U.S. patent number RE28,594 [Application Number 05/460,551] was granted by the patent office on 1975-10-28 for manufactured articles of blends of thermoplastic polymers having different fluidity degrees.
This patent grant is currently assigned to Monecatini Societa General per et al.. Invention is credited to Mario Catoni, Pier Lodovico Chini, Isidoro Ronzoni.
United States Patent |
RE28,594 |
Ronzoni , et al. |
October 28, 1975 |
**Please see images for:
( Certificate of Correction ) ** |
Manufactured articles of blends of thermoplastic polymers having
different fluidity degrees
Abstract
Stippled surface thermoplastic articles are produced by
extruding a mixture of a polymer of higher fluidity degree and one
of lower fluidity degree at a temperature above the temperature of
fluidization of the former but below the temperature of
fluidization of the latter. Preferred polymers include
polymethylmethacrylate, ABS type resins, and various copolymers of
methylmethacrylate or of styrene.
Inventors: |
Ronzoni; Isidoro (Camerlata
(Como), IT), Catoni; Mario (Milan, IT),
Chini; Pier Lodovico (Bergamo, IT) |
Assignee: |
Monecatini Societa General per et
al. (Milan, IT)
|
Family
ID: |
27272500 |
Appl.
No.: |
05/460,551 |
Filed: |
April 12, 1974 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
Reissue of: |
425320 |
Jan 13, 1965 |
03655829 |
Apr 11, 1972 |
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Foreign Application Priority Data
Current U.S.
Class: |
525/226;
260/DIG.32; 264/349; 525/82; 525/84; 525/228; 264/173.18; 525/83;
525/227; 525/230 |
Current CPC
Class: |
B29C
48/175 (20190201); C08L 33/12 (20130101); C08L
55/02 (20130101); C08L 57/00 (20130101); C08L
33/12 (20130101); C08L 2666/04 (20130101); C08L
55/02 (20130101); C08L 2666/04 (20130101); C08L
57/00 (20130101); C08L 2666/02 (20130101); B29C
48/08 (20190201); C08L 2205/18 (20130101); B29C
48/09 (20190201); B29C 48/12 (20190201); C08L
2205/02 (20130101) |
Current International
Class: |
C08L
33/00 (20060101); B29C 47/04 (20060101); C08L
33/12 (20060101); C08L 55/00 (20060101); C08L
55/02 (20060101); C08L 57/00 (20060101); C08f
024/24 () |
Field of
Search: |
;260/901,876 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Tillman; Murray
Assistant Examiner: Seccuro; C. J.
Claims
What we claim and desire to protect by Letters Patent is:
1. A process for producing articles having a stippled surface, said
.[.method.]. .Iadd.process .Iaddend.comprising extruding a mixture
of at least two thermoplastic polymers having different degrees of
fluidity, the ratio of the fluidity of the polymer having the
higher degree of fluidity to the fluidity of the polymer having the
lower degree of fluidity being at least 2.67, said extrusion being
performed at a temperature higher than the temperature of
fluidization of the polymer having a higher degree of fluidity and
lower than the temperature of fluidization of the polymer having
the lower degree of fluidity, said degree of fluidity being
determined according to ASTM 1238-62 at 190.degree. C with nozzle
diameter of 3 mm and plunger load of 10 kg; said polymers being
selected from the group consisting of polymethyl methacrylate, a
copolymer of methylmethacrylate with an acrylic ester or
methacrylic ester of a higher aliphatic alcohol;
polymethyl-methacrylate cross-linked with glycoldimethacrylate;
.[.and.]. an impact-proof ABS resin .Iadd.and a copolymer of
methylmethacrylate and styrene, .Iaddend.at least one of said
polymers being a polymethylmethacrylate polymer.
2. The process of claim 1, wherein the polymer component having
high fluidity is prsent in a ratio of from 95 to 40 parts by
weight, while the polymer component having low fluidity is present
in a ratio of from 5 to 60 parts by weight.
3. The process of claim 1 where a coloring agent is added to the
polymer mixture, before extrusion.
4. The process of claim 1 where an antioxidant is added to the
polymer mixture, before extrusion.
5. The process of claim 1 where a plastifier is added to the
polymer mixture, before extrusion.
6. The process of claim 1 where coloring agents, antioxidants and
plastifiers are added to the polymer mixture singly or
together.
7. The process of claim 1 wherein two polymethylmethacrylates of
differing degrees of fluidity are used.
8. The process of claim 1 where one polymethylmethacrylate has a
fluidity degree of from 0.8 to 1.3; while the second
polymethylmethacrylate has a fluidity degree from 0.1 to 0.3.
9. The process of claim 1, wherein polymethylmethacrylate and
polymethylmethacrylate cross-linked with 1% of glycoldimethacrylate
are use. .[.10. The process of claim 1 where the polymer mixture
consists of polyvinylchloride, polymethylmethacrylate which has a
fluidity degree of from 0.8 to 1.3, and polymethylmethacrylate
which has a fluidity degree of
0.1 to 0.3..]. 11. A method for the production of an article of
manufacture having a rough surface which diffuses light which
comprises blending (1) particles of a cross-linked, thermoplastic
polymer of a monomer selected from the group consisting of a
methacrylate, said polymer having been cross-linked with a
polyfunctional, cross-linking monomer, with (2) a non-cross-linked,
thermoplastic polymer of a monomer selected from the group
consisting of a methacrylate, and directly forming, by extrusion,
the resultant blend, as such, into said article, wherein said
non-cross-linked, thermoplastic polymer is molten at least during
said forming and said particles have diameters ranging from about
0.1 mm. to 2.5 mm. and are present in said blend in an amount
ranging from about 5%
to about 60%, by weight, based on the total weight of the blend.
12. A method according to claim 11 wherein said thermoplastic
polymers are
polymers of methyl methacrylate. 13. An article of manufacture
formed directly by extruding a blend of (1) particles of a
cross-linked thermoplastic polymer of a monomer selected from the
group consisting of a methacrylate, said polymer having been
cross-linked with a polyfunctional, cross-linking monomer and (2) a
non-cross-linked, thermoplastic polymer of a monomer selected from
the group consisting of a methacrylate, wherein said particles have
diameters ranging from about 0.1 mm. to 2.5 mm. and are present in
said blend in an amount ranging from about 5% to about 60%, by
weight, based on the total weight of the blend, and said
non-cross-linked, thermoplastic polymer was molten at least during
said
extrusion of the blend. 14. A composition according to claim 13
wherein either thermoplastic polymer is a polymer of methyl
methacrylate.
Description
This invention relates to manufactured articles made from
thermoplastic polymers, which articles have a stippled surface
appearance and are obtained by direct extrusion, and to a process
for their production.
An object of the present invention is the preparation of
manufactured articles (e.g. flat and corrugated plates, pipes,
structural shapes) from thermoplastic polymers, or mixes of
thermoplastic polymers, having a stippled surface appearance, by
direct extrusion of the materials in the extruder. By the use of
the term "manufactured article having a stippled surface
appearance," we mean a manufactured article which, although
homogeneous internally, has discontinuities on its surface, namely
"stipple or pin-spots" which on the whole produce a decorative
appearance; these decorative effects are also known as embossing,
and therefore the materials are said to be embossed articles.
At the present time, these effects are obtained by a batch process,
by placing the polymer in a vertical press provided with a suitable
metallic mold at a high temperature, or alternatively, by a
continuous process, by calendering the polymer articles obtained by
extrusion or molding by means of engraved cylinders. Such articles
with a stippled surface appearance can also be obtained by casting
in suitable molds.
The present invention eliminates further treatment of the articles
or the use of additional equipment to obtain the stippled effect,
thus effecting a substantial saving of time and effort.
It has now been found that by extruding a suitable mixture of
thermoplastic polymers, the stippled effect is obtained directly at
the extruder outlet without the necessity of additional processing.
The polymer mixture used herein consists essentially of two
components: the first component being a thermoplastic polymer or
mixture of thermoplastic polymers having a high fluidity, or a low
viscosity, in the molten state; and the second component being a
.Iadd.thermoplastic polymer or mixture of thermoplastic polymers
having little or no fluidity or, in other words, having a high
viscosity, in thermoplastic state. Fluidity degree .Iaddend.is
determined according to ASTM 1238-62 with the following particular
conditions:
Temperature-190.degree. C.
Nozzle diameter-3 mm.
Load on the plunger-10 kg.
Suitable mixtures include those wherein the first (high fluidity)
component is polymethylmethacrylate having a fluidity degree of
from 0.8 to 1.3 and the second (low fluidity) component is
polymethylmethacrylate having a fluidity degree from 0.1 to 0.3.
Other suitable mixtures include, for example, polyvinylchloride,
polymethylmethacrylate having a fluidity degree of from 0.8 to 1.3,
and polymethylmethacrylate having a fluidity degree of 0.1 to
0.3.
One combination of thermoplastic polymers of the present invention
is a polymethylmethacrylate having a fluidity of 1.1, and a
polymethylmethacrylate having a fluidity of 0.18. Another is a
polymethylmethacrylate having a fluidity of 1.1 and
polymethylmethacrylate, cross-linked with 1% of
glycoldimethacrylate, having a fluidity which is so low as to be
unmeasurable by the method indicated hereinabove.
In place of polymethylmethacrylate, its copolymers with styrene,
alpha-methylstyrene, acrylic esters, methacrylic esters of higher
aliphatic alcohols, acrylonitrile, and vinyl esters can be
substituted, while proceeding with the process described herein.
Similar results are obtained with styrene and its copolymers.
It is not necessary that the materials to be mixed have the same or
analogous chemical structure; on the contrary it is only important
that they are compatible and that they show a different
fluidity.
As an example, stippled manufactured articles can be obtained by
extruding polymethylmethacrylate having a low fluidity, with a
mixture consisting of polyvinylchloride and polymethylmethacrylate
having a normal fluidity; in this particular case the materials are
also self-extinguishing. Another suitable mixture consists of an
impact proof material comprising an ABS resin and of a
polymethylmethacrylate having a fluidity of 0.18.
The polymers or the mixes of polymers having different fluidity
employed in order to obtain these materials can be prepared in many
different manners, that is, either in suspension or in bulk, or in
solution, or in emulsion. However, in order to obtain the
decorative effects which are the object of the present invention,
it is essential that they are mixed in dry solid form, or as
pellets suspended in a medium to be dried successively. The size of
the polymers, pellets and granules or powders can be widely varied,
but it is necessary that they be suitable for the commonly used
extrusion process for thermoplastic materials.
The amounts of the two components are also widely variable, but an
amount of about 5% of the polymer having the low fluidity is
sufficient to give the above described stippled effects. A
preferred ratio is from about 95 to 40 parts of the polymer having
high fluidity, and from 5 to 60 parts of the polymer having low
fluidity. However, higher amounts of the latter can be used, thus
obtaining different effects as far as the intensity and the
appearance are concerned.
It is further possible to use for the preparation of these articles
of stippled surface appearance any of the additives generally used
in plastic materials such as plasticizers, lubricants,
antioxidants, coloring agents, absorbents of ultraviolet rays,
etc., provided that they are used within suitable ratios, being
added singly or together.
The process for the preparation of these articles of stippled
surface appearance is very simple. Preferably the operation is
carried out as follows: The previously mixed polymer (in the dry
state) is fed into the extruder. The extruder works at a
temperature higher than that suitable for the normal extrusion of
the more fluid polymer, this temperature being in relation to the
amount of the polymer having a low fluidity that is used, in the
way, that higher amounts of the polymer having lower fluidity in
the mixture require significantly higher operating temperatures of
the extruder than those of the polymer having higher fluidity. In
any case the extrusion temperature of the mixtures never reaches
the extrusion temperature of the polymer having lower fluidity.
At the outlet of the extruder, the stippled surface article is
cooled in air according to conventional methods. The mechanical
properties of the manufactured articles which are obtained
according to our process are analogous to those which are obtained
by means of conventional processes.
The stippled surface articles of the present invention can be made
using all of the conventional equipment for extrusion generally
used for thermoplastic material. The decorative stippled effect can
be seen either in transparent products or in opalinized, colored or
pigmented materials. It can be intensified by suitably varying the
optical characteristics of either of the materials or of both.
Different effects without limitation of numerical quantity can be
obtained, by varying materials used.
With regard to additional operations, the stippled surface
appearance articles prepared according to the present invention,
behave exactly the same as those having a smooth surface. In fact,
cutting, shaping and gluing are performed under the same conditions
and by use of the same equipment. Furthermore, it is to be noted
that in the case of very great stretching, the stippled effect
(surface showing stipple or pin-spots) of the plate and its
superficial appearance remain unchanged. This characteristic is
surprising, although extremely useful, since it allows one to
maintain unchanged the effect of light diffusion in thin layers of
opaline materials. This does not occur with numerous other
materials. The stippled effect still remains even if the
manufactured articles at the outlet of the extruder are treated
with a smooth cylinder. In this situation, the stippled effect
results in a brighter and smoother surface similar to that of
sandblasted glass. The optical characteristics of these articles
are particularly surprising, since they show simultaneously, both
high transparency, and also, high light diffusion. The present
invention includes products produced by the foregoing process which
are thereafter calendered by treatment with engraved cylinders.
The following examples are given to illustrate the present
invention without limiting it in any way. The amounts reported in
the examples are to be understood as amounts by weight, unless the
contrary is clearly stated.
EXAMPLE 1
15 kg./h. of the following mixture is fed to an extruder provided
with degasification and having a head of 300 .times. 3.3 mm.:
100 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 1.1 and an average diameter of between 0.1 and
0.3 mm.;
10 parts of transparent pearls of polymethylmethacrylate having a
fluidity degree of 0.18 and an average diameter of between 0.1 and
0.3 mm.
The two types of polymethylmethacrylate have been previously mixed
in a powder mixer for 20-30 minutes. The extruder works at a
temperature of about 240.degree. C. during the plastifying
operation and during the degasification operation. In this way 18
m./h. of a flat plate having a thickness of about 3 mm. and width
of 250 mm. is obtained. The plate is cooled in the air on a
suitable draft gear. It shows on the surface (stipple or pin-spots)
a typical stippled appearance. The light transmission and the light
diffusion of this article measured according to ASTM D 1003 on
specimens having a thickness of about 3 mm. are respectively 89 and
18%.
EXAMPLE 2
15 kg./h. of the following mixture is fed to an extruder similar to
that described in Example 1:
100 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 1.1 and a diameter of between 0.1 and 0.3
mm.;
20 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 0.18 and an average diameter of between 0.1 and
0.3 mm.
The two types of polymethylmethacrylate have been previously mixed
in a powder mixer for 20-30 minutes. The extruder works at a
temperature of about 250.degree. C. during the plastifying and
degasification operation. In this way, 18 m./h. of a flat plate
having a thickness of about 3 mm. and a width of about 250 mm. are
obtained. The plate is cooled in the air on a suitable draft gear.
It shows on the surface, a typical stippled decorative effect as
can be seen in the accompanying diagram, wherein section 1
represents a top view of transparent normal plate of
polymethylmethacrylate, placed on a drawing with thick lines,
whereas section 2 thereof shows a top view of a part of a plate
obtained by working as described in this example and placed on the
same drawing. The light transmission and diffusion of this product
measured according to ASTM D 1003 on a specimen having a thickness
of 3 mm. are respectively 85 and 48%.
EXAMPLE 3
15 kg./h of the following mixture is fed to an extruder similar to
that described in Example 1:
100 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 1.1 and a diameter of between 0.1 and 0.3
mm.;
50 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 0.18 and an average diameter of between 0.1 and
0.3 mm.
The two types of polymethylmethacrylate have been previously mixed
in a powder mixer for 20-30 minutes. The extruder works at a
temperature of about 250.degree. C. during the plastifying and
degasification step; in this way, 18 m./h. of a flat plate having a
thickness of about 3 mm. and a width of about 250 mm. is obtained.
The plate is cooled in the air on a suitable draft gear. It shows
on its surface a typical and marked decorative stippled effect, as
can be seen in section 3 of the accompanying diagram, which shows a
top view of a plate of the product obtained according to the
present process, and placed on a drawing having thick lines. The
light transmission and diffusion of this product measured according
to ASTM D 1003 on specimens having a thickness of 3 mm. are
respectively 80 and 88%.
EXAMPLE 4
Two suspensions of polymethylmethacrylate pearls having a pearl
content of about 25% are mixed in an autoclave in the ratio 10:2.
The first suspension consists of transparent polymethylmethacrylate
pearls having a fluidity degree of 1.1 and an average diameter of
between 0.1 and 0.3 mm.; the second suspension consists of
transparent polymethylmethacrylate pearls having a fluidity degree
of 0.18 and an average diameter of between 0.1 and 0.3.
After agitating for 10 minutes, the mixture of the two suspensions
is discharged into a centrifuge, and then the separated product is
dehydrated and dried. The dry product is sent to an extruder
similar to that described in Example 1, in quantities of 15 kg./h.
The extruder works at a temperature of about 250.degree. C. during
the plastifying and degasification step. In this way, 18 m./h. of a
flat plate having a thickness of about 3 mm. and a width of about
250 mm. is obtained. The plate is cooled in the air on a suitable
draft gear. It shows on the surface a typical decorative stippled
effect. The light transmission and diffusion of this product when
measured according to ASTM D 1003 on specimens having a thickness
of 3 mm. are respectively 85 and 48%.
EXAMPLE 5
15 kg./h. of the following mixture is fed to an extruder similar to
that described in Example 1:
100 parts of transparent methylmethacrylate pearls having a
fluidity degree of 1.1 and an average diameter of between 0.1 and
0.3 mm.
10 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 0.18 and an average diameter of between 0.1 and
0.3 mm.;
Parts Barium sulfate 2 Cacoyl violet ZIRS (anthraquinone
derivative, NYMCO S.p.A. 0.02 Tinuvin P
(hydroxy-phenyl-benzotriazole) 0.1 Stearic acid 0.2
are fed. The mixture is first mixed in a powder mixer for 20-30
minutes and then sent to the extruder. The extruder works at a
temperature of about 240.degree. C. during the plastifying and
degasification step. In this way, about 18 m./h. of a flat plate
having a thickness of about 3 mm. and a width of 250 mm. is
obtained. The plate is cooled in the air on a suitable draft gear.
It is opalized and shows a typically stippled surface with a
decorative effect. The light transmission and diffusion of this
product, when measured according to ASTM D 1003, on specimens
having a thickness of 3 mm., are 45 and 100% respectively.
EXAMPLE 6
15 kg./h of the following mixture is fed to the same extruder
described in Example 1:
100 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 1.1 and an average diameter of between 0.1 and
0.3 mm.;
20 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 0.18 and an average diameter of between 0.1 and
0.3 mm.
______________________________________ Parts Blue Vaxoline APS
(Sesacolor S.p.A., color in- dex: solvent blue 36, page 2883) 0.007
Red Vaxoline MPS (Sesacolor S.p.A., color in- dex: dispersed red 9)
0.0019 Yellow Vaxoline IS (Sesacolor S.p.A., color in- dex: solvent
yellow 14, page 2821) 0.00055 Tinuvin P
(hydroxy-phenyl-benzotriazole) 0.200
______________________________________
The mixture is previously mixed in a powder equipment for 20-30
minutes and then it is sent to the extruder. The extruder works at
about 250.degree. C. during the plastifying and degasification
step. In this way, 18 m./h. of a flat plate having a thickness of
about 3 mm. and width of 250 mm. is obtained. The plate is cooled
in the air on a suitable draft gear. It is grey colored and has the
typically stippled decorative effect surface. The light
transmission and diffusion of this product, when measured according
to ASTM D 1003, on specimens having a thickness of 3 mm., are 67
and 44% respectively.
EXAMPLE 7
15 kg./h. of the following mixture is fed to the same extruder
described in Example 1:
40 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 1.1 and a diameter of between 0.1 and 0.3
mm.;
20 parts of transparent polymethylmethacrylate pearls having a
fluidity degree of 0.18 and a diameter of between 0.1 and 0.3
mm.;
60 parts of polyvinylchloride pearls having a constant K of 62-65
(as constant K we intend the time for the fall measured in seconds
between two winning-posts 10 cm. distant, of a steel ball having a
weight of 2.03 g. into a test-glass having a diameter of 20 mm.
containing the platisol (polyvinylchloride dioctylphthalate 60:40),
at 20.degree. C.
______________________________________ Parts
Trichloroethylphosphate 5 Stanclere (tin alkylmercaptide) 173 1.8
Santowhite Crystal (4,4'-thiobis (6 tert. butyl- methacresol)
0.0015 Tinuvin P 0.100 Loxiol 30 (a wax like substance produced by
Neynaber Society) 0.500 Loxiol 31 (esters of fatty acid produced by
Ney- naber Society) 0.70 Calcoil Violet Z1RS 0.0003
______________________________________
The polymers and the additives are previously mixed in a powder
mixer for 20-30 minutes and then sent to the extruder. The extruder
works at a temperature of about 160-175.degree. C. during the
plastifying and degasification step. In this way, 18 m./h. of a
flat plate having a thickness of about 3 mm. and a width of 250 mm.
are obtained. The plate is cooled in air on a suitable draft gear.
It is transparent and its surface is typically stippled with a
decorative effect. Tested according to ASTM D 635 the plate proves
also self-extinguishing.
EXAMPLE 8
15 kg./h. of the following mixture is fed to an extruder similar to
that described in Example 1:
Parts Transparent polymethylmethacrylate pearls having a fluidity
degree of 1.1 and a diameter of between 0.1 and 0.3 mm. 100
Transparent polymethylmethacrylate granules having a fluidity
degree of 0.18 and a diameter of between 0.8 and 2.5 mm. and
obtained by milling polymeth- ylmethacrylate prepared in bulk
20
The two types of polymethylmethacrylate have been previously mixed
in a powder mixer for 20-30 minutes. The extruder works at a
temperature of about 250.degree. C. during the plastifying and
degasification step. In this way 18 m./h. of a flat plate having a
thickness of about 3 mm. and a width of about 250 mm. are obtained.
The plate is cooled in air on a draft gear. The plate shows a
typical decorative stippled effect on the surface. The light
transmission and diffusion of this product, when measured according
to ASTM D 1003, on specimens having a thickness of 3 mm. are 85 and
48% respectively.
EXAMPLE 9
15 kg./h. of the following mixture is fed to the same extruder
described in Example 1:
Parts Granules of an impact-proof ABS resin (type B 32 produced by
Montecatini Edison S.p.A.) 80 Polymethylmethacrylate pearls having
a fluidity de- gree of 0.18 and an average diameter of between 0.1
and 0.3 mm. 20
The polymers are previously mixed in a powder mixer for 20-30
minutes and then sent to the extruder. The extruder works at a
temperature of 180.degree.-200.degree. C. during the plastifying
phase and degasification step.
In this way 18 m./h. of a flat plate having a thickness of about 3
mm. and about 250 mm. width are obtained. The plate is opaque and
its surface is typically stippled with a decorative effect.
EXAMPLE 10
80 kg./h. of the following mixture is fed to an extruder provided
with degasification and having a head of 1,250 mm.:
Parts Transparent polymethylmethacrylate pearls having a fluidity
degree of 1.1 and a diameter of between 0.1 and 0.3 mm. 100
Transparent polymethylmethacrylate pearls having a fluidity degree
of 0.18 and diameter of between 0.1 and 0.3 mm. 20
The two types of polymethylmethacrylate have been previously mixed
into a powder mixer for 20-30 minutes. The extruder works at a
temperature of about 250.degree. C. during the plastifying and
degasification step. In this way, 20 m./h. of a plate having a
thickness of about 3 mm. and a width of about 1,200 mm. are
obtained. This plate is transparent and its surface shows the
typical stippled decorative effect. The light transmission and
diffusion of this product when measured according to ASTM D 1003
are 85 and 48% respectively.
While the present invention has been described with particular
reference to specific examples, it is not to be limited thereby,
but reference is to be had to the appended claims for a definition
of its scope.
* * * * *