Language selection

Search

Patent 2071078 Summary

Third-party information liability

Some of the information on this Web page has been provided by external sources. The Government of Canada is not responsible for the accuracy, reliability or currency of the information supplied by external sources. Users wishing to rely upon this information should consult directly with the source of the information. Content provided by external sources is not subject to official languages, privacy and accessibility requirements.

Claims and Abstract availability

Any discrepancies in the text and image of the Claims and Abstract are due to differing posting times. Text of the Claims and Abstract are posted:

  • At the time the application is open to public inspection;
  • At the time of issue of the patent (grant).
(12) Patent Application: (11) CA 2071078
(54) English Title: THERMOPLASTIC PHOTODEGRADABLE AND BIODEGRADABLE POLYMER BLEND
(54) French Title: MELANGE POLYMERIQUE THERMOPLASTIQUE, PHOTODEGRADABLE ET BIODEGRADABLE
Status: Deemed Abandoned and Beyond the Period of Reinstatement - Pending Response to Notice of Disregarded Communication
Bibliographic Data
(51) International Patent Classification (IPC):
  • C08L 33/14 (2006.01)
  • C08J 3/28 (2006.01)
  • C08L 7/00 (2006.01)
  • C08L 9/00 (2006.01)
  • C08L 19/00 (2006.01)
  • C08L 67/04 (2006.01)
(72) Inventors :
  • FOSTER, TERRY (Canada)
  • GNATOWSKI, MAREK (Canada)
  • KOUSTANDREAS, ANDY (Canada)
(73) Owners :
  • MINISTER OF NATIONAL DEFENCE
(71) Applicants :
  • MINISTER OF NATIONAL DEFENCE (Canada)
(74) Agent:
(74) Associate agent:
(45) Issued:
(22) Filed Date: 1992-06-11
(41) Open to Public Inspection: 1993-12-12
Examination requested: 1999-05-20
Availability of licence: N/A
Dedicated to the Public: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data: None

Abstracts

English Abstract


ABSTRACT
A photodegradable and fully biodegradable plastic
material, which can be molded using conventional molding
techniques, and which has relatively good properties includes a
blend of polyisoprene and polycaprolactone resins. The
material biodegrades in soil and sea water environments. All
blend ingredients are completely decomposed by microorganisms.
Polyisoprene is a natural polymer present in a large variety of
plant species. Polycaprolactone is a synthetic polymer resin
known to be decomposed by microorganisms. The plastic material
has thermoplastic properties which permits processing of the
material using conventional plastic-working techniques.


Claims

Note: Claims are shown in the official language in which they were submitted.


THE EMBODIMENTS OF THE INVENTION IN WHICH AN
EXCLUSIVE PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS
FOLLOWS:
1. A biodegradable and photodegradable,
thermoplastic polymer composition comprising a blend of 10 to
500 parts by weight polycaprolactone per 100 parts by weight
polyisoprene.
2. A composition according to claim 1, including 50
to 200 parts by weight polycaprolactone per 100 parts by weight
polyisoprene.
3. A composition according to claim 1, including an
additive commonly used in the plastic and rubber industry.
4. A composition according to claim 1 or 2, wherein
the polyisoprene is in the form of natural rubber.
5. A composition according to claim 1, wherein the
flow properties of the composition above the softening point
permit processing of the composition using conventional
thermoplastic working methods.
6. A composition according to claim 1 which can be
permanently oriented by the application of force.
7. A method for making a biodegradable and
photodegradable, thermoplastic polymer composition comprising
the steps of:
(a) blending 10 to 500 parts by weight
polycaprolactone with 100 parts weight polyisoprene at a
temperature above 60°C; and

(b) processing the resulting polymer blend into a
form suitable for further thermoplastic working.
8. A method according to claim 7, wherein 50 to 200
parts by weight polycaprolactone is blended with 100 parts by
weight polyisoprene.
9. A method according to claim 7, wherein blending
is performed at a temperature of 65 to 75°C.
10. A method according to claim 7, including the
step of:
(c) adding a small amount of an additive common in
the plastic and rubber industry to the composition.
11. A method according to claim 10, wherein said
additive is selected from the group consisting of casein,
antioxidants, dyes, fillers, vulcanized vegetable oils, fatty
acids and pigments.
12. A method according to claim 7, including the
step of molding the blend to form a biodegradable and
photodegradable plastic article.
13. A method according to claim 12, wherein the
blend is injection molded.
14. A method according to claim 12, wherein the
blend is blow molded.
15. A method according to claim 12, wherein the
blend is extruded.
16. A method according to claim 12, including the
step of irradiating the article.

Description

Note: Descriptions are shown in the official language in which they were submitted.


2~71~7~
This invention relates to fully biodegradable and
photodegradable polymer blends and to methods of making the
same.
More specifically, the present invention relates to
blends of polyisoprene and polycaprolactone which have
thermoplastic properties, and which are biodegradable in soil
and sea water environments, and photodegradable.
As a result of concerns about the environment and
disposal of waste materials, a great deal of effort has been
directed towards the development of biodegradable plastic
materials. The main emphasis of such effort has been placed
on the mechanisms of photodegradation and biodegradation.
Photodegradation is the decomposition of photosensitive
materials initiated by the ultraviolet component of natural
light, and biodegradation results from the action of
microorganisms such as bacteria, fungi or algae.
Photodegradablity is an inherent property of some
polymers and in certain cases it can be enhanced by the use of
photosensitizing additives. Photodegradable plastics have
found use in applications such as agricultural mulch film,
trash bags, and retail shopping bags.
Several different types of plastics have been
produced which are fully or partially biodegradable. Some
effort has been made to modify non-biodegradable polymers with
starch in concentrations of 2-15%. However some controversy
remains as to whether such materials are completely
- ' : ' : -

2071078
biodegradable. Some newer materials which use starch as part
of the polymer matrix at levels of 60-100~ are reported to be
completely biodegradable. Certain polyester polymers have
been shown to be biodegradable. These include aliphatic
esters such as polyhydroxybutyrate-valerate (PHBV) and
polycaprolactone.
Polycaprolactone blends are known which contain a
variety of thermoplastic resins including polyethylene,
polystyrene and nylon and are degradable in soil or sea water.
However, because of the presence of non-biodegradable resin
components, such blends are not completely biodegradable. In
addition, the blends do not possess accelerated photo-
degradation abilities as measured against the properties of
widely used commercial plastics.
The polyisoprene-polycaprolactone blend disclosed by
Canadian Patent No. 1,111,179 which issued to Eric G. Kent on
on October 20, 1981 is described as having thermoplastic
properties. The patented invention is used for molding
components of orthopedic devices specifically because of the
mechanical and thermal properties of the material. Canadian
Patent No. 1,080,875, which issued to Eric G. Kent on July 1,
1980 also describes a blend containing polyisoprene and
polycaprolactone. Because of its mechanical properties, the
blend is used in the manufacture of sporting goods,
specifically golf ball covers. Japanese Patent No. JP
89293048 describes a multi-component biodegradable coating
'

2~71~8
consisting of polycaprolactone, olefinic polymers, wax,
petroleum resin and fats and their derivatives including metal
salts. The possibility of introducing a natural resin
(polyisoprene) into such a coating is mentioned. Moreover,
one of the resins mentioned is natural rubber. Fertilizer
grains are coated by such a coating, which is degraded by
microorganisms in the soil.
None of the above-mentioned patents suggests a
composition which is photodegradable or biodegradable in sea
water. Only the Japanese patent mentions a composition with
the ability to biodegrade in soil. None of the patents
suggests using a composition for manufacturing a product using
known plastic working methods such as injection molding,
extrusion, blow molding or similar techniques which have
significant importance in applications for biodegradable and
photodegradable plastics.
Known biodegradable polymers have suffered slow
acceptance due to limitations in processing and high costs
relative to conventional, non-degradable polymers.
An object of the present invention is to provide a
plastic material which is completely biodegradable and
photodegradable, and which has thermoplastic properties
comprising a blend of polyisoprene and polycaprolactone.
Another object of the invention is to provide a
biodegradable and photodegradable plastic material comprising
a blend of polyisoprene and polycaprolactone which can be used

2071 078
to manufacture articles using conventional plastic processing
techniques.
Another object of the invention is to provide a
biodegradable and photodegradable article formed from a blend
of polyisoprene and polycaprolactone which has improved
mechanical properties and performance at high temperatures
because of a post-forming radiation treatment.
Yet another object of the invention is to provide a
method of making a fully biodegradable and photodegradable
plastic article by mixing polyisoprene and polycaprolactone to
form a blend, and processing the thus produced blend using
conventional plastic working techniques to form the article.
The invention provides a polyisoprene/polycapro-
lactone polymer blend having thermoplastic properties which is
fully biodegradable in soil and sea water and is photo-
degradable.
The polyisoprene/polycaprolactone blend of the
invention includes 10 to 500 parts by weight (pbw) of
polycaprolactone per 100 pbw polyisoprene resin, preferably 50
to 200 pbw of polycaprolactone per 100 pbw polyisoprene.
Some additivies such as, inter alia, casein, antioxidants,
dyes, fillers, vulcanized vegetable oils, fatty acids and
pigments commonly used in the plastic and rubber industry may
be incorporated into the blends in small amounts.
Polyisoprene can be obtained form natural rubber, or
can be produced as a synthetic polymer. Natural rubber

2071078
contains polyisoprene and is produced by many different plant
species. In its natural state, the rubber is biodegradable;
however, the use of stabilization techniques results in
reduced biodegradability. Natural rubber, in its pure form,
is not acceptable for producing useful products using
conventional techniques such as injection and blow molding,
and extrusion which are used for thermoplastic polymeric
materials. The main reasons for this are the poor flow
characteristics of natural rubber, unsuitable mechanical
properties, and tackiness prior to vulcanization.
Polycaprolactone is a synthetic polymer resin known
to be decomposed by microorganisms. However the applications
for polycaprolactone in commercial manufacturing are limited
because of its very low melting point of about 71 - 73C and
its relatively high price.
The properties of the polyisoprene/polycaprolactone
blends of this invention are very different from the
properties described above for the individual polymers. The
blends have thermoplastic properties which allow processing
using conventional plastic working techniques such as
injection molding, blow molding and extrusion. The blend has
no tackiness and does not stick to a cold metal mold. The
flow properties above the softening point of the blend permit
processing using known plastic working techniques. A blend in
accordance with the invention containing even low levels of
polycaprolactone (30%) is capable of being oriented when force

2071078
is applied, and will significantly increase the tensile
modulus and reduce or eliminate the elastic property
characteristic of some grades of polyisoprene to levels
typical of some commonly used plastics.
The polyisoprene/polycaprolactone blends can be
produced using techniques known to be suitable for blending
rubber or plastic such as extrusion, two roll milling and
Banbury milling. The blending temperature should be above
60C and preferably in the range 65-75C. The thermoplastic
resin obtained from the mixing of the two polymers should be
ground or pelletized for future use if the resin is intended
for injection molding, blow molding or extrusion manufacturing
processes. When compression or transfer or transfer molding
processes are to be used for manufacturing goods, the resin
can be stored in the form of sheets.
Such polyisoprene/polycaprolactone blends have a
relatively stable chemical structure when exposed to heat
during processing. They can be processed with standard
equipment used for injection molding, blow molding,
thermoforming, extrusion, compression or transfer molding to
manufacture bottles, containers, films, etc.
The manufactured goods produced using the
polyisoprene/polycaprolactone blend can be improved by
exposing them to electron beam or gamma radiation. Under
irradiation, the polyisoprene present in the blend becomes
cross-linked, and mechanical properties such as tensile

2~7~ 078
r
strength, elongation at break and impact strength are
significantly improved, especially when service at elevated
temperature is required.
Articles made from polyisoprene/polycaprolactone
blends which are placed in soil or sea water will biodegrade
at variable rates. The biodegradation rate depends on
conditions such as moisture level (soil), air (oxygen)
concentration, temperature, presence of microorganisms, etc.
It is expected that there should be no products of degradation
other than carbon dioxide and water. An article made from the
blends will degrade quickly when exposed to sunlight. The
presence of ultraviolet radiation in the sunlight, light
intensity and temperature will individually influence the
degradation rate.
The following examples describe preferred
embodiments of the invention.
EXAMPLE 1
30 lb of polyisoprene in the form of natural rubber
grade SMR-L was premasticated using a two roll mill at a
temperature of 50-75C. After fifteen minutes of mastication,
when the temperature rose to 75C, 15 lb of polycaprolactone,
in the form of Tone* P-787 Polymer (Union Carbide) was added
slowly over an 8 minute period. The blend was mixed at 75C
for the next 5 minutes, as per standard milling procedure, and
was then cooled and ground to achieve a particle size of 6-30
*Trademark

2~71~78
mesh blend. The resulting blend is described in the following
examples as Blend A.
EXAMPLE 2
30 lb of polyisoprene in the form of natural rubber
grade SMR-L was mixed with 30 lb of polycaprolactone in the
form of Tone 2101 (NL Chemicals). Mixing and grinding were
done as described in Example 1 with the exception that the
time for addition of the polycaprolactone to the polyisoprene
was extended to 12 minutes. The resulting blend is described
in the following examples as Blend B.
EXAMPLE 3
20 lab of polyisoprene in the form of natural
rubber grade SMR-L was mixed with 40 lb of polycaprolactone in
the form of Tone P-787 Polymer and 10 oz of Orange* PV-RL 01
(Hoechst). Mixing and grinding were done according to the
method of Example 1 with the exception that the time for
addition of the polycaprolactone to the polyisoprene was
extended to 18 minutes. The blend is described in the
following examples as blend C.
EXAMPLE 4
30 lb of polyisoprene in the form of natural rubber
grade SMR-L was premasticated using a two roll mill at a
temperature of 50-95 for 15 minutes. After mastication, when
the temperature had risen to 95C, 5 lb of edible technical
grade casein (90 Mesh) was added and mixed for another 15
minutes 95C. At this time, the temperature of the blend was
*Trademark
~ '

2071078
reduced to 75C and 15 lb of polycaprolactone in the form of
Tone P-787 Polymer was added slowly over an 8 minute period.
The blend was mixed at 75C for the next 5 minutes, as per
standard milling procedure, and was then cooled and ground to
achieve a particle size of 6-30 mesh blend. The resulting
blend is described in the following examples as Blend D.
EXAMPLE 5
An injection molding machine, with a reciprocating
screw, was fed with polyisoprene/polycaprolactone Blend A.
The temperature of the heating zones were as follows: Zone 1
- 180C, Zone 2 - 190C, Zone 3 - 200C. The nozzle heater
was at 70% capacity. A mold designed to produce test
specimens with variable thicknesses, including tensile bars
according to ASTM D-638M, was used. The mold was cooled with
tap water at 15C. Total shoot size was 23.5 g. The machine
was operated using standard procedures for molding plastics.
The moldings obtained showed adequate replication of cavities
and good surface finish.
EXAMPLE 6
A Keotex KEB-l extruder, with a 50 mm extruding
screw, was used for molding 100 ml bottles using polyisoprene/
polycaprolactone Blend C. The temperature of the heating zones
were as follows: Zone 1 - 150C, Zone 2 - 170C, Zone 3 -
170C. The extrusion head temperature was 190C. The 100 ml
bottle mold was cooled was tap water at 15C. The bottles
thus obtained had adequate finish and surface quality.
.

2071078
EXAMPLE 7
A hot press with cooling system was equipped with a
mold heated to 120C. 6.5 g of polyisoprene/polycaprolactone
Blend B or D was placed in the mold cavity measuring 0.3 mm x
140 mm x 140 mm. The mold was closed under 300 psi pressure,
heat was shut down and the cooling system was actuated. A
molding was obtained in the sheet form with no defects and a
good surface flnish.
EXAMPLE 8
Injection molded specimens in the form of tensile
bars (produced according to ASTM D-638M) were obtained using
polyisoprene/polycaprolactone Blend A. Specimens were exposed
to electron beam (EB) radiation with 120 KGray. Specimens
were later tested according to ASTM D-638M for tensile
strength and elongation at break at a temperature of 23+2C,
together with control specimens not exposed to radiation. The
results of testing, which indicate improvement in the
mechanical properties of polyisoprene/polycaprolactone Blend A
after exposure to EB radiation, are shown in Table 1.
EXAMPLE 9
Blow molded bottles made from polyisoprene/poly-
caprolactone Blend C, produced as described in Example 6, and
bottles produced from high density polyethylene (HDPE) were
placed in exterior conditions in garden soil, approximately 5
cm deep, from late March to late May in Vancouver, B.C. The
bottles were inspected at the end of the experiment and tested
:
.

2~71 07~
for weight loss, as well as for surface damage visible with
the naked eye and under a microscope. The results listed in
Table 2 indicate biodegradation of bottles made from
polyisoprene/polycaprolactone Blend C. The bottles made from
polyethylene were unchanged.
EXAMPLE 10
Plastic sheets compression molded from polyisoprene/
polycaprolactone Blend B or D in a similar manner to that
described in Example 7, and identical sheets made from HDPE
were immersed in sea water for a period of 30 or 90 days (at
water temperature of 10+2C) from the beginning of February
to the end of May. The specimen exposure area was screened
from direct sunlight. The sheets were inspected at the end of
the period and tested for weight loss, change in dimensions,
surface damage, and growth of microorganisms visible with the
naked eye and under a microscope. The results listed in Table
3 indicate biodegradation of the sheets made from the
polyisoprene/polycaprolactone blends.
EXAMPLE 11
Hot-pressed film specimens approximately 0.25 mm (10
mil) made from polyisoprene/polycaprolactone Blend C were
placed in a Q W accelerated weathering machine along with
linear low density polyethylene (LLDPE - Dupont Sclair 2114)
film specimens prepared in similar manner and were tested
according to ASTM D4329. UVB-313 lamps were employed to
irradiate the specimens with ultraviolet rays. The test

207~078
condition consisted of alternating cycles of 8 hours of UV
light followed by 4 hours of condensation. The temperature
for the light cycle was 40C and 50C for the condensation
cycle. Sample specimens were tested for tensile strength (TS)
and elongation at break (EB) after 200 hours and 400 hours
accelerated aging according to ASTM D882. The results are
shown in Table 4 and Table 5. The polyisoprene/polycapro-
lactone Blend C showed greater loss of tensile strength and
elongation at break in comparison with polyethylene.

2~71078
TABLE 1
TENSILE PROPERTIES OF SPECIMENS
Specimen Dose Temperature Tensile Strength Elongation
No. (kGy) (C) (kg/cm2)At Break
(%)
1 120 23 122.2 1355.0
2 0 23 32.1 232.9
TABLE 2
DEGRADATION IN GARDEN SOIL OF BOTTLES
MADE FROM BLEND C IN COMPARISON WITH
POLYETHYLENE BOTTLES
BottleExposure WeightWeightWeight Appearance
Materials Period Initial After Loss
(days) (g)Exposure (g)
(g)
Blend C 70 13.66112.787 0.874 Extensive
surface
deterioration
and coloniza-
tion.
Polyethylene 7013.312 13.294 0.018 No change

2~7~ ~78
TABLE 3
DEGRADATION IN SEA WATER OF SHEETS
MADE FROM BLEND B AND D IN COMPARISON
WITH HDPE SHEETS
Sheet ExposureWeight Loss Appearance
Materials Periodper 100 cm2
(days) Sample (g)*
Blend B 30 0.07 Deposit of micro-
organisms beginning
100 0.26 surface
deterioration
Blend D 30 0.08 Deposit of micro-
organisms beginning
100 0.38 surface
deterioration
HDPE 30 0 No visible
change
100
* Based on one side of specimen.
TABLE 4
TENSILE STRENGTH (TS) OF BLEND C IN
COMPARISON WITH LLDPE AFTER
EXPOSURE TO ACCELERATED WEATHERING
Polymer Exposure 200 Hours Exposure 400 Hours
TS TS Changes TS TS Changes
Initial Final (%) Initial Final (%)
kg/cm2 kg/cm2 kg/cm2 kg/cm2
Blend C 192 134 -30 192 78 -59
Polyethylene 125 149 +19 125 99 -21
..

2071078
TABLE 5
ELONGATION AT BREAK (EB) OF BLEND C
IN COMPARISON WITH POLYETHYLENE AFTER
EXPOSURE TO ACCELERATED WEATHERING
PolymerExposure 200 Hours Exposure 400 Hours
EB EB Changes EB EB Changes
Initial Final (%) Initial Final (%)
(%) (%) (~
Blend C1120 666 -41 1120 18 -98
Polyethylene 36 17 -53 36 7 -81

2071078
SUMMARY
The material described hereinbefore, namely the
blend of polyisoprene and polycaprolactone resins, possesses a
unique combination of the following properties:
(1) thermoplastic properties that allow the material to
be processed using conventional thermoplastic-
working techniques; and
(2) degradability properties that allow the material to
completely degrade following the natural mechanisms
of biodegradation and photodegradation.
Blends of the material can be successfully processed
using techniques such as injection molding, blow molding,
thermoforming, extrusion, compression molding, and transfer
molding to produce articles commonly made with thermoplastic
resins.
The addition of polycaprolactone to polyisoprene
results in increased tensile modulus, and significantly
reduced or eliminated elasticity in comparison to the original
polyisoprene properties and imparts the ability for polymer
orientation. Moreover, polycaprolactone eliminates the
problem of polyisoprene sticking to cold metal molds during
thermoplastic processing.
Blends of the material will biodegrade in soil or
sea water and will photodegrade upon exposure to sunlight, and
are expected to generate only carbon dioxide and water as
products of degradation.
16
- .
~ . . '
.: . : .
.

2~71078
The composition of the blends includes 10 to 500
parts hy weight (pbw) of polycaprolactone per 100 pbw
polyisoprene, with the preferred range being 50 to 200 pbw
polycaprolactone to 100 pbw polyisoprene. Additives commonly
used in the plastic and rubber industry may be added to the
blends in small amounts in order to enhance properties.
The prior art describes polyisoprene/polycapro-
lactone blends which possess thermoplastic properties (see
Canadian Patents Nos. 1,080,875 and 1,111,179) but, because of
the use of components such as sulphur vulcanized natural
rubber or ionomer copolymer, the feature of degradability is
not addressed. Manufacturing goods using conventional
thermoplastic processes is not mentioned. In the one case
where biodegradability is mentioned, (Japanese Patent
89293048), polyisoprene/polycaprolactone comprise a part of a
formulation, which does not possess thermoplastic properties,
and which is not photodegradable. Hence, the known prior art
does not teach combined thermoplasticity and degradability
properties.
,
.

Representative Drawing

Sorry, the representative drawing for patent document number 2071078 was not found.

Administrative Status

2024-08-01:As part of the Next Generation Patents (NGP) transition, the Canadian Patents Database (CPD) now contains a more detailed Event History, which replicates the Event Log of our new back-office solution.

Please note that "Inactive:" events refers to events no longer in use in our new back-office solution.

For a clearer understanding of the status of the application/patent presented on this page, the site Disclaimer , as well as the definitions for Patent , Event History , Maintenance Fee  and Payment History  should be consulted.

Event History

Description Date
Revocation of Agent Requirements Determined Compliant 2020-09-01
Inactive: IPC from MCD 2006-03-11
Inactive: IPC from MCD 2006-03-11
Application Not Reinstated by Deadline 2003-10-02
Inactive: Dead - No reply to s.30(2) Rules requisition 2003-10-02
Deemed Abandoned - Failure to Respond to Maintenance Fee Notice 2003-06-11
Inactive: Abandoned - No reply to s.30(2) Rules requisition 2002-10-02
Inactive: S.30(2) Rules - Examiner requisition 2002-04-02
Amendment Received - Voluntary Amendment 1999-07-26
Letter Sent 1999-06-25
Inactive: Status info is complete as of Log entry date 1999-06-25
Inactive: Application prosecuted on TS as of Log entry date 1999-06-25
All Requirements for Examination Determined Compliant 1999-05-20
Request for Examination Requirements Determined Compliant 1999-05-20
Application Published (Open to Public Inspection) 1993-12-12

Abandonment History

Abandonment Date Reason Reinstatement Date
2003-06-11

Maintenance Fee

The last payment was received on 2002-05-01

Note : If the full payment has not been received on or before the date indicated, a further fee may be required which may be one of the following

  • the reinstatement fee;
  • the late payment fee; or
  • additional fee to reverse deemed expiry.

Please refer to the CIPO Patent Fees web page to see all current fee amounts.

Fee History

Fee Type Anniversary Year Due Date Paid Date
MF (application, 5th anniv.) - standard 05 1997-06-11 1997-06-11
MF (application, 6th anniv.) - standard 06 1998-06-11 1998-04-16
MF (application, 7th anniv.) - standard 07 1999-06-11 1999-05-20
Request for examination - standard 1999-05-20
MF (application, 8th anniv.) - standard 08 2000-06-12 2000-06-09
MF (application, 9th anniv.) - standard 09 2001-06-11 2001-06-07
MF (application, 10th anniv.) - standard 10 2002-06-11 2002-05-01
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
MINISTER OF NATIONAL DEFENCE
Past Owners on Record
ANDY KOUSTANDREAS
MAREK GNATOWSKI
TERRY FOSTER
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
Documents

To view selected files, please enter reCAPTCHA code :



To view images, click a link in the Document Description column. To download the documents, select one or more checkboxes in the first column and then click the "Download Selected in PDF format (Zip Archive)" or the "Download Selected as Single PDF" button.

List of published and non-published patent-specific documents on the CPD .

If you have any difficulty accessing content, you can call the Client Service Centre at 1-866-997-1936 or send them an e-mail at CIPO Client Service Centre.


Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Cover Page 1994-03-13 1 17
Abstract 1994-03-13 1 17
Claims 1994-03-13 2 51
Description 1994-03-13 17 444
Reminder - Request for Examination 1999-02-15 1 116
Acknowledgement of Request for Examination 1999-06-25 1 179
Courtesy - Abandonment Letter (R30(2)) 2002-12-11 1 166
Courtesy - Abandonment Letter (Maintenance Fee) 2003-07-09 1 174
Fees 2001-06-07 1 39
Fees 2002-05-01 1 30
Fees 1997-06-11 1 30
Fees 1998-04-16 1 33
Fees 1999-05-20 1 28
Fees 2000-06-09 1 31
Fees 1996-05-28 1 39
Fees 1995-05-17 1 40
Fees 1994-05-12 1 37