720

Y22/D

0.084

0.065

0.100

R32/D

0.063

0.050

0.075

X32/D

0.463

0.370

0.555

Y32/D

0.009

0.007

0.011

R42/D

0.043

0.034

0.052

X42/D

0.463

0.370

0.555

Y42/D

0.029

0.023

0.035

A12

60.00°

55.00°

75.00°

A22

4.19°

1.00°

10.00°

A32

55.81°

45.00°

75.00°

A42

60.00°

45.00°

75.00°

Salient features of the plate illustrated in

FIGS. 1 through 3

generally include a substantially planar center portion (which may be crowned as noted above and illustrated throughout the various figures) with four adjacent rim portions extending outwardly therefrom, each rim portion defining a radius of curvature as set forth above and further noted below. The first rim portion extends outwardly from the planar center portion and is convex upwardly as shown. There is defined by the plate a first arc A

12

with a first radius of curvature R

12

wherein the arc has a length S

1

. A second rim portion is joined to the first rim portion and is downwardly convex, subtending a second arc A

22

, with a radius of curvature R

22

and a length S

2

. A third, downwardly convex, rim portion is joined to the second rim portion and subtends an arc A

32

. There is defined a third radius of curvature R

32

and a third arc length S

3

. A tangent to the third arc at the upper portion thereof is substantially parallel to the planer center portion as shown in

FIG. 20. A

fourth rim portion is joined to the third rim portion, which is also downwardly convex. The fourth rim portion subtends a fourth arc A

42

with a length S

4

, with a radius of curvature R

42

.

The length of the second arc, S

2

is generally less the length of the fourth arc S

4

, which, in turn, is less than the length S

1

of the first arc A

12

. The radius of curvature R

42

of the fourth arc is less than the radius of curvature R

32

of the third rim portion, which in turn, is less than radius of curvature R

22

of the second rim portion. The angle of the first arc, A

12

is generally greater that about 55 degrees, while, the angle of the third arc, A

32

is generally greater than about 45 degrees as is set forth in the foregoing tables. The angle of the fourth arc A

42

is generally less than about 75 degrees and more preferably is about 60 degrees.

Typically, the length S

1

of arc A

12

is equivalent to the length S

3

of arc A

32

and R

12

of the first rim portion is equivalent in length to the radius of curvature R

32

of the third rim portion.

Generally speaking, the height of the center of curvature of the first arc (that is the origin of ray R

12

) above the central planar portion is substantially less than, perhaps twenty five percent or so less than, the distance that the center of curvature of the second rim portion (the origin of ray R

22

) is below the central planar portion. In other words, the length Y

12

is about 0.75 times or less the length Y

22

.

So also, the horizontal displacement of the center of curvature of the second rim portion from the center of curvature of the first rim portion is at least about twice the length of the first radius of curvature R

12

. The height of the center of curvature of the third rim portion above the central planar portion is generally less than the height of the center of curvature of the fourth rim portion above the plane of the central planar portion. The horizontal displacement of the center of curvature of the second rim portion is generally outwardly disposed from the center of curvature of the third and fourth rim portions.

A further noteworthy feature of the plate of

FIGS. 1 through 3

is that the height of the center of curvature of the third rim portion above the planar central portion is less than about 0.3 times the radius of curvature R

42

of the fourth rim portion; while the height of the center of curvature of the fourth rim portion above the plane of the central portion is at least about 0.4 times the first radius of curvature R

12

. The plates are preferably made from mineral-filled polyolefin sheet such as polyethylene or polypropylene mineral-filled sheet. As will be appreciated from the foregoing data tables as well as from the drawings and discussion above, the ratio of the fourth radius of curvature to the diameter of the plate is preferably at least about 0.03, while the ratio of the third radius of curvature to the diameter of the plate is preferably at least about 0.050. The ratio of the second radius of curvature to the diameter of the plate is preferably at least about 0.2 and the ratio of the length of the first radius of curvature to the diameter of the plate is preferably at least about 0.045.

Preferred materials are plastics or filled plastics. Typically, in filled plastics the primary mineral filler is mica, talc, kaolin, bentonite, wollastonite, milled glass fiber, glass beads (solid or hollow), silica, or silicon carbide whiskers or mixtures thereof. We have discovered that when polypropylene is melt-compounded with acidic-type minerals the resulting mixture has a higher odor index (offensive odors) that would disqualify them from use in food service products. Acidic type fillers such as mica; natural clay minerals such as kaolinite, bentonite, attapulgite, montmorillonite, clarite, or fuller's earth; and silica are particularly detrimental in generating odor compounds when processed under high shear and high temperature conditions experienced during twin screw compounding. We have found that changing the compounding process and adding a basic or other odor supressing compound or component to the primary acidic filler allows the production of low odor index compounds. The reason for this effect is unknown since the fundamental cause of the degradation in polypropylene may be due, in part, to catalysis effects caused by impurities in the mineral as well as its acidic or basic nature. In this regard, the addition of CaCO

3

to talc is beneficial whereas, it may be unnecessary when wollastonite is used as the primary filler.

The preferred primary fillers are mica, talc, kaolin, bentonite, milled glass fibers, and wollastonite or mixtures thereof. Of these, milled glass fibers and wollastonite are basic in nature and may not necessarily require the addition of a secondary basic component. An odor suppressing compound is also preferably included. As noted above, suitable mineral fillers include mica, talc, kaolin, bentonite, wollastonite, milled glass fiber, glass beads (hollow or solid), silica whiskers, silicon carbide whiskers and mixtures thereof as well as the mineral fillers recited herein, whereas the basic organic or inorganic compound is generally the reaction product of an alkali metal or alkaline earth element with carbonates, phosphates, carboxylic acids as well as alkali metal and alkaline earth element oxides, hydroxides, or silicates and basic metal oxides including mixtures of silicon dioxide with one or more of the following oxides: magnesium oxide, calcium oxide, barium oxide, and mixtures of the foregoing. More specifically, the basic organic or inorganic compound may be selected from the group consisting of: calcium carbonate, sodium carbonate, potassium carbonate, barium carbonate, aluminum oxide, sodium silicate, sodium borosilicate, magnesium oxide, strontium oxide, barium oxide, zeolites, sodium citrate, potassium citrate, calcium stearate, potassium stearate, sodium phosphate, potassium phosphate, magnesium phosphate, mixtures of silicon dioxide with one or more of the following oxides: magnesium oxide, calcium oxide, barium oxide, and mixtures of one or more of the above. Furthermore, hydroxides of the metals and alkaline earth elements recited above may be utilized.

Where a basic inorganic odor suppressing compound is chosen, generally such compound is selected from the group consisting of calcium carbonate, sodium carbonate, potassium carbonate, barium carbonate, aluminum oxide, sodium silicate, sodium borosilicate, magnesium oxide, strontium oxide, barium oxide, zeolites, sodium phosphate, potassium phosphate, magnesium phosphate, mixtures of silicon dioxide with one or more of the following oxides: magnesium oxide, calcium oxide, barium oxide, and mixtures of one or more of the basic inorganic compounds set forth above. The amount of a basic inorganic compound is generally from about 2 to 20 weight percent, but is usually from about 5 to about 15 weight percent of the article. Most preferably the basic inorganic compound selected is calcium carbonate; typically present from about 5 to about 20 weight percent.

Where an organic compound is chosen, it is typically selected from the group consisting of sodium stearate, calcium stearate, potassium stearate, sodium citrate, potassium citrate, and mixtures of these where the amount of such compound is from about 0.5 to about 2.5 weight percent of the article. Typically, microwaveable articles produced in accordance with the present invention exhibit an odor index of less than about 0.75; preferably less than about 0.6; with a practical lower limit being 0.1 or so.

As shown below in connection with microwaveability testing, and summarized in Table 11, competing commercial polystyrene type plates cannot withstand the high temperatures generated in the microwave oven during food contact and either significantly warp or deform when the aforementioned food products were heated on them. Under the usual microwaving conditions with high grease content foods, the prior art plates tend to deform and flow to the point where parts of the plate become adhered to the inside of the microwave oven. For disposable plates and containers, having suitable food contact olfactory properties, appearance and feel are important attributes. Another significant property of the containers and plates of this invention is their cut resistance. These rigid articles of manufacture are of sufficient toughness to be resistant to cutting by serrated polystyrene flatware. In normal usage they are also resistant to cutting by regular metal flatware.

Whereas any microwaveable article may be produced in accordance with the invention, most typically the article is a bowl or a plate suitable for serving food at a meal. Preferred articles are thermoformed and include a micronodular food contact surface. Micronodular food contact surfaces are produced by thermoforming a sheet into the article which has been extruded optionally with at least one matte roll and by vacuum thermoforming the sheet by applying vacuum opposite to the surface where the micronodular surface is desired. Most typically the micronodular surface will have a surface gloss of less than about 35 at 75° as measured by TAPPI method T-480OM 92. Articles also will typically have a Parker Roughness Value of at least about 12 microns.

While any suitable polypropylene polymer may be used, the polypropylene polymers are preferably selected from the group consisting of isotactic polypropylene, and copolymers of propylene and ethylene wherein the ethylene moiety is less than about 10% of the units making up the polymer, and mixtures thereof. Generally, such polymers have a melt flow index from about 0.3 to about 4, but most preferably the polymer is isotactic polypropylene with a melt-flow index of about 1.5. In particularly preferred embodiments, the melt-compounded composition from which the resultant extruded sheet is formed into articles further includes a polyethylene component and titanium dioxide. The polyethylene component may be any suitable polyethylene such as HDPE, LDPE, MDPE, LLDPE or mixtures thereof.

The various polyethylene polymers referred to herein are described at length in the

Encyclopedia of Polymer Science

&

Engineering

(2d Ed.), Vol. 6; pp: 383-522, Wiley 1986; the disclosure of which is incorporated herein by reference. HDPE refers to high density polyethylene which is substantially linear and has a density of generally greater that 0.94 up to about 0.97 g/cc. LDPE refers to low density polyethylene which is characterized by relatively long chain branching and a density of about 0.912 to about 0.925 g/cc. LLDPE or linear low density polyethylene is characterized by short chain branching and a density of from about 0.92 to about 0.94 g/cc. Finally, intermediate density polyethylene (MDPE) is characterized by relatively low branching and a density of from about 0.925 to about 0.94 g/cc. Unless otherwise indicated these terms have the above meaning throughout the description which follows.

The microwaveable articles according to the invention typically exhibit melting points from about 250 to about 330° F. and include mica or other primary fillers in amounts from about 20 to about 35 weight percent. Most preferably mica is present at about 30 weight percent, and calcium carbonate is present from about 8 to about 12 weight percent.

It has been found that C8 and C9 organic ketones correlate well with or are associated with undesirable odors in polypropylene/mica compositions. Accordingly, it is preferred that articles in accordance with the invention are substantially free from volatile C8 and C9 organic ketones. In order to avoid undesirable odors, articles in accordance with the invention are preferably prepared from a melt-compounded polyolefin mica composition which is prepared at a process melt temperature of less than about 425° F.; with below about 400° F. being even more preferred. Optionally, the melt processed polyolefin/mineral composition is melt-compounded in a nitrogen atmosphere.

In another aspect of the invention, there is provided a thermoformed, mineral-filled polypropylene food contact article formed from a melt-compounded composition comprising from about 40 to about 90 percent by weight of a polypropylene polymer, from about 10 to about 50 percent by weight of a primary mineral filler and an effective odor-reducing amount of a basic organic or inorganic compound operative to impart an odor index of less than about 0.75 to said melt-compounded composition.

Preferably the inventive articles are prepared from a melt-compounded polyolefin/mica composition prepared by way of a low temperature compounding process.

A preferred low temperature compounding process used for producing mineral-filled polypropylene melt-compounded compositions with an odor index of less than about 0.75 including a basic odor suppressing agent in accordance with the invention with from about 40 to about 90 percent by weight of a polypropylene polymer includes the sequential steps of: (a) preheating a polypropylene polymer while maintaining the polymer below a maximum temperature of about 370° F. and preferably below 350° F. and more preferably below a maximum of about 260° F.; but suitably above about 240° F; followed by; (b) admixing mineral filler to said preheated polymer in an amount from about 10 to about 50 percent weight based on the combined weight of the resin and primary filler and maintaining the mixture below about 425° F.; followed by, (c) extruding the mixture. Polymer may be melted exclusively through the application of shear, or the shear may be supplemented through heating by infrared radiation or ordinary heating coils or performed externally to the mixing chamber. Preferably, the basic odor suppressing agent is added simultaneously with the mineral filler. It is desirable to keep the duration of the step of admixing mineral filler and a basic odor suppressant agent to the mixture relatively short so as not to generate compounds which cause odor and to preserve the particle size and aspect ratio of the mineral filler. Accordingly, the step of admixing the mineral filler should be no more than about five minutes with the duration of the admixing step of less than about three minutes being even more preferred. Any suitable means may be used to carry out the sequential process in accordance with the invention, however, the process is normally carried out in a batch mode in a mixing chamber provided with a pair of rotating rotors in an apparatus referred to in the industry as a Banbury type mixer. One may choose to use a twin screw extruder or a Buss kneader to practice the inventive process if so desired, provided that appropriate elements are used to minimize shear heating.

Thermoforming is typically conducted at a sheet temperature of from about 260° to about 310° F., and more preferably at a temperature of from about 280° to about 300° F.

There is provided in a still further aspect of the invention a crack-resistant, thermoformed food contact article having a wall thickness ranging from about 10 to about 80 mils consisting essentially of from about 40 to about 90 weight percent of a polypropylene polymer, from about 10 to about 50 percent by weight of a mineral filler, from about 1 to about 15 percent by weight polyethylene, from about 0.1 to about 5 weight percent titanium dioxide and optionally including a basic organic or inorganic compound. The basic compound is, generally speaking, the reaction product of an alkali metal or alkaline earth element with carbonates, phosphates, carboxylic acids as well as alkali metal and alkaline earth element oxides, hydroxides, or silicates and basic metal oxides, including mixtures of silicon dioxide with one or more of the following oxides: magnesium oxide, calcium oxide, barium oxide, and mixtures thereof. A particularly preferred article is where the basic organic or inorganic compound is calcium carbonate which is present in an amount of from about 5 to about 20 weight percent.

Polyethylene is more typically present from about 2.5 to about 15 weight percent, preferably from about 4 to about 5 weight percent of the crack resistant article. Titanium dioxide is included in various amounts, from about 0.1 to about 3 percent by weight being typical; from about 0.25 to 2 percent titanium dioxide may be included. Preferably, titanium dioxide is included in at least 0.5 percent by weight

The caliper, or wall thickness, of the articles is usually from about 0.010 to about 0.050 inches or from about 10 mils to 50 mils. A caliper of from about 15 to 25 mils is most typically employed.

While any suitable polypropylene polymer may be employed, the most preferred polymer is isotactic polypropylene having a melt index in the range of from about 0.3 to 4, with a melt index of about 1.5 being typical. The polyethylene employed may be HDPE, LLDPE, LDPE or MDPE, mixtures thereof or a polyethylene with bimodal molecular weight distribution. Polypropylene is sometimes referred to hereafter as “PP”.

The inventive compositions from which the crack resistant articles are made do not include coupling agents such as maleic anhydride containing polypropylene as further described herein, but may optionally include other components which do not alter the basic and novel characteristics of the crack-resistant plates. For example, nucleants such as sodium benzoate in amounts detrimental to crack resistance are to be avoided.

In a still further aspect of the invention there is provided a method of making a microwaveable mineral-filled polypropylene food contact article comprising preparing a melt-compounded composition comprising from about 40 to about 90 percent by weight of a polypropylene polymer and from about 10 to about 50 percent by weight of a mineral filler and optionally an effective amount of an odor-reducing compound. The melt-compounded composition exhibits a relative aroma index, relative to a corresponding composition consisting essentially of polypropylene and mica of less than about 0.75. The composition is extruded into a sheet and formed into a suitable food contact article. Preferably, the article consists essentially of polymer and mineral filler and excludes such components as excess anti-oxidants and the like.

Suitably the basic inorganic or organic compounds are selected from the group consisting of calcium carbonate, sodium carbonate, potassium carbonate, barium carbonate, aluminum oxide, sodium silicate, sodium borosilicate, magnesium oxide, strontium oxide, barium oxide, zeolites, sodium phosphate, potassium phosphate, magnesium phosphate, mixtures of silicon dioxide with one or more of the following oxides: magnesium oxide, calcium oxide, barium oxide, and mixtures of these or other basic inorganic or organic compounds such as sodium stearate, calcium stearate, potassium stearate, sodium citrate, potassium citrate, and mixtures of these basic organic compounds.

The function of the basic inorganic compound or organic compound is to minimize the formation of odor-causing compounds in the mineral-filled polyolefin composition and thus provide products with food contact compatible olfactory properties for consumer use. In this connection, the amount of the basic inorganic compound or organic compound added is controlled to be sufficient to reduce formation of decomposition products to sufficiently low levels to provide containers and plates with suitable food contact compatible olfactory properties. Suitably 5 to 15 weight percent of the container comprises the basic inorganic compound, advantageously about 8 to 12 percent When the basic organic compounds are used, lower quantities are required, suitably from about 0.5 to 2.5 weight percent, advantageously 1.0 to 1.5 percent. Coupling agents and pigments may be utilized. Maleic anhydride and acrylic modified polypropylenes are suitable coupling agents for some embodiments.

Advantageously, the sheet is formed by an extrusion process utilizing a compounded polymer/mica basic inorganic compound or basic organic compound mixtures. The final extrusion process renders a sheet with excellent thermal properties, cut resistance, and food contact compatible olfactory properties.

Mica is easily cleaved into thin, relatively regular, flexible yet strong sheets (leaf-like flakes) with thickness in the range of half a micron and aspect ratio as high as 300. Mica is much softer than other inorganic fillers (wollastonite, glass) yet only slightly harder than talc. Mica has a slippery tactile feel and low abrasiveness relative to other common inorganic fillers.

The reinforcement effect at 40 weight percent mica is equivalent to that of 30 weight percent glass fiber. Hard inorganic fibrous fillers such as glass (various lengths) and wollastonite (acicular structures) have drawbacks in some respects such as abrasiveness and are prone to fracture degradation during conventional melt processing. Other fibrous (organic) fillers are derived from wood and vegetable sources and are not suitable for use in the manufacture of the containers of this invention since the organic fillers, when used in substantial amounts, tend to degrade during processing and they are also moisture sensitive.

In some applications it may be preferred to treat the mineral and/or basic inorganic compounds prior to using them in the inventive articles. A suitable compound for this treatment is amino-silane; sometimes referred to as a “coupling” agent

Suitable basic inorganic and organic compounds used in the process include: calcium carbonate, sodium carbonate, sodium hydroxide, potassium carbonate, barium carbonate, aluminum oxide, sodium silicate, sodium borosilicate, magnesium oxide, strontium oxide, barium oxide, zeolites, sodium phosphate, potassium phosphate, magnesium phosphate, mixtures of silicon dioxide with one or more of the following oxides: magnesium oxide, calcium oxide, barium oxide, and mixtures of these or other basic inorganic or organic compounds such as sodium stearate, calcium stearate, potassium stearate, sodium citrate, potassium citrate, and mixtures of these basic compounds.

In the case where microwaveability is desired for a plastic disposable food contact article, the not so perfect solution has been the use of relatively expensive high heat modified polystyrene based or heat resistant materials (e.g., unfilled PPO and SMA engineering resins), where PPO refers to polyphenylene oxide and SMA refers to styrene-maleic anhydride copolymer.

Mica or another mineral filler and the basic inorganic compound or the basic organic compound filled polypropylene is compounded by pre-blending the polypropylene in pellet or flake form with mica powder and the basic inorganic compound or the basic organic compound powder and other additives (color concentrates, pigments, antioxidants, lubricants, nucleating agents, antistatic agents, etc.). This mixture is conveyed into the feed section addition point of a twin screw compounding extruder, or compounded in a Banbury-type mixer to provide a melt-processed polyolefin composition. Alternatively, the components are advantageously fed separately into the same or different points of addition, using combinations of volumetric and/or gravimetric (i.e., loss in weight type) feeders as further described herein.

For white pigmentation, titanium dioxide is preferred due to combination of brightness, and opacity, as well as stability during processing and final use. Surface treatment may be optionally used to further enhance wetting, dispersion, compatibility with matrix resins whereas the titanium dioxide forms may be of the rutile or anatase type. Alternate white pigments may also consist of calcined clay or blends of calcined clay with titanium dioxide. For black pigmentation, carbon black is preferred due to a combination of desirable characteristics such as blackness, and dispersibility, the latter of which can be carefully controlled by choice of particle size and surface chemistry. Carbon black is amorphous carbon in finely divided form which is made by either the incomplete combustion of natural gas (channel black) or by reduction of liquid hydrocarbons in refractory chambers (furnace black).

A twin screw extruder provides sufficient mixing action to effectively cause the wetting and dispersion of the filler into the polymer matrix. The twin screw extruder may be of the co-rotating or counter-rotating type, where each type is equipped with different screw flight elements which are appropriate for the feed, mixing, and melt metering zones. The discharge zone normally consists of a strand die where the exiting molten material strands are quenched in a circulating water bath followed by knife cutting into pellets. In a particularly preferred embodiment, a Banbury-type mixer is used for compounding the resin, mica and basic compound as further described herein.

Low molecular weight additives such as waxes, fluorinated polymers, and other specialty lubricants are suitably used as process aids to reduce the melt viscosity and improve throughput Polyethylene resin may also be added to the blend. Other additives may include nucleating agents and antistatic agents. Antioxidants may be added in small amounts, generally less than one weight percent, to minimize shear and thermal degradation of the polypropylene during the extrusion and forming processes as well as to promote the chemical stability of the sheet prior to and during final article use. Suitable antioxidants are advantageously selected from the group of phenolics and phosphites and blends thereof. These are produced by Ciba-Geigy and General Electric Corporation. Plastic sheet extrusion equipment is suitable for the manufacture of multilayered or single layered mica or other mineral filler and the basic inorganic or organic compound filled sheets of a polyolefin selected from the group consisting of polypropylene, polypropylene/polyethylene copolymer or blend, and mixtures of these. Melt strength of the sheets is improved when mica is used as a filler since geometry of the mineral in the form of high aspect ratio flakes serves to provide “inter-particle connectivity” or physical cross-linking. The food contact compatible olfactory properties are enhanced when in addition to the mica, basic inorganic compounds or organic compounds such as calcium carbonate, sodium carbonate, potassium carbonate, barium carbonate, aluminum oxide, sodium silicate, sodium borosilicate, magnesium oxide, strontium oxide, barium oxide, zeolites, sodium phosphate, potassium phosphate, magnesium phosphate, mixtures of silicon dioxide with one or more of the following oxides: magnesium oxide, calcium oxide, barium oxide, and mixtures of these or other basic inorganic or organic compounds such as sodium stearate, calcium stearate, potassium stearate, sodium citrate, potassium citrate, and mixtures of these are mixed with mica or other mineral filler and the polyolefin to produce the containers of this invention. Exemplary inorganic materials which may also be employed as a primary mineral filler include talc, barium sulfate, calcium sulfate, magnesium sulfate, clays, glass, dolomite, alumina, ceramics, calcium carbide, silica and so on. Many of these materials are enumerated in the

Encyclopedia of Materials Science and Engineering

, Vol. # 3, pp. 1745-1759, MIT Press, Cambridge, Mass. (1986), the disclosure of which is incorporated herein by reference.

Mineral fillers are sometimes referred to by their chemical names. Kaolins, for example, are hydrous alumino silicates, while feldspar is an anhydrous alkali, alumino silicate. Bentonite is usually an aluminum silicate clay and talc is hydrated mangesium silicate. Glass, or fillers based on silicon dioxide may be natural or synthetic silicas. Wollastonite is a calcium metasilicate whereas mica is a potassium alumino silicate. Mineral fillers are further discussed below. As noted above, clays may be employed as a primary filler. The two most common of which are kaolin and bentonite. Kaolin refers generally to minerals including kaolinite which is a hydrated aluminum silicate (Al

2

O

3

.2SiO

2

.2H

2

O) and is the major clay mineral component in the rock kaolin. Kaolin is also a group name for the minerals kaolinite, macrite, dickite and halloysite. Bentonite refers to hydrated sodium, calcium, iron, magnesium, and aluminum silicates known as montmorillonite which are also sometimes referred to as smectites . A large number of siliceous materials may also be employed as a primary filler. These materials include diatomite, perlite, pumice, pyrophillite, silica, and talc. These minerals typically consist of an alkali metal oxide or alkaline earth element oxide , and silicon dioxide together with a minor amount of water and other elements. Talc, for example, includes from about 25% to about 35% MgO, 35-60% SiO

2

and about 5% H

2

O. These materials are further described below. Diatomite or kieselguhr is a sedimentary material formed by centuries of life cycles of aquatic diatoms, a simple plant in the algae family with an opaline silica cell wall. Thousands of species of diatoms have flourished and continue to do so in both marine and lacustrine environments. Fossilized skeletal remains of diatoms in commercial quantities are found in many parts of the world. Perlite is believed to result from hydration of volcanic glass or obsidian. Generally, hydration is about 2-5%; this water content is important to the expansibility of the perlite, influencing melting point and supplying expansion steam.

The rapid expansion of dissolved gases in silica lavas during volcanic eruptions produces the light density pumice or pumicite. The finer pumicite particles are transported by wind away from the source volcano, whereas pumice accumulates closer to the vent

The hydrous aluminum silicate, pyrophilite, is formed by hydrothermal metomorphism of acid tuffs or braccias.

Silica sand is frequently obtained from the weathering of quartz-containing rock. Decomposition and disintegration of the rock with decomposition of other minerals leaves a primary quartz sand that has been concentrated by water movement. Induration of sands to sandstone results in another source for silica sand. Amorphous silica, or more properly cryptocrystalline or microcrystalline silica, is formed by the slow leaching of siliceous limestone or calcareous chert. Talc is formed by the metamorphic (hydrothermal) alteration of magnesium silicates such as serpentine, pyroxene or dolomite.

The siliceous fillers are generally inert in most applications as shown by pH values in the range from about 6-10.

Sulfate minerals, such as gypsum and barite may likewise be employed as a primary filler. Gypsum is the name given to the mineral that consists of hydrous calcium sulfate (CaSO

4

2H

2

O), and also to the sedimentary rock that consist primarily of this mineral. In its pure state, gypsum contains 32.6% lime (CaO), 46.5% sulfur trioxide (SO

3

), and 20.9% water. Single crystals and rock masses that approach this theoretical purity are generally colorless to white, but in practice, the presence of impurities such as clay, dolomite, silica and iron imparts a gray brown, red or pink color to the rock.

There are three common varieties of gypsum: selenite, which occurs as transparent or translucent crystals or plates; satin spar, which occurs as thin veins (typically white) of fibrous gypsum crystals; and alabaster, which is compact, fine-grained gypsum that has a smooth, even-textured appearance. Most deposits or rock gypsum that are suitable for industrial purposes are aggregates of fine to coarse gypsum crystals that have intergrown to produce a thick, massive sedimentary rock unit that is 90-98% gypsum. Alabaster is highly prized because of its uniformly fine particle size, but the more common deposits of rock gypsum consisting of coarser-grained selenite can generally be crushed and ground to produce a suitable filler and coating material.

Gypsum has a hardness of 2 on the Mohs scale, and can be scratched with the fingernail. Large rock masses are easily crushed and ground to a fine powder. The specific gravity of gypsum is about 2.31 and the refractive index is about 1.53. Gypsum is slightly soluble in water but it is an inert substance that resists chemical change. The oil-absorption capacity of gypsum is fairly low (0.17-0.25 cm

3

g

−1

).

Raw or crude gypsum is one of the forms used as fillers and coatings, but for some purposes calcined or deadburned gypsum is desired. In calcining, the gypsum is heated to abut 120-160° C. to drive off free water and partially remove the water of crystallization. The calcined material or stucco, has a chemical composition of CaSO

4

.½H

2

O, and it readily takes up water. Calcination at higher temperatures (500-725° C.) results in a product called deadburned gypsum, which has a composition of CaSO

4

.

Anhydrite, a sulfate mineral and rock that is closely associated with gypsum in nature and has minor uses as a filler, in anhydrous calcium sulfate (CaSO

4

) containing 41.2% CsO and 58.8% SO

3

. It is typically fine grained (like alabaster), and occurs in thick, massive sedimentary rock units. Anhydrite usually is white or bluish gray when pure, but it may be discolored by impurities. Anhydrite has a hardness of 3.5, a specific gravity of 2.98, and a refractive index of 1.57-1.61.

Thus, fillers commonly include:

Barium Salt

Barium Ferrite

Barium Sulfate

Carbon/Coke Power

Calcium Fluoride

Calcium Sulfate

Carbon Black

Calcium Carbonate

Ceramic Powder

Chopped Glass

Clay

Continuous Glass

Glass Bead

Glass Fiber

Glass Fabric

Glass Flake

Glass Mat

Graphite Powder

Glass Sphere

Glass Tape

Milled Glass

Mica

Molybdenum Disulfide

Silica

Short Glass

Talc

Whisker

Glass

Calcium carbonate

Alumina

Beryllium oxide

Magnesium carbonate

Titanium dioxide

Zinc oxide

Zirconia

Hydrated alumina

Antimony oxide

Silica

Silicates

Barium ferrite

Barium sulphate

Molybdenum disulphide

Silicon carbide

Potassium titanate

Clays

Whereas fibrous fillers are commonly:

Whiskers

Glass

Mineral wool

Calcium sulphate

Potassium titanate

Boron

Alumina

Sodium aluminum

Hydroxy carbonate

Suitably the extruded sheet includes coloring agents for aesthetic appeal, preferably titanium dioxide, carbon black, and other opacifying agents in the range of 0.5-8 weight percent based on total composition, preferably 1.5 to 6.5 weight percent. The extruded sheet comprises minor amounts of other additives such as lubricants and antioxidants. These articles of manufacture may be suitably colored with pigments or dyes. Pigments are defined as small insoluble organic or inorganic particles dispersed in the resin medium to promote opacity or translucency. Usual pigments include carbon black, titanium dioxide, zinc oxide, iron oxides, and mixed metal oxides. Dyes are organic and soluble in the plastic, and may be used alone or in combination with pigments to brighten up pigment based colors. All such colorants may be used in a variety of modes which include dry color, conventional color concentrates, liquid color and precolored resin.

Aroma Profile Test Method

The Sensory Analysis Center at Kansas State University has developed a profiling protocol in which a highly trained panel identifies specific odors and rates their intensity. The intensity scale is a 15-point “universal” scale of the type typically chosen for sensory studies, where 1 is barely perceptible or threshold and 15 is extremely strong. If an attribute or odor component is not listed in the tables which follow, it means it is not present and would score a 0. The panel members are selected on the basis of a series of screening tests that include basic taste, odor recognition, taste intensity recognition, taste intensity ranking, and a personal interview to evaluate availability and personality traits. Training, which includes the fundamental sensory principles and all aspects of the profile technique, is done over a 4-12 month period.

The panelists work as a group to arrive at a description of the product. Individual results are compiled by the panel leader and discussion follows in which disagreements are discussed until a consensus is reached on each component of the profile. Reference materials and more than one session usually are required in order to reach the consensus.

The procedure for resin is to place 40 ml. of resin in a 340 ml. glass brandy snifter, which is covered with a watch glass. Sheet samples are cut into two 2″×2″ sections and placed in the same size brandy snifter. In testing, panelists found that some samples had initial odor components that disappeared rapidly. Therefore an initial impact and a sustained impact were evaluated for each sample. The initial impact was judged immediately after the watch glass had been removed; the sustained impact was judged 10 seconds after the watch glass had been removed. Typical results are shown in the Table 4 below for Low Odor and High Odor Compositions. “Low” odor formulations were produced using lower melt processing temperatures in compounding and adding 10% calcium carbonate to the formulation.

TABLE 4

High Odor vs. Low Odor Polypropylene Composites:

Effect of Adding 10% CaCO

3

ODOR PROFILE FOR COMPOUNDED RESIN

Consensus Odor Profile on Resin

Resin Impact

(Kansas State University Sensory Analysis Center)

Resin

Initial

Sustained

Petroleum

Pungent

Musty

Scorched

Medicinal

Sweet

Waxy

Soapy

High

9.0

3.5

8.0

4.0

7.0

3.5

3.0

Odor

Low

5.5

2.5

2.5

4.5

1.5

2.0

4.5

Odor

High Odor Resin

65.63% Polypropylene

30% Mica

2.5% Coupling Agent

1.87% Pigment

Low Odor Resin

55.63% Polypropylene

30% Mica

10% CaCO

3

2.5% Coupling Agent

1.87% Pigment

High Odor and Low Odor compositions were compounded utilizing the process melt temperatures indicated in the first column of Table 5 and formed into sheets as described above. Thermoformed sheet was evaluated for aroma profile.

TABLE 5

ODOR PROFILE FOR SHEET FORMED

FROM COMPOUNDED RESIN AT TWO TEMPERATURES

Sheet Impact

Consensus Odor Profile on Sheet

Resin

Initial

Sustained

Petroleum

Pungent

Musty

Scorched

Medicinal

Sweet

Waxy

Soapy

High Odor

12.0

6.0

10.0

8.0

7.5

4.5

4.0

370° F.

High Odor

11.0

8.0

7.5

7.5

6.0

3.5

2.0

459° F.

Low Odor

5.5

2.0

3.5

4.0

2.0

2.5

2.5

371° F.

Low Odor

5.5

2.0

3.0

3.5

2.0

3.5

460° F.

The foregoing data demonstrates that: when a basic moiety containing compound was added to the mica polyolefin composition, a resin was produced having suitable food contact compatible olfactory properties. Significant decreases in the initial and sustained odors were observed and the scorched, pungent and petroleum aroma components were removed or greatly reduced and these undesirable components seem to be replaced with sweet, waxy, and soapy aroma components.

When compounded pellets are subjected to sheet extrusion, those without calcium carbonate increase in the disagreeable components (pungent and petroleum) and increase in the initial and sustained odor output with subsequent processing. In contrast when pellets contain calcium carbonate, no increase in undesirable aroma components was observed and no increase in the initial or sustained odor was produced with subsequent processing. Test panel data correlated well with analytical techniques as can be seen from the discussion and examples which follow.

C8/C9 Ketones

The precise nature of the odor causing compounds in polypropylene/mica compositions is not known; however, it has been found that undesirable odors correlate well with eight carbon (C8) and nine carbon (C9) alkyl ketones as described hereinafter, and may be associated with such compounds. A Likens-Nickerson steam/methylene chloride extraction technique was used to extract possible odor causing compounds from polypropylene/mica compositions and produce a concentrate. The extraction was performed until complete. The concentrate was analyzed through gas chromatography/mass spectrometry to produce chromatograms. The C8/C7 ratios referred to hereinafter are ratios of the abundance at the peaks assigned to be 4-methyl-2-heptanone to the abundance at the peak assigned to be 4-heptanone as measured by Likens-Nickerson extraction followed by gas chromtography/mass spectrometry.

Generally, “low odor” compositions reduce concentration of C8 and C9 ketones over “high odor” compositions by ⅔ with ⅕ being typical and {fraction (1/10)} being preferred. Thus, in general, melt-compounded compositions in accordance with the invention have extractable concentrations of C8 and C9 alkyl ketones of less than about 3.5 ppm (weight) with less than 2 ppm being typical and less than 1 ppm being particularly preferred. Thus, the C8/C7 ratio can be used as an alternative indicator of desirable olfactory characteristics. Typically, “low odor” compositions in accordance with the invention have a C8/C7 ratio at least five times less than high odor compositions with at least ten times less being typical. In preferred compositions according to the invention, C8/C7 ratios as measured by Likens-Nickerson extraction followed by gas chomatography/mass spectrometry are generally less than about 0.5 or so as is seen from in the examples which follow. C8/C7 ratios of less than about 0.3 are typical and C8/C7 ratios of less than about 0.1 are particularly preferred. The articles of the invention and the pellets from which they are made are further characterized by an odor index which is determined by commercially available equipment in accordance with the procedure detailed below.

Odor Index

Melt processed compositions produced in accordance with the present invention, particularly extruded pellets from which articles such as plates and bowls are made, characteristically exhibit relatively low odor as opposed to conventionally formulated mineral/polypropylene compositions. Generally the odor index (as defined herein) is less than about 0.75, with less than or equal to about 0.6 being preferred. In general, the lower the odor index, the lower the odor intensity of the mineral-filled/polypropylene pellets. Less than or equal to about 0.5 is most preferred with a practical lower limit believed to be somewhere around 0.1 or so. Thus, in accordance with the invention, melt compositions will generally have an odor index of less than about 0.75 and typically from about 0.60 to about 0.1.

The odor index of a particular melt-processed composition is readily determined using conventional materials and equipment

The odor index is defiled as the arithmetic average of all sensor integrals for a given mineral-filled polypropylene sample including both a primary mineral filler and calcium carbonate or other odor suppressing compound divided by the arithmetic average of all integrals for a filled polypropylene sample including a primary mineral filler, but no odor suppressing basic compound, or in equation form:

Odor Index = \frac{\begin{matrix} \begin{matrix} average readings of pellets including a primary mineral \\ filler and calcium carbonate or other odor suppressing \end{matrix} \\ compound \end{matrix}}{\begin{matrix} average readings of pellets including mineral filler only \\ without an odor suppressing basic compound \end{matrix}}

A commercially available “electronic nose” aroma scanning device is used. Typically, such devices utilize a plurality of conductivity sensors to determine the odor of a sample. The particular device used in the discussion which follows uses 32 sensors whose response is integrated over time. The various integrals are averaged for each sample and the single value is used in the numerator and the denominator of the above equation.

A sample of the present invention is described in Table 6 and following.

TABLE 6

Index Numerator Composition

Amount (Wt.

Component

Manufacturer

Product Number

Percent)

Polypropylene

Exxon

Escorene 4772

55.63

Mica

Franklin

L-140

30.0

Industrial

Minerals, Inc.

Calcium

Huber

Q-325

10.0

Carbonate

Coupling Agent

Aristech

Unite NP-620

2.5

Titanium

Tioxide

TR-23

1.87

Dioxide

The above components were extruded on a 90 mm Berstorff Co-Rotating Twin Screw Extruder with underwater pelletizing under the following conditions:

200 rpm screw speed with the following set temperature profile:

Zone 1—510° F.

Zone 2—485° F.

Zone 3—400° F.

Zone 4—380° F.

Zone 5—380° F.

Zone 6—380° F.

Head Flange—425° F.

Screen Changer—425° F.

Die—440° F.

Throughput appx. 900 LB/HR

to produce pellets, the odor values of which are used in the numerator of the above equation.

The preferred instrument to perform the aroma intensity measurements is an AromaScan® model A32 (AromaScan, Hollis, N.H., USA). This instrument employs a dynamic head space type of measurement, in which nitrogen gas flows through a sample vial and carries aroma volatiles to the sensors. All pellet samples are analyzed in triplicate with the final results averaged to minimize measurement noise. In the illustrations which follow, The “Acquisition Parameters” method of the instrument is set with a sampling interval of 1 and a detection threshold of 0.2. The “Multisampler-SP” method of the instrument sets the platen temperature (100° C. for the examples herein). Two other temperatures (15° C. and 125° C.) are automatically set. The Multisampler-SP method is also used to set the parameters in Table 7 to measure aroma intensity.

TABLE 7

AromaScan ® Settings

Sample Equilibration Time:

5 minutes

Vial Size:

22 ml

Mix Time:

0

Mix Power:

1

Relative Humidity:

10%

Sampling Time:

4 minutes

Wash Time:

5 minutes

Data Collection Time (minutes):

19

Time Between Injections

20

(minutes):

In the recognition window, start and end are set at 1. In addition to the foregoing, the “Vial Pressurization Control” is set at 20 kPa, the “Vial Needle Flow” is set at 50 ml/min nitrogen; “Transfer Line Flow” across the sensors, between, before and after samples is set at 150 ml/min. All gas flows are for dry nitrogen.

A response of each of the 32 sensors of the AromaScan® machine is integrated over a time interval of 55-150 seconds. The initial 55 seconds is allowed to let humidity/moisture exit the system to a great extent before integration is started. The 150 second integration end time was chosen to allow the sensor signals to return to baseline, at which time all significant signal has been integrated. The various signals seen after 150 seconds are insignificant in terms of the odor measurement.

Using the foregoing procedure and composition, 2.0 grams of compounded polymer pellets are weighed and placed in the 22 ml, crimp top, septum capped vials and analyzed automatically by the instrument. A denominator, or reference sample is prepared as described in connection with Tables 7 and 8, except that no calcium carbonate is used; i.e. the sample has 65.63% polypropylene. Through the use of an automated instrument, the odor intensity of the melt-compounded pelletized composition can be reduced to a single value. While the foregoing sets forth a particular and preferred method of determining the odor intensity index, it may also be possible to employ other instruments consistent with this protocol since such instruments are readily available. If such alternative instrument is employed the standard composition detailed above should be used to ensure that calibration is proper. As noted, the reference or denominator composition is prepared by substituting polypropylene for the calcium carbonate (or other basic compound) of the numerator composition.

EXAMPLES 1-9

A series of resin compositions and sheet products were prepared in accordance with the discussion above and characterized by C8/C7 ketone ratio and odor panel testing. Variables included calcium carbonate addition, process atmosphere (air or nitrogen) and process melt temperature. Results appear in Table 8 for examples 1 through 9.

TABLE 8

CaCO

3

Effect of Process Conditions and Compositions on Odor of PP/Mica Composites

Odor Panel Data

Type

“Scorched”

(Banbury or

Process

C

8

/C

7

Sustained

Odor Profile

Extruded

Atmosphere

CaCO

3

Process Melt

Ketone

(Total

Component

Example

Sheet)

(Air/N

2

)

(Yes/No)

Temperature

Ratio

Intensity)

Intensity

1

Brabender

Air

Yes

370° F.

0.055

2.0

0

Banbury

Compounded

2

Brabender

Air

Yes

460° F.

0.6

4.0

5.0

Banbury

Compounded

3

Sheet

N

2

Yes

460° F.

0.3

4

Brabender

Air

Yes

460° F.

0.6

4.0

5.0

Banbury

Compounded

5

Sheet

Air

Yes

370° F.

0.15

2.0

0

6

Sheet

Air

No

370° F.

1.3

6.0

4.5

7

Sheet

Air

Yes

400° F.

—

5.0

2.5

8

Sheet

Air

No

460° F.

0.9

8.0

3.5

9

Sheet

Air

Yes

460° F.

0.7

2.0

0

See discussion above for C8/C7 ketone ratio, odor; Kansas State University Odor Panel Profile. Extruded Sheet was prepared using a single screw extruder with pre-compounded resin made by a twin screw process.

The resins of Examples 1, 2, and 4 were prepared on a Brabender device (C. W. Brabender, model EPL2V5502) with a Banbury mix head (model R.E.E.6, 230v, 11a) with a mixing time of 5-10 minutes.

The sheet samples, Examples 3 and 5 through 9, were prepared from precompounded resin pellets extruded under the conditions shown in Table 9.

TABLE 9

Sheet Extrusion Conditions for PP/Mica Pilot Extruder

CONDITIONS

ACTUAL

SET POINT

Barrel Zone 1 (° F.)

354-378

360-375

Barrel Zone 2 (° F.)

366-410

370-410

Barrel Zone 3 (° F.)

371-460

370-460

Adapter temp (° F.)

359-460

370-460

Feed Block Temp (° F.)

370-468

370-460

Die Zones 1-3 temps

368-462

370-460

(° F.)

Extruder RPM

110

110

Drive Amperes

15-23

—

Melt Pressure (psi)

1050-1850

—

Die Pressure (psi)

745-910

—

Line Speed (FPM)

8.25-9.74

—

Chill roll temp. (° F.)

130

—

The odor of PP/mica composites (pellets or sheet) is affected by temperature, atmosphere, and by the addition of a basic filler such as CaCO

3

. The C8/C7 ketone ratio is consistent with the odor panel data and shows that offensive odor components decrease with:

Using lower processing temperatures

Using a base such as CaCO

3

as a buffering agent

Processing under inert atmosphere such as N

2

.

EXAMPLES 10-13

Particularly preferred, low odor compositions are prepared by way of a sequential process in a Banbury mixer at relatively low temperatures. It has been found that melt compositions prepared in a sequential Banbury process exhibit superior stiffness as measured by flexural modulus properties and low odor. In a sequential process in accordance with the invention, two feed steps are used in order to minimize the time heated or molten polypropylene is in contact with the mica or other mineral filler.

TABLE 10

Comparison of Compounding Processes

Compound

Flexural

Odor Index;

COMPOUNDING

Modulus

9″ Plate

Approximate

PROCESS

(Tangent), PSI

Rigidity (g/0.5″)

(Compound)

Twin Screw

718,000

417

0.625

Example 10

Banbury

591,000

378

0.375

(non-sequential)

Example 11

Banbury

708,000

416

0.41

(sequential,

1 min. pre-heat)

Example 12

Banbury

635,000

352

0.3875

(Sequential, 2 min.

premelt)

Example 13

Table 10 shows compound flexural modulus (as measured by ASTM method D 790-95a), corresponding plate rigidity, and aroma intensity index on four indicated compounding processes designated as Examples 10-13. In the case of twin-screw (Example 10), high modulus is obtained but with higher odor with relatively low throughput, in the range of 900 lb/hr, which is less than half the output of Banbury compounding processes (utilizing a Stewart-Bolling Banbury Mixer with batch sized in the range of 150-200 lb) listed herein. In the case of non-sequential Banbury process, low modulus is obtained with corresponding low plate rigidity with lower odor and high throughput. In the last two cases corresponding to sequential Banbury processes designated as “1 min. pre-heat” and “2 min. pre-melt”, the short 1 minute preheat case (Example 12) is. preferred because it gives high compound modulus and high plate rigidity (comparable to twin screw case) with benefits of both low odor and high throughput, in excess of 2000 lb/hr.

The twin screw formulation in the above table contains PP/30% mica/10% CaCO3 with 2.5% coupling agent (maleic anhydride modified PP grade Aristech Unite NP—620) and no polyethylene. The formulation corresponding to all three listed Banbury processes in above table contain PP/30% mica/10% CaCO3/0.5% Ti02/4%LLDPE with no coupling agent where such ingredients have the following sources and grades: Mica=Franklin Minerals L-140, CaCO

3

=Huber Q325, PP=Exxon Escorene PP4772, LLDPE=Novapol Novachemical G1-2024A.

The Banbury “non-sequential” case (Example 11 in Table 10 corresponds to adding all ingredients together with a total compounding time of about 4.5 minutes followed by conversion of the batch (having temperature of 430° F.) to pellets using a continuous 10″ single screw extruder equipped with one 30 mesh and one 20 mesh screen, and an underwater pelletizing die assembly, with a pelletizing temperature in the range of 455-470° F.

The Banbury “sequential 2 min premelt” case (example 13) in Table 10 corresponds to a 2 minute period for melting the PP/LLDPE mixture (in the presence of CaCO3 and TiO

2

) to a maximum temperature of about 350° F., followed by adding mica and thereafter mixing for a period of about 105 sec to achieve a batch temperature of about 430° F., followed by conversion to pellets with a pelletizing temperature of about 460° F. The Banbury “sequential, 1 min pre-heat” case (Example 12) in Table 10 corresponds to about a 1 minute period for presoftening the PP/PE mixture (in the presence of TiO

2

, or alternatively adding the TiO

2

with the mica and calcium carbonate) to a maximum temperature of about 260° F., followed by adding the mica/CaCO

3

mixture and thereafter mixing to achieve a batch temperature of about 425° F., followed by conversion to pellets with a pelletizing temperature of about 425° F. In this preferred mode, it has been found that polymer preheating aids in preserving compound stiffness (required for rigid articles of manufacture) and intimate contact of mica with odor suppressing agent (CaCO

3

) aids the production of low odor material.

Pellets from the above mentioned Banbury compounding processes were subsequently extruded at 370° F. as cast sheets in the range of 17-18 mil. Sheet line conditions also included a screw RPM value of 100, a chill roll temperature of about 130° F., drive amperage value of about 22, melt pressure of about 2000 psi, die pressure of about 970 psi and a line speed of about 7 ft/min. Plates were subsequently vacuum thermoformed using a female mold and trimmed and tested for rigidity.

Physical Properties, Heat Resistance and Food Contact Suitability

TABLE 11

MICROWAVE COOKING TEST RESULTS FOR

PLATES J AND S

PLATE TYPE

FOODTYPE

J

S

Donut

Pass

Sugar glazing sticks

Broccoli/cheese

Pass

Significantly deforms

Pepperoni pizza

Pass

Moderate

deformation,

Staining

Barbecue pork

Slight stain

Significant

stain/warpage

Pancake/syrup

Pass

Significant warpage

Beans & pork

Pass

Significant warpage

Butter

Slight warpage

Significant warpage

Bacon

Moderate warpage

Significant warpage

Localized melting,

Rubbery plate flows

no leak

and

Sticks to glass tray

Microwaveability

Fort James Corporation (J) plate specimens of this invention and plates manufactured by Solo Cup Company (S) were tested in the microwave (Samsung model MW 8690) with a variety of foods. The highest power setting (10) was used in all cases and cooking/heating times and procedures corresponded to food manufacturer instructions on the packages. Most tested foods were of the frozen microwaveable type and were placed in a semi-thawed state directly on plates prior to cooking. When appropriate, a loose covering of wax paper was employed during the cooking process. After cooking, the plates were gently washed with warm water and inspected. The following are the detailed test results which are also summarized in above Table 11.

Test #1 Results—Sugar Glazed Donut

J. A large, oval shaped sugar glazed plain donut was microwaved on the plate of this invention for 60 seconds. The sugar glazing melted, bubbled, and flowed on the plate. The boiling sugar and grease mixture caused the bottom of the plate to feel very warm but the plate exhibited no warping, no staining, no softening, and no soak-through. The plate was cool enough to be safely handled. The residue of the donut was easily washed off and the appearance of the used plate was excellent

S. The bottom of the plate got hot and slightly deformed with no soak-through, however, sugar stuck to the plate.

Test #2 Results—Broccoli with Cheese Sauce

J Green Giant 10 oz. Broccoli with cheese sauce was removed from the flexible pouch and heated for five minutes in the microwave on the plate with loose covering of wax paper. The cheese melted and bubbled on the plate without sticking. The plate bottom was warm, but no soak-through and no loss of dimensional stability was observed. After washing, no staining was observed and the appearance of the used plate was excellent

S The plate bottom got hot and significantly deformed with no soak-through.

Test #3 Results—Pepperoni Pizza

J Tombstone 7 oz. Pepperoni pizza was cooked on an uncovered plate for 4 minutes. The cheese melted and started bubbling about halfway through the test The molten cheese mingled with the hot liquid fat extruded from the pepperoni and dripped on the sides of the crust onto the plate. No sticking, no soak-through, no staining, and no loss in plate dimensional stability was observed and the appearance of the used plate was excellent

S The plate bottom got hot and moderately deformed with no soak-through. The greasy reddish stain from oil in pepperoni could not be completely washed off.

Test #4 Results—Microwave Kid Meal

Pork Rib Patties Barbecue Sauce, Fries, Honey Corn Bread

J A quick meal preparation simulation test was conducted using a Swanson 7.2 oz. microwave kids' meal with ingredients consisting of partially cooked boneless pork rib patties, barbecue sauce, fries, and honey corn bread. The food was transferred from the compartmented tray onto the plate. Sauce was spooned on top of the pork meat and was allowed to drip on the sides of the patties and onto the plate. The cornbread batter was spooned out and was placed on the plate next to the fries. The food was loosely covered with wax paper and cooked for 3.5 minutes. Examination after microwaving showed that the cornbread was fully cooked and there was no sticking or damage to the plate. The fries and pork meat with sauce caused no soak-through and no loss in plate dimensional stability. Washing of plate revealed the presence of slight staining from barbecue sauce. Overall, the appearance of the used plate was very good.

S The plate bottom deformed mainly from pork meat with considerable staining from the barbecue sauce without soak-through.

Test #5 Results—Beans with Pork and Tomato Sauce

J Beans with pork and tomato sauce (8 oz. Can) were placed on the plate, covered with wax paper and heated for 2 minutes near boiling. The bottom of the plate got hot, but the rim was cool to touch. The hot plate bottom exhibited no bulging and also, when the hot food plate was handled by the rim there was no perceived loss in dimensional stability. No soak-through, no warping and no staining was observed. The appearance of the plate was excellent.

S The plate bottom became very hot and severely deformed with no soak-through and when handled by the rim, the plate felt like it had low rigidity.

Test #6 Results—Pancakes with Syrup and Precooked Bacon

J In this test, Swanson microwave pancakes and bacon breakfast (4.5 oz. size) were used. The semi-thawed meal consisted of thee pancakes and three partially, precooked bacon strips. The pancakes and bacon were removed from the tray in carton and placed on plate. Approximately 5 teaspoons of pancake syrup was spooned over the pancakes and the assembled meal was covered with wax paper and microwaved for 2 minutes. Although the bottom of the plate got hot, the overall plate performance was excellent, i.e. no warpage, no soak-through, no loss in dimensional stability, and no staining. Some hot grease was exuded by the bacon during crisping but there was no observed damage to the plate. The appearance of the used plate was excellent.

The plate bottom became hot and significantly deformed (especially in areas where bacon was placed), but no soak-through was observed and when handled by the rim, the plate felt soft

Test #7—Butter

J Butter (5-tsp. chunk) was placed on the plate and was loosely covered with wax paper and was microwaved for 3 minutes. The butter melted completely and covered the whole plate bottom. The butter began boiling toward the end of the test. The plate bottom got very hot and became slightly warped but no soak-through. The rim of the plate felt cool to touch enabling safe removal of the plate from the microwave oven. A small portion of the butter became charred but was easily washed off the plate. Overall plate performance was good.

S The plate bottom became very hot and was significantly warped but no soak-through was observed and the greasy film residue could not be washed off completely. Plate felt soft and rubbery when handled by the rim.

Test #8 Results—Bacon

J Three strips of raw, cured bacon were wrapped in three sheets of paper towel and cooked for 5 minutes. All of the bacon became crispy and about 20% of it was charred. The bottom of plate got very hot but most of the rim area was relatively cool to the touch. Grease exuded from bacon and soaked through the towel. The grease pooled on the plate bottom, side and on some rim areas. The grease which pooled in some rim regions caused localized melting of the plate but no holes were formed. The hot grease which pooled on plate bottom caused significant warpage but no soak-through. Overall plate performance for Test #8 was less satisfactory than Test #7.

S When the raw bacon was wrapped in paper toweling and cooked on the S plate, the bottom became very soft and stuck to the glass tray in the microwave. Under such hot grease conditions, the adhering polymer regions underwent localized melting and stretched when the plate was lifted off the glass tray. The plate was severely warped but no holes formed and no soak-through was noticed.

With the possible exception of raw bacon, the behavior of the J plate of this invention in the microwave oven is considered excellent with a variety of aqueous, greasy/fatty, sugary food combinations. No unusual or off odors were detected during and after cooking for each type of food directly on the plate. The foregoing data demonstrates the superior properties of the plates of this invention.

Crack Resistance

Low temperature crack resistance of rigid plates is of paramount importance when considering that product must survive during storage and shipping to point of sale. Normally, it is difficult to improve crack resistance or reduce brittleness of rigid polymeric materials without reducing the stiffness which is usually the case when introducing excessive amounts of softer extensible materials such as polyethylenes, rubber modified resins and the like. In order to be successful in imparting crack resistance without significantly reducing stiffness, one must add relatively low amounts of polyethylene or rubber modified additives, generally in the range of several to about 5 wt %. However, this invention shows that addition of low levels of polyethylene alone is not sufficient to promote crack resistance whereby the desired result is produced by a synergistic binary combination of polyethylene and TiO

2

. Such low odor products have high crack resistance which renders them useful in the commercial sense.

EXAMPLES 14-21

There is provided in a still further aspect of the invention toughened, crack resistant articles. It has been found that polypropylene/mineral/polyethylene/-titanium dioxide formulations without a coupling agent resist cracking. Generally, the articles have the components set forth in Table 12, in the amounts mentioned above in the summary of the invention herein. In Table 12, it is demonstrated that polyethylene/titanium dioxide exhibit synergy in resisting cracking.

TABLE 12

Low Temperature crack data for 9 inch plates made of

PP/30% mica/10% CaCO

3

modified with various combinations

of TiO

2

, polyethylene, or coupling agent

Coupling

Example

TiO

2

LLDPE

HDPE

Agent

Percent Cracked

#

(wt %)

(wt %)

(wt %)

(wt %)*

plates at 0° F.**

14

—

4

—

—

100 (n = 5)

15

—

—

—

2.5

100 (n = 5)

16

1.9

—

—

—

100 (n = 5)

17

—

4

—

2.5

100 (n = 5)

18

1.9

0

0

2.5

100 (n = 5)

19

0.5

4

—

2.5

60 (n = 5)

20

0.5

4

0

0

0 (n = 5)

21

0.5

0

4

0

0 (n = 10)

*coupling agent is maleic anhydride modified PP grade Aristech Unite NP-620. Other ingredients are: Mica = Franklin Minerals L 140, CaCO3 = Huber Q325, PP = Exxon Escorene PP4772, LLDPE = Novapol Novachemical G1-2024A

**percentage of plates which cracked at 0° F. for specimen sets comprised of the indicates number n

Crack resistance of Examples 14 through 21 was evaluated in the laboratory according to method set forth below which was found useful as an investigative tool for optimizing the formulation with various combination of TiO2, polyethylene, or coupling agent. A laboratory procedure was devised and used to evaluate the crack resistance of plates. Specifically, following is a description of test instruments and associated fixtures used to subject plates to a repeatable rim crushing force. The model numbers of standard equipment used on this procedure are recited below and additional fixtures used in these tests were employed as follows:

Instron—Model #55R402 was used which was equipped with Instron Environmental Chamber Model #3111. The Instron environmental chamber—Model #3111 was modified to control low temperatures with liquid nitrogen. It was equipped with a control solenoid mounted on the rear of the cabinet and an electronic control module mounted on the control panel assembly. The temperature within the chamber was controlled in relationship to the setpoint on the front panel temperature dial. A thermocouple within the chamber provides feed back to the device. A mercury thermometer was placed in the chamber and oriented so that temperature within the chamber was visible through an insulated glass door. It was monitored and adjusted to 0° C. using the panel temperature dial. A push rod was attached to the load cell of the instron and was passed through an opening in the top of the environmental chamber. A circular metal device measuring 100 mm in diameter and 10 mm in thick was attached to the end of the push rod inside the chamber. This circular metal device was used to contact the edge of a plastic plate during testing.

The plate support fixture was placed on a circular metal base support which measured 140 mm in diameter by 14 mm thick. This metal base support was located just above the inside floor of the environmental chamber. It was attached to a support rod that passes through the floor of the environmental chamber and attached to the base of the instron. Centering stops were provided on the metal base support so that the plate support fixture could be repeatedly placed at the same location in the environmental cabinet.

The plate support fixture is constructed of 5-mm thick sheets of plexiglas. The main base of this fixture measures 100×125 mm. The 125-mm dimension represents the width of the front of the mixture. The edge of the 125 mm side of a second plexiglas panel measuring 160×125 mm was permanently attached to the plexiglas main base. This panel was attached at a 90° angle to the main base and 35 mm in from the front edge. An L shaped plexiglas component was attached to the main base behind and parallel to the permanent panel by thumbscrews. Two 20-mm long slots were provided in the base of the L shaped component to allow attachment and provide movement for adjustment to hold the test plate. The short leg or base of the L shaped component faces the rear of the fixture. A block measuring 40×25×15 mm thick was permanently attached at the upper most end at the center of the L shaped component. This block is located on the front side of the moveable component or just opposite the short leg of the L shaped component, while an adjustable plate stop was attached to one side of the moveable L shaped component.

The methodology for testing the crack resistance of plates was as follows. The test plate was secured in a vertical position on edge in the plate support fixture. The bottom of the test plate was placed against the permanently attached plexiglas panel of the plate support fixture. The thumbscrews were loosened on the moveable portion of the plate support fixture. The L shaped moveable component was moved toward the plate. The plate was held in a vertical position by the fixed plexiglas panel and the block which was attached to the wall of the L shaped moveable component.

The plate stop located on the L shaped moveable component was adjusted so that the center of the plate would align with the center of the plate support fixture. The plate support fixture along with the test plate secured in a vertical position was placed on the metal base support in the environmental chamber. The instron was adjusted so that the push rod crush assembly was located 0.5 inches above the plate edge.

Prior to the test, the environmental chamber was adjusted to 0° F. After placement of the plate support fixture along with the test plate secured in a vertical position in the environmental chamber, the chamber had to re-establish 0° F. This time period was about 30 seconds. After reestablishment of the test temperature, the plate was conditioned for an additional five minutes prior to the test The crosshead speed of the instron was set at 40 inches per minute. After the five minute conditioning time period, the instron was activated and the edge crushing force applied. A set of five or a set of ten replicate plates was tested for each condition. The total number of plates tested and the total number plates showing rim crack failure for each condition tested are reported in Table 12. In addition, the percentage of plates which cracked was calculated as shown above. The above formulations for crack resistance testing were compounded in the temperature range of 400 to about 425° F. on commercial Banbury equipment using batch sizes in the range of 150-200 lb. and nominal mixing times of 3 min. followed by underwater pelletizing.

Pellets were subsequently extruded at 370° F. as cast sheets in the range of 18 mil. Sheet line conditions also included a screw RPM value of 100, a chill roll temperature of 130° F. Plates were subsequently vacuum thermoformed using a female mold, trimmed, and thereafter tested for crack resistance.

Data on Examples 14 through 16 show that presence of TiO

2

, polyethylene, or coupling agent alone is not sufficient to promote crack resistance of plates comprised of PP/mica/CaCO

3

. In addition, data on Examples 17 and 18 show that binary combinations of polyethylene with coupling agent or TiO

2

with coupling agent are two cases which are also not sufficient for imparting crack resistance. Furthermore, the tertiary combination of TiO

2

, polyethylene, and coupling agent (Example 19) also does not impart sufficient crack resistance, as evidenced by the majority of samples which exhibit cracking. Rather, the useful additive packages of this invention (Examples 20 and 21) comprises the binary system of polyethylene (either LLDPE or HDPE) with at least 0.5 wt % TiO

2

whereby crack resistance is excellent as evidenced by no cracked samples.

EXAMPLES 22-29

Additional plates were fabricated in accordance with the foregoing procedures and compositions; crack testing results appear in Table 13 below.

TABLE 13

Crack Data and Physical Properties for Various Compounded Formulations

Base Formulation: PP/30% Mica/10% CaCO

3

Melt

Flow

Flexural

Formulation

g/10

Filler

Modulus

9″ Plate

Product

Crack

TiO

2

PE

Coupling

min. @

Content

Tangent

Rigidity

Weight

Data @ 0° F.

Example

(wt. %)

(4 wt. %)

Agent*

230° C.

(Wt. %)

(psi)

(grams/0.5″)

(grams)

(# Cracked Total)

22

0

LLDPE

No

1.45

39.4

505,000

288

19.3

5/5

23

1.9

LLDPE

No

1.64

40.6

581,600

422

23.13

0/5

24

1.2

LLDPE

No

2.05

39.8

578,500

385

22.12

0/5

25

0.5

LLDPE

No

1.77

38.6

487,500

286

20.65

0/5

26

1.9

HDPE

No

1.5

40.6

637,500

436

22.70

1/5

27

1.9

0

Yes

1.9

39.0

717,585

417

21.25

5/5

28

1.9

LLDPE

Yes

1.6

39.6

494,000

391

21.6

5/5

29

1.9

0

Yes

1.2

40.3

593,000

353

20.8

5/5

*When present, coupling agent concentration is 2.5%

In a still further aspect of the invention, food contact articles are provided by way of preparing a melt-compounded composition with from about 40 to 90 percent of a polypropylene polymer, about 10 to about 50 percent by weight of a mineral filler and optionally an effective amount of an odor-reducing compound. The melt-compounded composition is extruded into a sheet and formed into a food contact article and is characterized by a relative aroma index, relative to a composition containing 30 weight percent mica only, of less than about 0.75; preferably less than about 0.6. The relative aroma index is thus defined similarly as above; however, relative to a mica composition without an odor suppressing compound such as calcium carbonate. Stated another way, the relative aroma index is determined in the same way as the odor index utilizing the AromaScan® device as noted above or other suitable instrument, except a 30 wt % mica filled composition is used as the reference (or denominator) compound. In equation form,

Relative  Aroma  Index = \frac{\begin{matrix} \begin{matrix} average readings of pellets including a \\ primary mineral filler and optionally \end{matrix} \\ including calcium carbonate or other \\ odor suppressing compound \end{matrix}}{\begin{matrix} \begin{matrix} average readings of pellets including 30 wt % \\ mica only without an odor suppressing \end{matrix} \\ basic compound \end{matrix}}

Thus, a composition consisting essentially of 30% talc, 10% calcium carbonate and the balance polypropylene would have a relative aroma index, relative to a 30% by weight mica composition of:

Relative Aroma Index = \frac{\begin{matrix} average readings of 30 % talc, 10 % calcium \\ carbonate, 60 % polypropylene composition \end{matrix}}{\begin{matrix} average readings of 30 % mica, 70 % \\ polypropylene composition \end{matrix}}

The invention also includes: (a) preparing a melt-compounded composition including from about 90 percent by weight of a polypropylene polymer, from about 10 to about 50 percent by weight of a primary mineral filler and optionally an effective odor-reducing amount of a basic or optionally acidic organic or inorganic compound; (b) extruding the melt-compounded composition into a sheet; and (c) forming a food contact article from the sheet, wherein the melt compounded composition exhibits a relative aroma index of 0.75 or less. Particularly preferred primary mineral fillers include talc, kaolin, bentonite and wollastonite.

While the invention has been exemplified and described in detail, numerous modifications to specific examples within the spirit and scope of the invention will e apparent to those of skill in the art. The invention is defined in the appended claims.

Number	Name	Date	Kind
D41986	Smith	Dec 1911	S
D51874	Beyrand	Mar 1918	S
D61248	Reizenstein	Jul 1922	S
1440070	Fry	Dec 1922	A
D66556	Cunningham	Feb 1925	S
D76433	Tams	Sep 1928	S
D86627	Newton	Mar 1932	S
1848066	Shepard et al.	Mar 1932	A
D88688	Thompson	Dec 1932	S
D103599	Ruck	Mar 1937	S
D106554	Wilson	Oct 1937	S
D109494	Leigh	May 1938	S
D116789	Barbiers	Sep 1939	S
D116790	Barbiers	Sep 1939	S
D135030	Harshman	Feb 1943	S
D140345	Fordyce	Feb 1945	S
D164669	Chaplin	Oct 1951	S
D169133	Foster	Mar 1953	S
2738915	St. Clair	Mar 1956	A
D179011	Kimble	Oct 1956	S
2928567	Davis	Mar 1960	A
D188502	Metzler et al.	Aug 1960	S
D190336	Dennl	May 1961	S
3001665	Tomarin	Sep 1961	A
D221290	Wiedemann	Jul 1971	S
3672538	Widemann	Jun 1972	A
3675811	Artz	Jul 1972	A
D232613	Cheladaze	Sep 1974	S
3930890	Dietz	Jan 1976	A
D250928	Franklin	Jan 1979	S
D251713	Brody	May 1979	S
D275255	Durand	Aug 1984	S
D276117	Solt	Oct 1984	S
D279345	Durand	Jun 1985	S
4578296	Miyazaki et al.	Mar 1986	A
4734450	Kawai et al.	Mar 1988	A
4746057	Wagner	May 1988	A
4781295	Gunesin et al.	Nov 1988	A
4809876	Tomaswick et al.	Mar 1989	A
4933526	Fisher et al.	Jun 1990	A
4981631	Cheung et al.	Jan 1991	A
D316800	Wertheim	May 1991	S
5023286	Abe et al.	Jun 1991	A
5045369	Kobayashi et al.	Sep 1991	A
5088640	Littlejohn	Feb 1992	A
5165978	Lecinski	Nov 1992	A
5184995	Kuchenbecker	Feb 1993	A
D342186	Frere	Dec 1993	S
5300747	Simon	Apr 1994	A
D348804	Feer	Jul 1994	S
D351316	Mann	Oct 1994	S
D351968	Zivin	Nov 1994	S
D354884	Carranza	Jan 1995	S
5377860	Littlejohn et al.	Jan 1995	A
5439628	Huang	Aug 1995	A
D364537	Anderson	Nov 1995	S
5622780	Paleari	Apr 1997	A
5665442	Andersen et al.	Sep 1997	A
D386048	Bebawey	Nov 1997	S
5758773	Clements	Jun 1998	A

Number	Date	Country
0 407 198	Jan 1991	EP
0 532 233	Mar 1993	EP
0 837 003	Apr 1998	EP
2101307	Mar 1972	FR
53-84044	Dec 1976	JP
59-209520	May 1983	JP

Smooth profiled food service articles

Information

Patent Number

Date Filed

Date Issued

Inventors

Original Assignees

Examiners

Agents

CPC

US Classifications

Field of Search

US

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Abstract

Description

Claims

CROSS-REFERENCE TO RELATED APPLICATIONS

US Referenced Citations (60)

Foreign Referenced Citations (6)

Provisional Applications (1)