U.S. patent number RE41,110 [Application Number 11/512,391] was granted by the patent office on 2010-02-09 for heat-resistant material and coating material for oa equipments having flexibility.
This patent grant is currently assigned to Daikin Industries, Ltd.. Invention is credited to Takayuki Araki, Masami Kato, Masahiro Kumegawa, Norihito Otsuki, Tetsuo Shimizu, Yoshito Tanaka.
United States Patent |
RE41,110 |
Araki , et al. |
February 9, 2010 |
Heat-resistant material and coating material for OA equipments
having flexibility
Abstract
It is possible to provide the heat resistant material and
coating material for OA equipment which comprise a
fluorine-containing multi-segment polymer having heat resistance,
abrasion resistance, non-sticking property against toner and oil
resistance in addition to flexibility and are used particularly on
surfaces of fuser roll and belt. Those materials comprise a
fluorine-containing multi-segment polymer having an elastomeric
fluorine-containing polymer chain segment A and a non-elastomeric
fluorine-containing polymer chain segment B, and the elastomeric
fluorine-containing polymer chain segment A comprises not less than
90% by mole of perhaloolefin unit as a recurring unit and imparts
flexibility to the whole polymer.
Inventors: |
Araki; Takayuki (Osaka,
JP), Tanaka; Yoshito (Osaka, JP), Kumegawa;
Masahiro (Osaka, JP), Otsuki; Norihito (Osaka,
JP), Kato; Masami (Osaka, JP), Shimizu;
Tetsuo (Osaka, JP) |
Assignee: |
Daikin Industries, Ltd. (Osaka,
JP)
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Family
ID: |
26567235 |
Appl.
No.: |
11/512,391 |
Filed: |
August 30, 2006 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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09582417 |
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PCT/JP98/05790 |
Dec 22, 1998 |
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Reissue of: |
10241490 |
Sep 12, 2002 |
06838139 |
Jan 4, 2005 |
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Foreign Application Priority Data
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Dec 26, 1997 [JP] |
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9-360214 |
Nov 2, 1998 [JP] |
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10-312584 |
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Current U.S.
Class: |
428/35.7; 526/79;
525/276 |
Current CPC
Class: |
C08F
293/00 (20130101); C09D 153/00 (20130101); G03G
15/2057 (20130101); C08F 214/262 (20130101); C08L
53/00 (20130101); Y10T 428/1352 (20150115) |
Current International
Class: |
B32B
27/00 (20060101) |
Field of
Search: |
;428/35.7 ;525/276
;526/79 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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1 029 875 |
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Aug 2000 |
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EP |
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2-15873 |
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Apr 1990 |
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JP |
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4-270712 |
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Sep 1992 |
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JP |
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6-220143 |
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Aug 1994 |
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JP |
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7-316246 |
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Dec 1995 |
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JP |
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WO 98/07056 |
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Feb 1998 |
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WO |
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Other References
International Search Report for PCT/JP98/05790, date unknown. cited
by examiner .
Translation of International Preliminary Examiner Report for
PCT/JP98/05790 date unknown. cited by examiner .
European Search Report for EP 98 96 1461 dated Feb. 5, 2004. cited
by examiner .
Araki et al., Caplus An 1999:460449 (Jul. 1999). cited by
examiner.
|
Primary Examiner: Mullis; Jeffrey C
Attorney, Agent or Firm: Sughrue Mion, PLLC
Parent Case Text
CROSS REFERENCE TO RELATED APPLICATION
This .Iadd.application is a REI of Ser. No. 10/241,490 filed Sep.
12, 2002, now U.S. Pat. No. 6,838,139, which .Iaddend.is a
continuation of application Ser. No. 09/582,417 filed Aug. 11,
2000, now issued as U.S. Pat. No. 6,476,151, which is a .[.317.].
.Iadd.371 .Iaddend.of PCT/JP98/05790 filed Dec. 22, 1998; the
disclosure of which is incorporated herein by reference.
Claims
What is claimed is:
1. A tube produced by molding a fluorine-containing multi-segment
polymer having an elastomeric fluorine-containing polymer chain
segment A and a non-elastomeric fluorine-containing polymer chain
segment B; said elastomeric fluorine-containing polymer chain
segment A comprises not less than 90% by mole of perhaloolefin unit
as a recurring unit and said non-elastomeric fluorine-containing
polymer chain segment B contained in said fluorine-containing
multi-segment polymer is a polymer chain having a crystalline
melting point of not less than 150.degree. C.
2. The tube of claim 1, which is characterized in that the
elastomeric fluorine-containing polymer chain segment A contained
in said fluorine-containing multi-segment polymer is a polymer
chain having a glass transition temperature of not more than
25.degree. C.
3. The tube of claim 2, which is characterized in that the
elastomeric fluorine-containing polymer chain segment A contained
in said fluorine-containing multi-segment polymer is an elastic
polymer chain comprising 50 to 85% by mole of tetrafluoroethylene
and 15 to 50% by mole of perfluoro(alkyl vinyl ether).
4. The tube of claim 3, which is characterized in that the
non-elastomeric fluorine-containing polymer chain segment B
contained in said fluorine-.Iadd.containing multi-segment polymer
is a polymer chain comprising more than 85% by mole and
.Iaddend.not more than 100% by mole of tetrafluoroethylene and from
0% by mole or less than 15% by mole of the formula (1):
CF.sub.2.dbd.CF--R.sub.f.sup.1 (1) wherein R.sub.f.sup.1 is
CF.sub.3 or OR.sub.f.sup.2, in which R.sub.f.sup.2 is a
perfluoroalkyl group having 1 to 5 carbon atoms.
5. The tube of claim 1, which is characterized in that the
non-elastomeric fluorine-containing polymer chain segment B
contained in said fluorine-containing multi-segment polymer is a
polymer chain comprising more than 85% by mole and not more than
99.7% by mole of tetrafluoroethylene and not less than 0.3% by mole
and less than 15% by mole of the formula (1):
CF.sub.2.dbd.CF--R.sub.f.sup.1 (1) wherein R.sub.f.sup.1 is
CF.sub.3 or OR.sub.f.sup.2, in which R.sub.f.sup.2 is a
perfluoroalkyl group having 1 to 5 carbon atoms.
6. The tube of claim 3, which is characterize in that the
non-elastomeric fluorine-containing polymer chain segment B
contained in said fluorine-containing multi-segment polymer is a
polymer chain comprising more than 85% by mole and not more than
99.7% by mole of tetrafluoroethylene and not less than 0.3% by mole
and less than 15% by mole of the formula (1):
CF.sub.2.dbd.CF--R.sub.f.sup.1 (1) wherein R.sub.f.sup.1 is
CF.sub.3 or OR.sub.f.sup.2, in which R.sub.f.sup.2 is a
perfluoroalkyl group having 1 to 5 carbon atoms.
7. The tube of claim 1, which is characterized in that the
non-elastomeric fluorine-containing polymer chain segment B
contained in said fluorine-containing multi-segment polymer is a
polymer chain comprising more than 85% by mole and not more than
100% by mole of tetrafluoroethylene and 0% by mole or less than 15%
by mole of the formula (1): CF.sub.2.dbd.CF--R.sub.f.sup.1 (1)
wherein R.sub.f.sup.1 is CF.sub.3 or OR.sub.f.sup.2, in which
R.sub.f.sup.2 is a perfluoroalkyl group having 1 to 5 carbon atoms.
Description
TECHNICAL FIELD
The present invention relates to a fluorine-containing
multi-segment polymer which has flexibility and is used for parts
of office automation equipment (OA equipments) requiring heat
resistance. Further the present invention relates to a coating
material prepared by using the fluorine-containing multi-segment
polymer and a tube used for OA equipments.
BACKGROUND ART
Hitherto a urethane rubber, EP rubber, silicone rubber and the like
have been used for rolls for printing machine and platen rolls. As
a fuser roll for electrophotographic copying machine, a silicone
rubber roll, a fluorine-containing rubber roll or the like is
known. However in those rolls, even in case of use of a toner
having releasing property, since releasing property (non-sticking
property against toner) is not enough, a non-elastic roll coated
with a fluorine-containing resin, an elastic roll covered with a
shrinkable fluorine-containing resin tube on its surface, or the
like has been proposed. Further there have been proposed an elastic
roll obtained by coating a mixture of fluorine-containing rubber
and fluorine-containing resin powder and then baking to form a
fluorine-containing resin powder layer on the surface of roll
(JP-B-1-36622), a roll obtained by coating a fluorine-containing
rubber and fluorine-containing resin powder, baking and then
further coating a fluorine-containing resin powder to form a
fluorine-containing resin layer (JP-B-6-100876), and the like
roll.
In fixing operation of electrophotographic copying machine, coating
of a releasing oil, generally a silicone oil on a fuser roll is
carried out to improve releasing property of the roll. In that
case, in order to prevent a silicone oil from permeating inside the
roll and causing swelling of the fuser roll, there have been
proposed a fuser roll obtained by covering a shrinkable
fluorine-containing resin tube on an elastic roll or a fuser roll
provided with a silicone rubber layer, a fluorine-containing rubber
layer or fluorosilicone rubber layer and a silicone rubber layer in
that order on its metallic core roll as described in
JP-A-1-205188.
Also in JP-A-62-285839, the present inventors proposed an elastic
roll obtained by forming a layer of fibrillated
polytetrafluoroethylene (PTFE), particularly stretched porous
polytetrafluoroethylene impregnated and integrated with a heat
resistant elastomer material on its metallic core roll.
On the other hand, in the roll for printing machine and platen roll
which are produced by using a urethane rubber, EP rubber or
silicone rubber, elasticity of the roll is good, but releasing
property is not always said to be good. For that reason, there were
problems that troubles such as adherence of toner, contamination of
printed matters due to adherence of paper powder and winding of
paper on a roll occur.
Particularly in case of the fuser roll for electrophotographic
copying machine, a non-elastic roll coated with a
fluorine-containing resin such as PTFE or PFA (copolymer of
tetrafluoroethylene and perfluoro(alkyl vinyl ether)) has a defect
that the roll has no elasticity, and roll obtained by covering a
surface of elastic roll with a shrinkable fluorine-containing resin
tube is not always satisfactory from the viewpoint of surface
elasticity since the fluorine-containing resin is hard and small in
elongation. Further an elastic roll having a fluorine-containing
resin powder layer on its surface (formed by powder coating of PFA,
etc.) is good in elasticity and releasing property at an initial
stage of its use, but since the fluorine-containing resin powder on
its surface is easily peeled or separated, a life of the releasing
property is short and further in application for a fuser roll in
which its temperature becomes as high as 150.degree. to 200.degree.
C., heat resistance of the roll is not enough. Particularly since
the fluorine-containing rubber component is deteriorated and
strength thereof is decreased, durability of the roll is
lowered.
Also as described in JP-A-1-205188, with respect to the roll having
a silicone rubber layer on a fluorine-containing rubber layer or
fluorosilicone rubber layer, strength of the silicone rubber layer
on the roll surface is insufficient. If an amount of a filler is
increased to increase the strength, releasing property is lowered.
Further since an adhesive strength between the silicone rubber
layer and the fluorine-containing rubber layer or fluorosilicone
rubber layer is not enough, there is a problem that coating of a
silicone oil and fixing operations are carried out repeatedly,
thereby causing cracking on the surface silicone rubber layer and
peeling thereof in the worst case. Further in application for a
fuser roll in which its temperature becomes as high as 150.degree.
to 200.degree. C., the surface silicone rubber layer and the inside
fluorine-containing rubber layer or fluorosilicone rubber layer are
deteriorated and abraded due to lowering of strength since they
have insufficient heat resistance.
Also the elastic roll disclosed in JP-A-62-285839 is very excellent
in releasing property and good in affinity and anti-swelling
property with a silicone oil, but is poor in elastic properties,
particularly elasticity recovering ability. Further that elastic
roll is poor in heat conductivity and has a problem that its
surface temperature is lowered particularly at the time of copying
continuously.
In recent years, in a copying machine, the tendency is toward color
printing and higher copying speed, and thus a surface material for
rolls of fixing part which has flexibility, heat resistance and
abrasion resistance is demanded.
The present invention was completed in view of the mentioned
problems.
Therefore an object of the present invention is to provide a heat
resistant material for OA equipments which has a preferable
flexibility and abrasion resistance and excellent releasing
property, particularly to provide a heat resistant material for
roll or belt of OA equipments.
Another object of the present invention is to provide a heat
resistant material for OA equipments which has less swelling
property with a silicone oil, etc. and has good releasing property
(non-sticking property against toner), paper separating property,
fixing property and color developing property and excellent heat
resistance and durability and to provide a heat resistance material
for roll or belt of OA equipments.
The present inventors have found that a specific
fluorine-containing multi-segment polymer itself having an
elastomeric fluorine-containing polymer chain segment imparting
flexibility to the whole polymer and a non-elastomeric
fluorine-containing polymer chain segment is suitable as a material
for OA equipments which is required to have heat resistance,
flexibility and non-sticking property.
The above-mentioned polymer can be used preferably as a material
for rolls of OA equipments in applications for electronic type
fixing and photosensitive parts. Particularly when used for a fuser
roll, the polymer can impart, to the roll surface, excellent fixing
property, color developing property, oil resistance, non-sticking
property against toner and paper separating property and further
heat resistance, durability and abrasion resistance.
DISCLOSURE OF INVENTION
The heat resistant fluorine-containing material for OA equipments
of the present invention having flexibility comprises a
fluorine-containing multi-segment polymer having an elastomeric
fluorine-containing polymer chain segment A imparting flexibility
to the whole polymer and a non-elastomeric fluorine-containing
polymer chain segment B, in which the fluorine-containing
multi-segment polymer is characterized in that the elastomeric
fluorine-containing polymer chain segment A imparts flexibility to
the whole polymer and comprises not less than 90% by mole of
perhaloolefin unit as a recurring unit.
BEST MODE FOR CARRYING OUT THE INVENTION
Namely in the present invention, it is important that the
fluorine-containing multi-segment polymer contains, in one molecule
thereof, the elastomeric fluorine-containing polymer chain segment
A (hereinafter referred to as "elastomeric segment A") and the
non-elastomeric fluorine-containing polymer chain segment B
(hereinafter referred to as "non-elastomeric segment B") which are
bonded in blocked or grafted form.
In the present invention, for bonding the elastomeric segment A to
the non-elastomeric segment B by blocking or grafting to give the
fluorine-containing multi-segment polymer, various known processes
can be adopted. Among them, a process for preparing a blocked
fluorine-containing multi-segment polymer which is disclosed in
JP-B-58-4728, etc., a process for preparing a grafted
fluorine-containing multi-segment polymer which is disclosed in
JP-A-62-34324, etc., and the like process can be adopted
preferably.
Particularly preferred is the blocked fluorine-containing
multi-segment polymer synthesized through so-called iodine
transferring polymerization method which is disclosed in
JP-B-58-4728 and Kobunshi Ronbunshu (Vol. 49, No. 10, 1992) from
the viewpoint that a segmenting ratio (blocking ratio) is high and
a uniform and regular segmented polymer can be obtained.
On the other hand, in case of a simple mixture of an elastomeric
fluorine-containing polymer and non-elastomeric fluorine-containing
polymer, generally mechanical properties (particularly at high
temperature) becomes insufficient and lowering of abrasion
resistance, flexibility and durability arises though it depends on
kind, miscibility and compatibility of the respective polymers to
be mixed.
On the contrary, by bonding the elastomeric segment A to the
non-elastomeric segment B by blocking or grafting to give the
multi-segment polymer like the present invention, heat resistance,
mechanical properties (particularly at high temperature), etc. are
enhanced, and also in case of use for rolls, heat resistance,
durability and abrasion resistance can be improved more effectively
as compared with the above-mentioned simple mixture of an
elastomeric fluorine-containing polymer and non-elastomeric
fluorine-containing polymer.
Further a rubber roll provided with a layer of fluorine-containing
thermoplastic rubber having an elastomeric fluorine-containing
polymer chain segment containing vinylidene fluoride as a main
component on its outer surface has been proposed (Utility Model
Publication JP-B-2-15873). Though the fluorine-containing segmented
polymer is used for that roll, heat resistance and non-sticking
property are not enough because the elastomeric fluorine-containing
polymer chain segment does not contain a perhaloolefin unit as a
main component.
The present inventors have found that in the iodine transferring
polymerization method, when not less than 90% by mole of
perhaloolefin units are contained as a recurring unit in the
elastomeric segment A, a block copolymerization reaction with
monomer for the non-elastomeric segment B advances regularly and
uniformly and it is possible to largely decrease an amount of
unintended products such as a molecule comprising only an
elastomeric fluorine-containing polymer chain segment which is not
bonded to a non-elastomeric component and a non-elastomeric
fluorine-containing polymer chain segment having a low molecular
weight even if a bonding occurs, and further that molded articles
produced therefrom are useful as a heat resistant material for OA
equipments, particularly a roll or belt for OA equipments. On the
other hand, a material comprising a fluorine-containing
multi-segment polymer containing unintended un-reacted elastomeric
fluorine-containing polymer chain segment, etc. has adverse effect
on parts for OA equipments produced therefrom, such as lowering of
mechanical strength, heat resistance and abrasion resistance.
The elastomer segment A in the fluorine-containing multi-segment
polymer to be used for the heat resistant fluorine-containing
material for OA equipments of the present invention imparts good
flexibility to the material. Particularly in case of use for roll
and belt for OA equipments, it is preferable that an elastic
modulus of the whole fluorine-containing segmented polymer is not
more than 7.times.10.sup.8 dyn/cm.sup.2 at 150.degree. C.,
particularly not more than 5.times.10.sup.8 dyn/cm.sup.2 at
150.degree. C., thereby giving good fixing property and color
developing property even in applications for fuser rolls or belts,
in which the tendency is toward high quality picture and
coloring.
Examples of the usable perhaloolefin as a recurring unit of the
elastomeric segment A are, for instance, tetrafluoroethylene (TFE),
chlorotrifluoroethylene (CTFE), perfluorovinylethers such as
perfluoro(alkyl vinyl ether) (alkyl group has 1 to 5 carbon atoms)
(PAVE) and CF.sub.2.dbd.CFO(CF.sub.2CFYO.sub.
PCF.sub.2CF.sub.2CF.sub.2O.sub.q--R.sub.f wherein Y is F or
CF.sub.3, R.sub.f is a perfluoroalkyl group having 1 to 5 carbon
atoms, p is 0 or an integer of 1 to 5, q is 0 or an integer of 1 to
5, provided that p+q.gtoreq.1, hexafluoropropylene (HFP), and the
like. Among them, those having a combination and composition giving
elastomeric property can be used. Further a monomer giving a curing
site for peroxide crosslinking, polyol crosslinking, polyamine
crosslinking and other curing reaction and a monomer having
functional group for imparting adhesive property, etc. with other
material may be introduced in an amount of not more than 10% by
mole.
In the fluorine-containing multi-segment polymer used in the
present invention, the elastomeric segment A is a segment generally
being non-crystalline and having a glass transition temperature of
not more than 25.degree. C. Examples of preferred composition
thereof are, for instance, 50 to 85/15 to 50/0 to 10% by mole,
particularly 50 to 80/20 to 50/0 to 5% by mole of TFE/PAVE/monomer
giving a curing or adhering function.
Examples of the monomer giving a curing site are, for instance,
vinylidene fluoride, iodine-containing monomers represented by
CX.sub.2.dbd.CX--R.sub.f.sup.3CHRI, in which X is H, F or CH.sub.3,
R.sub.f.sup.3 is a linear or branched fluoro- or perfluoro-alkylene
group or fluoro- or perflouro-oxyalkylene group which may have at
least one ether type oxygen atom, a fluoropolyoxyalkylene group or
a perfluoropolyoxyalkylene group, R is H or CH.sub.3,
CF.sub.2.dbd.CHI, nitrile-containing monomers represented by
##STR00001## in which m is 0 or an integer of 1 to 5, n is an
integer of 1 to 3, ##STR00002## in which n is an integer of 1 to 4,
CF.sub.2.dbd.CFO(CF.sub.2.sub.n--OCF(CF.sub.3)X.sup.4 in which n is
an integer of 2 to 5, ##STR00003## in which n is an integer of 1 to
6,
CF.sub.2.dbd.CF(OCF.sub.2CF(CF.sub.3)).sub.nOCF.sub.2CF(CF.sub.3)X.sup.4
in which n is 1 or 2, or ##STR00004## wherein X.sup.4 is CN, COOH
or COOR.sup.1, in which R.sup.1 is an alkyl group which has 1 to 10
carbon atoms and may contain fluorine atom, bromine-containing
monomers, carboxyl group-containing monomers, alkoxycarbonyl
group-containing monomers, and the like. Usually iodine-containing
monomers, nitrile-containing monomers and carboxyl group-containing
monomers are suitable.
As the iodine-containing monomer, a perfluoro(vinyl ether) compound
is suitable from the viewpoint of copolymerizability thereof. For
example, perfluoro(6,6-dihydro-6-iodo-3-oxa-1-hexene) and
perfluoro(5-iodo-3-oxa-1-pentene) are suitable.
In addition, there is fluorovinylether disclosed in JP-B-5-63482
and represented by the formula:
ICH.sub.2CF.sub.2CF.sub.2(OCFY.sup.3CF.sub.2.sub.n--OCF.dbd.CF.sub.2
in which Y.sup.3 is a trifluoromethyl group, n is 0, 1 or 2.
Examples of the monomer giving good adhesion to other materials,
e.g. metals such as aluminum and stainless steel and organic
materials such as silicone rubber and polyimide, are a
fluorine-containing or non-fluorine-containing monomer having
hydroxyl group, carboxyl group, carboxylic acid derivative,
sulfonic acid, sulfonic acid derivative, epoxy group, acetyl group
or the like.
In order to impart enough flexibility to rolls for OA equipments,
particularly a fuser roll and a soft roll of pressure roll, it is
preferable that a glass transition temperature of the elastomeric
segment A in the fluorine-containing multi-segment polymer of the
present invention is not more than 10.degree. C.
The elastomeric segment A can be prepared by iodine transferring
polymerization method known as a process for preparing a
fluorine-containing rubber (JP-B-58-4728, JP-A-62-12734).
For example, there is a method of carrying out emulsion
polymerization with stirring the above-mentioned perhaloolefin and
if necessary, monomer giving a curing site under pressure in water
medium substantially under oxygen-free condition in the presence of
an iodine compound, preferably a diiodine compound and a radical
polymerization initiator.
Represented examples of diiodine compound to be used are, for
instance, 1-3-diiodoperfluoropropane, 1,4-diiodoperfluorobutane,
1,3-diiodo-2-chloroperfluoropropane,
1,5-diiodo-2,4-dichloroperfluoropentane, 1,6-diiodoperfluorohexane,
1,8-diiodoperfluorooctane, 1,12-diiodoperfluorododecane,
1,16-diiodoperfluorohexadecane, diiodomethane and 1,2-diiodoethane.
Those compounds can be used alone or in a mixture thereof. Among
them, 1,4-diiodoperfluorobutane is preferred. An amount of the
diiodine compound is from 0.01 to 1% by weight on the basis of a
total weight of the elastomeric segment A.
A radical polymerization initiator which is used for preparing the
elastomeric segment A of the present invention may be the same as
that which has been used for polymerization of a
fluorine-containing elastomer. Examples thereof are organic and
inorganic peroxides and azo-compounds. Represented examples of the
initiator are persulfates, carbonate peroxides, peroxide esters,
and the like. Preferred initiator is ammonium persulfate (APS). APS
can be used solely or in combination with a reducing agent such as
sulfites.
Though a wide range of emulsifying agents can be used for emulsion
polymerization, from a point of inhibiting a chain transfer
reaction with molecules of the emulsifying agent which occurs
during the polymerization, carboxylic acid salts having a
fluorocarbon chain or fluoropolyether chain are desirable. An
amount of the emulsifying agent is desirably from about 0.05% by
weight to 2% by weight, particularly desirably from 0.2 to 1.5% by
weight based on added water.
Since the monomer mixture gas used in the present invention is
explosive as described in Advances in Chemistry Series, G. H. Kalb
et al, 129, 13 (1973), it is necessary to take measures for a
polymerization equipment not to cause a sparking. From that point
of view, it is preferable that a polymerization pressure is as low
as possible.
The polymerization pressure can be changed in a wide range,
generally in a range of from 0.5 to 5 MPa. The higher the
polymerization pressure is, the more a polymerization speed
increases. Therefore the polymerization pressure is desirably not
less than 0.8 MPa from the viewpoint of increasing
productivity.
It is preferable that a number average molecular weight of the
so-called elastomeric segment A is from 5,000 to 750,000,
particularly from 20,000 to 400,000 from the viewpoint of imparting
flexibility, elasticity and mechanical properties to the whole
fluorine-containing multi-segment polymer obtained.
An end of the so-obtained elastomeric segment A is of perhalo type
and has an iodine atom which becomes a starting point of block
copolymerization of the non-elastomeric segment B.
In the present invention, the non-elastomeric segment B is
basically not limited if it has a fluorine atom and does not have
the above-mentioned elastomeric property. The non-elastomeric
segment B may be selected according to characteristics and
functions which are intended to be obtained by block-copolymerizing
the non-elastomeric segment B.
Among monomers constituting the non-elastomeric segment B, examples
of a fluorine-containing monomer are, for instance, one or two or
more of perhaloolefins such as TFE, CTFE, PAVE, HFP,
CF.sub.2.dbd.CF(CF.sub.2).sub.pX.sup.3 in which p is an integer of
1 to 10, X.sup.3 is F or Cl, and perfluoro-2-butene; and partly
fluorinated olefins such as vinylidene fluoride (VdF), vinyl
fluoride, trifluoroethylene,
CH.sub.2.dbd.CX.sup.1--CF.sub.2.sub.q--X.sup.2 in which X.sup.1 and
X.sup.2 are H or F, q is an integer of 1 to 10 and
CH.sub.2.dbd.C(CF.sub.3).sub.2. Also one or two or more of monomers
copolymerizable therewith, for example, ethylene, propylene, vinyl
chloride, vinyl ethers, vinyl esters of carboxylic acid and acryls
can be used as copolymerizable components.
Among them, examples of preferred monomer used as a main component
are a single use of fluorine-containing olefin, a combination of
fluorine-containing olefins, a combination of ethylene and TFE and
a combination of ethylene and CTFE from the viewpoint of chemical
resistance and heat resistance. Particularly a single use of
perhaloolefin and a combination of perhaloolefins are
preferred.
Examples thereof are (1) VdF/TFE (0 to 100/100 to 0), particularly
VdF/TFE (70 to 99/30 to 1), PTFE or PVdF; (2) ethylene/TFE/HFP (6
to 43/40 to 81/10 to 30),
3,3,3-trifluoropropylene-1,2-trifluoromethyl-3,3,3-trifluoropropylene-1/P-
AVE (40 to 60/60 to 40); (3) TFE/CF.sub.2.dbd.CF--R.sub.f.sup.1
(amount exhibiting non-elastomeric property, namely less than 15%
by mole of CF.sub.2.dbd.CF--R.sub.f.sup.1, in which R.sub.f.sup.1
is CF.sub.3 or OR.sub.f.sup.2 (R.sub.f.sup.2 is a perfluoroalkyl
group having 1 to 5 carbon atoms); (4) VdF/TFE/CTFE (50 to 99/30 to
0/20 to 1); (5) VdF/TFE/HFP (60 to 99/30 to 0/10 to 1); (6)
ethylene/TFE (30 to 60/70 to 40); (7) polychlorotrifluoroethylene
(PCTFE); (8) ethylene/CTFE (30 to 60/70 to 40); and the like.
When heat resistance and abrasion resistance are required in case
of a material for fuser rolls and belts, it is preferable that a
crystalline melting point of the non-elastomeric segment B is not
less than 150.degree. C. In case of a material for fuser rolls and
belts particularly for high speed copying machine or printer, the
crystalline melting point is particularly preferably not less than
250.degree. C. Particularly from the viewpoint of good heat
resistance, non-sticking property and abrasion resistance, the
non-elastomeric fluorine-containing polymer chain segment having
perhaloolefin as a main recurring unit is preferred.
Further it is particularly preferable that the non-elastomeric
segment B in the fluorine-containing multi-segment polymer of the
present invention is a polymer chain comprising more than 85% by
mole and not more than 100% by mole of tetrafluoroethylene and 0%
by mole or less than 15% by mole of the formula (1) represented by:
CF.sub.2.dbd.CF--R.sub.f.sup.1 wherein R.sub.f.sup.1 is CF.sub.3 or
OR.sub.f.sup.2, in which R.sub.f.sup.2 is a perfluoroalkyl group
having 1 to 5 carbon atoms. The resulting polymer exhibits
excellent characteristics such as heat resistance, abrasion
resistance and non-sticking property against toner in case of use
for rolls for OA equipments and fuser rolls.
An iodine atom at a molecular end of the fluorine-containing
multi-segment polymer of the present invention can be replaced with
another atom or organic group by various methods.
For example, the molecular end of the fluorine-containing
multi-segment polymer of the present invention consisting of
perhaloolefin can be fluorinated and replaced with --CF.sub.3 group
by treating the polymer with fluorine gas.
Thereby non-sticking property, heat resistance, oil resistance and
chemical resistance of the fluorine-containing multi-segment
polymer can be enhanced more.
The treatment with fluorine gas is carried out by bringing the
fluorine-containing multi-segment polymer of the present invention
consisting of perhaloolefin into contact with fluorine gas usually
at 50.degree. to 250.degree. C., preferably at a temperature up to
200.degree. C. for 1 to 10 hours, preferably for 2 to 5 hours. A
treating pressure may be from 1 to 10 kgG/cm.sup.2, usually an
atmospheric pressure. Fluorine gas to be used may be pure fluorine
gas. From the viewpoint of safety, fluorine gas diluted with an
inert gas such as nitrogen gas, helium gas or argon gas to 2 to 25%
by volume, preferably 7 to 15% by volume is preferred.
When brought into contact with fluorine gas, the
fluorine-containing multi-segment polymer may be in any form of
powder, pellet or flake. Further it is possible to carry out the
fluorination treatment after the polymer is formed into a film,
tube or other molded article.
To the non-elastomeric segment B or to the structure of the
fluorine-containing multi-segment polymer of the present invention,
if necessary a carboxyl group or its derivative, hydroxyl group,
sulfonic acid group or its derivative, epoxy group or the like can
be introduced by copolymerization of a monomer having functional
group or by reaction of end group of the segmented polymer, and
thereby adhesion to a substrate, crosslinkability and affinity for
a filler can be enhanced and various other functions can be
imparted.
Block copolymerization of the non-elastomeric segment B can be
carried out subsequently to the emulsion polymerization of the
elastomeric segment A by changing a monomer to one for the
non-elastomeric segment B.
A number average molecular weight of the non-elastomeric segment B
can be adjusted in a wide range of from 1,000 to 1,200,000,
preferably from 3,000 to 600,000. An important feature of the
present invention is to use the fluorine-containing multi-segment
polymer in which the non-elastomeric segment B can be securely
block-copolymerized with the elastomeric segment A and a molecular
weight (degree of polymerization) of the non-elastomeric segment B
can be increased. As mentioned above, this can be achieved by
making the elastomeric segment A have perhaloolefin units of not
less than 90% by mole, particularly not less than 95% by mole as a
recurring unit.
The thus obtained fluorine-containing multi-segment polymer mainly
comprises polymer molecules (B-A-B) in which the non-elastomeric
segments B are bonded to both sides of the elastomeric segment A
and polymer molecules (A-B) in which the non-elastomeric segment B
is bonded to one side of the elastomeric segment A. An amount of
polymer molecules (C) which comprise only the elastomeric segment A
without being bonded to the non-elastomeric segment B is not more
than 20% by weight, preferably not more than 10% by weight based on
a total amount of the segment A and polymer molecule (C) in the
fluorine-containing multi-segment polymer.
If the polymer molecule (C) exists in an amount exceeding 20% by
weight, mechanical properties and abrasion resistance of parts for
OA equipments which are produced therefrom are lowered.
Particularly in case of use for rolls and belts for OA equipments
which are heated to a temperature of as high as not less than
150.degree. C., abrasion resistance particularly at high
temperature is lowered.
A proportion of the elastomeric segment A to the elastomeric
segment B in the fluorine-containing multi-segment polymer is
optionally selected depending on kind of member, roll or belt used
for OA equipments, required characteristics, etc. and also
depending on compositions of each segment. The proportion of the
elastomeric segment A: the elastomeric segment B is selected
preferably in the range of from 5:95 to 98:2 (% by weight).
Particularly in case of use as a material for rolls at a fixing
part which requires flexibility, heat resistance and abrasion
resistance together, the elastomeric segment A: the elastomeric
segment B is preferably 20:80 to 95:5 (% by weight), particularly
preferably 30:70 to 90:10 (% by weight).
In case of use for rolls and belts for OA equipments, if the
proportion of the elastomeric segment A is too small, flexibility
becomes insufficient and fixing property and color developing
property are lowered. Also if the proportion of the elastomeric
segment B is too small, heat resistance, and mechanical properties
and abrasion resistance in case of use at high temperature become
insufficient, which is not preferable.
When a crosslinking point is provided by introducing a curing site
in the elastomeric segment A, vulcanization (crosslinking) can be
carried out by peroxide vulcanization with known organic peroxides,
polyol vulcanization with known polyols, polyamine vulcanization
with known polyvalent amine compounds, and the like.
In addition, the vulcanization can be carried out by triazine
vulcanization, in which a triazine ring is formed with an organotin
compound (for example, JP-A-58-152041), oxazole vulcanization, in
which a nitrile group is introduced as a crosslinking point in a
fluorine-containing elastomer and an oxazole ring is formed with
bisaminophenol (for example, JP-A-59-109546), imidazole
vulcanization, in which an imidazole ring is formed with a
tetraamine compound (for example, JP-A-59-109546), thiazole
vulcanization, in which a thiazole ring is formed with
bisaminothiophenol (for example, JP-A-8-104789), and the like.
To the fluorine-containing multi-segment polymer of the present
invention can be mixed various fillers depending on application and
purpose.
Particularly when the fluorine-containing multi-segment polymer of
the present invention is used as a material for rolls for OA
equipments represented by fuser rolls for copying machine, printer,
etc. and belts for OA equipments, fillers which can impart electric
conductivity to the roll surface are mixed mainly.
Examples of the filler for imparting electric conductivity are
carbon blacks (Ketjen Black, Acetylene Black, etc.); carbons such
as PAN type carbon fiber, pitch type carbon fiber and pulverized
expansive graphite; fluorinated carbons prepared by fluorinating
those carbons completely or partly; metals such as Ag, Ni, Cu,
brass, silver-plated copper, Zn, Al and stainless steel (in the
form of powder, flake, fiber or the like); metal oxides in the form
of fine particles such as SnO.sub.2 (Sb dope), In.sub.2O.sub.3 (Sn
dope) and ZnO (Al dope); ferrites; highly dielectric substances
such as barium titanate; and the like.
An adding amount of the filler being capable of imparting electric
conductivity is optionally selected depending on a desired surface
resistance or volume specific resistance of rolls or belts for OA
equipments and further depending on kind of an electrically
conductive filler to be used. The amount of the filler is from
about 0.1% by weight to about 40% by weight, preferably from 1 to
30% by weight on the basis of the whole composition comprising the
fluorine-containing multi-segment polymer and filler.
Particularly a partly fluorinated carbon is preferred from the
points that the resistance can be controlled stably in a narrow
range of from 10.sup.8 to 10.sup.13 .OMEGA.cm and that electric
conductivity can be given without lowering non-sticking property of
the fluorine-containing polymer.
Examples of the preferred partly fluorinated carbon are those
obtained by fluorinating carbon materials such as carbon black,
carbon fiber, petroleum coke and graphite powder.
Among them, preferred is a fluorinated carbon black obtained by
fluorinating carbon black, particularly a fluorinated carbon black
having a ratio F/C of fluorine atom to carbon atom of not less than
0.1 and less than 1.0, particularly not less than 0.1 and less than
0.5.
If F/C of the fluorinated carbon black is less than 0.1, an effect
of the fluorination is insufficient and problems which a carbon
material before the fluorination has remain unsolved, namely a
problem that a ratio of change in resistance for an adding amount
is very large and controlling of electric conductivity is difficult
and a problem that dispersing of fluorinated carbon becomes
non-uniform due to developed structure and the obtained composition
becomes hard. If F/C is not less than 1.0, a desired electric
conductivity cannot be given to the composition.
In the present invention, F/C is measured as follows. A fluorinated
carbon black is wrapped together with a combustion improver
Na.sub.2O.sub.2 and polyethylene film in a filtrating paper and
then burnt in a tightly closed flask filled with oxygen.
Measurement of the generated hydrogen fluoride is made through
usual method by using a fluoride ion meter (Ion Analyzer 901
available from Orion Co., Ltd.). A fluorine content is calculated
from the measured value. F/C is calculated from the obtained
fluorine content.
The above-mentioned fluorinated carbon black mainly comprises
poly(carbon monofluoride). Preferred is a fluorinated carbon black
obtained by fluorinating carbon black having an average particle
size of from 0.01 to 50 .mu.m, preferably from 0.01 to 1 .mu.m. In
case of a fluorinated carbon black obtained from a carbon material
having an average particle size exceeding 50 .mu.m, for example,
petroleum coke, graphite powder or carbon fiber as a starting
material, an amount thereof has to be increased for imparting
electric conductivity and non-sticking property to a resin and
disadvantages tend to arise, such as an increase in surface
roughness of the obtained composition, lowering of mechanical
strength and non-uniform resistance.
Example of the suitable carbon material for the fluorinated carbon
black is a carbon black having an average particle size mentioned
above. Examples of commercially available carbon black are, for
instance, Furnace Black for rubber (for example, ASAHI #55
available from Asahi Carbon Co., Ltd.), Channel Black for coloring
(for example, LEBEN 7000 available from Columbia Carbon Co., Ltd.),
Thermal Black (SEVACARBON MT-C1 available from Columbia Carbon Co.,
Ltd.), and the like.
Among carbon blacks, those generally called conductive carbon black
are preferred. The conductive carbon black is defined by factors
such as a smaller average particle size (average particle size: not
more than 0.1 .mu.m), a larger surface area (N.sub.2 surface area:
not less than 50 m.sup.2/g), a developed structure (oil absorption:
not less than 100 cc/g), less impurities (ash content: less than
0.1%) and advanced graphitization. The conductive carbon black is
widely used since it can impart conductivity to a material in a
relatively small amount. Examples of the commercially available
conductive carbon black are, for instance, Ketjen Black EC and
Ketjen Black EC-600JD (Ketjen Black International Co., Ltd.), Black
Pearls 2000, Vulcan XC-72 and CSX-99 (Cablack Co., Ltd.), Denka
Black (Denki Kagaku Kogyo Kabushiki Kaisha), Conductex 950
(Columbia Carbon Co., Ltd.), and the like.
The fluorinated carbon black to be used in the present invention
can be obtained by bringing those carbon materials into contact
with fluorine gas at a temperature in the range of from 200.degree.
to 600.degree. C., more preferably from 300.degree. to 500.degree.
C. At a reaction temperature lower than that range, there occur
problems that progressing of fluorination reaction is slow, a
degree of fluorination is difficult to increase, thermal stability
is not enough and characteristics of the fluorinated carbon black
such as non-sticking property and lubricity are not exhibited. On
the contrary, at a reaction temperature higher than that range,
thermal decomposition reaction easily arises and a yield of the
obtained fluorinated carbon black is decreased. Also since there is
a case where a drastic thermal decomposition reaction occurs, which
results in an explosion, full attention should be paid to that.
Fluorine gas to be used in the reaction may be diluted with an
inert gas such as nitrogen, argon, helium or carbon tetrafluoride
or may contain hydrogen fluoride. The reaction can be carried out
under normal pressure, and there is no problem even if the reaction
is made under reduced pressure or under pressure.
Besides the above-mentioned conditions, a reaction time, a fluorine
gas flow, etc. may be optionally selected depending on a reactivity
of a starting carbon material with fluorine and a desired F/C
(fluorine content).
A proportion of the fluorine-containing multi-segment polymer of
the present invention to the above-mentioned fluorinated carbon is
optionally selected depending on a desired resistance. The
proportion is from 1/99 to 20/80 (in weight ratio, hereinafter the
same). If an amount of the fluorinated carbon is decreased, a
sufficient effect of the addition cannot be obtained, and if its
amount is too large, mechanical strength such as tensile strength
tends to be lowered.
Further in order to enhance mechanical properties and compression
restoration property, filler may be mixed. Represented examples of
preferred filler are those in the form of fiber such as glass
fiber, carbon fiber, asbestos fiber, potassium titanate fiber and
the like.
Examples of rolls for OA equipments, to which the
fluorine-containing multi-segment polymer of the present invention
is applied, are as follows.
Roll Example 1
(i) Metallic core roll of aluminum or stainless steel (ii)
Fluorine-containing multi-segment polymer having, as the
Elastomeric segment A, one or two more segments comprising a
polymer chain having a molecular weight of 5,000 to 750,000 and
obtained by copolymerizing 50 to 85% by mole of tetrafluoroethylene
with 15 to 50% by mole of perfluoro(alkyl vinyl ether) and as the
non-elastomeric segment, one or two or more segments comprising a
polymer chain having a molecular weight of 3,000 to 1,200,000 and
obtained by polymerizing more than 85% by mole and not more than
100% by mole of tetrafluoroethylene with 0% by mole or less than
15% by mole of the formula (1): CF.sub.2.dbd.CF--R.sub.f.sup.1 (1)
wherein R.sub.f.sup.1 is CF.sub.3 or --OR.sub.f.sup.2, in which
R.sub.f.sup.2 is a perfluoroalkyl group having 1 to 5 carbon atoms.
Fuser roll or pressure roll at a fixing part which is produced by
laminating the polymer (ii) as an outer layer of the substrate (i).
Roll Example 2 (i) Metallic core roll of aluminum or stainless
steel (ii) Composition prepared by mixing a filler imparting
electric conductivity with the fluorine-containing multi-segment
polymer described in (ii) of Roll Example 1 (outer layer) Fuser
roll or pressure roll at a fixing part which is produced by
laminating the polymer (ii) as an outer layer of the substrate
(i).
The fluorine-containing multi-segment polymer of the present
invention itself has flexibility and therefore even if laminated
directly on the metallic core roll as described in the
above-mentioned Roll Examples 1 and 2, enough flexibility can be
obtained. In addition, by providing an elastic layer of silicone
rubber, fluorine-containing rubber, urethane rubber, EPDM or the
like, the roll can be endowed with more flexibility and effectively
comply with requirements for higher quality picture and paper
feeding property at high speed. Among them, the elastic layers
having a rubber hardness of 10 to 40 degrees or not more than 10
degrees (including a layer in the form of sponge) are selected.
Roll Example 3
(i) Metallic core roll of aluminum or stainless steel (ii) Silicone
rubber (iii) Fluorine-containing multi-segment polymer described in
(ii) of Roll Example 1 (outer layer) Fuser roll or pressure roll at
a fixing part which is produced by laminating the silicone rubber
layer (ii) on the substrate (i) and thereon the polymer layer (iii)
as an outermost layer. Roll Example 4 (i) Metallic core roll of
aluminum or stainless steel (ii) Silicone rubber (iii) Composition
prepared by mixing a filler imparting electric conductivity with
the fluorine-containing multi-segment polymer described in (ii) of
Roll Example 1 (outer layer) Fuser roll or pressure roll at a
fixing part which is produced by laminating the silicone rubber
layer (ii) on the substrate (i) and thereon the polymer layer (iii)
as an outermost layer.
Between each layer of each layered rolls of the above-mentioned
Roll Examples 1 to 4, an adhesive or primer may be used to improve
adhesion thereof.
Preferred are Roll Examples 3 and 4. Usually any one of the fuser
roll or pressure roll of the fixing part or the both of them are
provided with a heating device such as a ceramic heater to soften
or melt a toner for fixing an image to a paper. The material for OA
equipments of the present invention has enough heat resistance
against such a heating device.
The fluorine-containing multi-segment polymer used for the material
for OA equipments of the present invention is used as a molding
material which can be molded into the form of sheet, film or tube
and thus is applied to the roll or belt for OA equipments. In that
case, known molding methods can be used. The fluorine-containing
multi-segment polymer or the composition prepared by blending a
filler to the fluorine-containing multi-segment polymer can be
molded into necessary forms by extrusion molding, injection
molding, compression molding or the like.
Further the fluorine-containing multi-segment polymer used for the
material for OA equipments of the present invention can be used as
a coating material when prepared into a composition containing a
liquid carrier or into a powder form having a specific particle
size and apparent density. The coating material can be used not
only for application in OA equipments but also for a lining
material, roll, belt, hose, sealing material, and the like in the
fields of transportation such as automobiles, semiconductor
production facilities, chemical plant, aircraft, food processing
facilities, photographic and printing facilities, coating
apparatuses, steel making facilities, etc. The coating material of
the present invention comprises the fluorine-containing
multi-segment polymer. As the fluorine-containing multi-segement
polymer, those described above in the heat resistant material for
OA equipments having flexibility can be preferably used similarly.
The coating material is applied to the rolls and belts for OA
equipments and substrates in other applications and a coating film
having excellent flexibility, sealing property, heat resistance,
abrasion resistance and non-sticking property can be obtained.
Further the present invention relates to the coating powder
comprising the above-mentioned fluorine-containing multi-segment
polymer.
For the coating powder of the present invention, the same material
as the above-mentioned heat resistant material for OA equipments
having flexibility can be preferably used.
The coating powder of the present invention which is used
preferably is in the form of powder or particle having a particle
size of from 10 to 1,000 .mu.m and an apparent density of from 0.3
to 1.2 g/cc.
To the coating powder of the present invention can be added
optionally additives, for example, a pigment such as a carbon
powder, titanium oxide or cobalt oxide; a reinforcing material such
as a glass fiber powder, carbon fiber powder or mica; an amine type
anti-oxidant, organic sulfuric compound, organotin type
anti-oxidant, phenolic anti-oxidant or a thermal stabilizer such as
metal soap; a leveling agent; an anti-static agent; the same filler
as mentioned above which is capable of imparting electric
conductivity; and the like in the range not lowering remarkably
characteristics of a fluorine-containing resin such as heat
resistance.
Mixing of the fluorine-containing coating powder of the present
invention with the above-mentioned additives may be carried out in
the form of powder (dry type) or in the form of slurry (wet type).
Preferred is the mixing in the form of powder. Examples of the
usable mixing equipment are, for instance, usual mixers such as
sand mill, V-type blender and ribbon type blender and pulverizing
machine.
The fluorine-containing coating powder of the present invention is
coated through electrostatic coating, fluid bed dipping, rotary
lining or the like and then baked (preferably at a temperature of
not less than a crystalline melting point thereof) to form a good
coating film.
Generally it is possible to form a coating film of from 10 to 200
.mu.m thick in case of the electrostatic powder coating and from
200 to 1,000 .mu.m thick in case of the rotary lining.
The present invention further relates to the coating composition
comprising the fluorine-containing multi-segment polymer of the
present invention and a liquid medium.
For the coating composition of the present invention, the same
fluorine-containing multi-segment polymers as those for the
above-mentioned heat resistant material for OA equipments having
flexibility can be preferably used.
The liquid carrier to be used for the coating composition of the
present invention is selected from liquids which can dissolve or
disperse the fluorine-containing multi-segment polymer to be used
in the present invention. Examples thereof are alcohols such as
methanol, ethanol, propanol and butanol and in addition,
hydrocarbon type solvents such as acetone, methyl ethyl ketone,
ethyl acetate, dimethylformamide, dimethylacetamide,
N-methyl-2-pyrrolidone, dimethylsulfoxide, triethylphosphate,
tetrahydrofuran, methyl isobutyl ketone, cyclohexanone,
1,4-dioxane, methyl cellosolve acetate, 2-nitropropane, methyl
isoamyl ketone, 4-methoxy-4-methylpentanone-2 and
4-methoxy-4-methylpentanol-2; haloalkanes such as
trichlorotrifluoroethane, dichlorotetrafluoroethane,
dichlorodifluoroethane, chlorodifluoroethane,
dichloropentafluoropropane, tetrachlorohexafluorobutane and
perfluorohexane; fluorine-containing solvents such as
fluorine-containing ethers, i.e. FLORINATE FC-75 (available from
Three M Co., Ltd.), FLORINATE FC-77 (available from Three M Co.,
Ltd.) and HFE7100 (available from Three M Co., Ltd.); water; and a
mixture of two or more thereof.
Also it is possible to blend usual additives such as a pigment,
surfactant, anti-foaming agent, viscosity control agent and
leveling agent in the range not lowering remarkably heat
resistance, chemical resistance, non-sticking property and abrasion
resistance.
Besides the additives, a coupling agent can be used as another
component to enhance adhesive property.
The coupling agent in the present invention means a compound which
acts on an interface between the organic material and the inorganic
material and forms a strong bridge between the both materials
through chemical or physical coupling. The coupling agent is
usually a compound of silicone, titanium, zirconium, hafnium,
trium, tin, aluminum or magnesium which has a group being capable
of coupling the organic material and the inorganic material. Among
those coupling agents, preferred are a silane coupling agent,
ortho-acid esters of transition elements (for example, titanium or
zirconium) of the group IV in Periodic Table and derivatives
thereof, and particularly preferred is an amino silane
compound.
The coating composition of the present invention can be in the form
of aqueous dispersion, organic solvent dispersion, organosol or
aqueous emulsion of organosol containing the fluorine-containing
multi-segment polymer and if necessary, the above-mentioned
additives. Among them, the form of aqueous dispersion for a coating
is preferred from environmental and safety point of view.
Particularly preferred is the composition in the state of the
fluorine-containing multi-segment polymer being dispersed in water
in the form of fine particles of from 0.01 to 1.0 .mu.m, in which a
surfactant is generally blended for stabilizing the dispersion.
The aqueous dispersion for a coating of the present invention can
be prepared through various processes. Concretely there are, for
example, a process for finely pulverizing a powder of
fluorine-containing multi-segment polymer obtained by suspension
polymerization, or the like and then dispersing the finely
pulverized powder uniformly in an aqueous medium with a surfactant,
a process for preparing an aqueous dispersion of
fluorine-containing multi-segment polymer at the same time of
polymerization by emulsion polymerization and if necessary, adding
a surfactant and additives, and the like process. From the
viewpoint of productivity and quality (for forming into smaller and
uniform particle size), the process for preparing the aqueous
dispersion directly through the emulsion polymerization is
preferred.
A method of application of the coating composition of the present
invention is optionally selected depending on kind of the
fluorine-containing multi-segment polymer, form of a coating,
purpose and application. For example, in case of the aqueous
dispersion and organic solvent dispersion, usually spray coating,
brush coating, roll coating and spin coating are carried out. After
the coating, drying and sintering are carried out to give a coating
film on a substrate. The sintering conditions are optionally
selected depending on kind (composition, melting point, etc.) of
the fluorine-containing multi-segment polymer. Generally the baking
is carried out at a temperature of not less than a melting point of
the non-elastomeric segment B in the fluorine-containing
multi-segment polymer. The baking time is from five minutes to
three hours, preferably from about 10 minutes to about 30 minutes
while it varies depending on the sintering temperature.
The coating material of the present invention comprising the
fluorine-containing multi-segment polymer is coated on a metallic
core roll (aluminum and SUS) of a roll as a heat resistant material
for OA equipments having flexibility or on an elastic layer of
silicone rubber, fluorine-containing rubber, urethane rubber or
EPDM provided on the roll, and thus a fuser roll or pressure roll
having not only flexibility, heat resistance and abrasion
resistance but also non-sticking property and oil resistance can be
obtained.
In order to obtain the above-mentioned rolls for OA equipments by
applying the coating material of the present invention, after
applying, if necessary, a primer to the metallic core roll or
intermediate elastic layer and then sintering depending on
necessity, it is possible to coat any of the aqueous dispersion
coating, solvent-soluble coating, solvent-dispersion coating or
powder coating which comprises the coating material of the present
invention and then bake at a temperature of not less than a melting
point thereof to form a coating film. A thickness of the coating
film varies depending on purpose, application and hardiness of a
substrate, and is selected in the range of from 1 to 500 .mu.m,
preferably from 5 to 150 .mu.m, particularly from 5 to 100 .mu.m.
If necessary, the coating film may be ground to make its surface
smooth. It is preferable to adjust a surface roughness (Ra) to not
more than 1.0 .mu.m, more preferably not more than 0.5 .mu.m.
Further the coating material of the present invention can be used
in various applications other than the application for OA
equipments, by making use of its heat resistance, chemical
resistance, non-sticking property, flexibility, sealing property
and abrasion resistance. Examples of the application are shown in
Tables 1, 2 and 3.
The tube of the present invention is a cylindrical article obtained
by molding the fluorine-containing multi-segment polymer into a
tubular form. The above-exemplified preferred fluorine-containing
multi-segment polymers can be preferably used similarly.
A size of the tube varies depending on purpose, application and
conditions in use and is not limited. Usually its inner diameter is
from about 5 mm to about 50 mm and its thickness is not more than 1
mm. Particularly in case of rolls for OA equipments such as fuser
rolls and pressure rolls, it is preferable that the inner diameter
is from 10 to 40 mm and the thickness is from 0.01 to 0.15
.mu.m.
The tube of the present invention is formed into a tube by usual
melt-extrusion. The tube may be stretched (single screw or two
screws) if necessary and may have thermal shrinkability, but
usually may have neither stretchability nor thermal
shrinkability.
The tube of the present invention may contain the above-mentioned
filler imparting electric conductivity if necessary. The tube can
be produced usually by mixing previously an electric
conductivity-imparting agent by kneading or dry blending to the
starting material (in the form of pellet or powder) before molding
into a tube by melt-extrusion.
The molding method is also not limited particularly. Generally melt
extrusion molding with a ring die is carried out as mentioned
above. Namely, a cylindrical film melt-extruded through a ring die
with a single screw or multi-screw extruder is taken off while
being cooled as it is with a proper cooling means or is taken off
while adjusting its size and shape toward inside or outside by
using a sizing jig after the ring die and cooling at normal
temperature or with a coolant such as air or water. In that case,
there is no restriction in employing such conditions as feeding of
air into the cylindrical article, stretching somewhat at the time
of taking off and carrying out slow cooling or rapid cooling.
The tube usually comprises one layer, and may comprise two or more
layers. In such a case, it is necessary to study enough and select
compatibility between polymers of each layer and a heating
temperature under specific conditions mentioned below. This is
because a heat treating temperature of each layer differs from each
other. Molding is carried out by co-extrusion method, and there are
no specific conditions like the molding of one layer.
The tube of the present invention is optionally subjected to inner
surface treatment, if necessary, in order to enhance adhesion to an
article to be covered with the tube. Example of the preferred inner
surface treatment is chemical etching treatment, and for example,
sodium-based etching agent is used preferably. In addition to the
chemical etching, any of inner surface treatments may be employed
as far as enhancement of adhesion can be expected. Further after
the chemical etching of the inner surface, a primer may be applied
to enhance adhesion to a substrate more.
The tube of the present invention is used for rolls (particularly
for fuser roll and pressure roll) for OA equipments and can impart
excellent flexibility and heat resistance to the rolls. In addition
to those characteristics, good non-sticking property can be given
by fitting the tube of the present invention on an outermost
surface of the roll.
The roll provided with the tube of the present invention may be
produced as mentioned above by covering its metallic core roll
directly with the tube or by providing an elastic layer of silicone
rubber, fluorine-containing rubber, urethane rubber or EPDM between
the metallic core roll and the tube.
While the tube of the present invention can impart enough
flexibility to the roll surface even if covered directly on the
metallic core roll, more flexibility can be given to the roll
surface by providing the elastic layer between the roll and the
tube, and in case of use as a fuser roll and pressure roll for OA
equipments, a higher quality picture and enhanced paper feeding
property at high speed can be attained. In that case, an elastic
layer having a rubber hardness of from about 10 degrees to about 30
degrees or an elastic layer having a rubber hardness of not more
than 10 degrees (including a layer in the form of sponge) is
preferred.
If necessary, an adhesive is used or treatment with a primer is
carried out to impart adhesion between the tube of the present
invention and the substrate (metallic core roll or elastic layer)
contacting thereto. In that case, it is preferable to use the
above-mentioned tube subjected to the inner surface treatment by
etching from the point that a stronger adhesion can be
obtained.
In producing the roll by providing the tube of the present
invention directly on the metallic core roll, known methods can be
optionally employed. It is preferable that a tube having thermal
shrinkability and subjected to etching treatment of its inner
surface is covered on a metallic core roll subjected to primer
treatment and is shrank at a temperature of not more than a melting
point (for example, at 150.degree. to 200.degree. C.) for setting
to the substrate, followed by sintering at a temperature of not
less than the melting point (for example, at 320.degree. to
400.degree. C.) to bond by fusion.
The roll having an elastic layer between the tube of the present
invention and the metallic core roll can be produced by a method of
firstly putting the metallic core roll and the tube of the present
invention in a cylindrical molded article so that a space is
provided between the roll and the tube and the inner surface of the
cylindrical molded article comes into contact with the outer
surface of the tube, and then pouring a raw rubber, latex or
elastomer into the above-mentioned space, and if necessary carrying
out vulcanizing. It is a matter of course that the roll covered
with the tube has to be taken out of the cylindrical molded article
at a necessary time. In that case, the inner surface of the tube
may be subjected previously to etching treatment or primer
treatment so that it is easily contacted to the rubber portion.
Also the roll may be produced by previously making a rubber roll
and then covering the tube of the present invention on the surface
of the rubber roll. In that case, it is better to use a tube having
thermal shrinkability. Thus there is no restriction in the
production method of the roll.
When the roll obtained above is used as rolls for OA equipments
such as a fuser roll and pressure roll, a step for making the
surface of roll smooth may be carried out as case demands.
For example, a surface roughness (Ra) of the roll can be decreased
by grinding the roll surface. Preferred Ra is not more than 1
.mu.m, more preferably not more than 0.5 .mu.m.
TABLE-US-00001 TABLE 1 Fields of industry Final product Application
Parts Electrical Semiconductor Semiconductor CVD device O-ring
(square), production Dry etching packing, sealing apparatus device
material, tube, Liquid crystal Wet etching roll, coating, panel
production device lining, gasket, apparatus Oxidation/diffu-
diaphragm, hose Plasma panel pro- sion device duction apparatus
Sputtering device Ashing device Cleaning device Ion implantation
device Transportation means Automobile Automobile Engine and pe-
Gasket, shaft seal, ripheral parts valve stem seal, sealing
material, hose AT device Hose, sealing material Fuel line and pe-
O-ring (square), ripheral parts tube, packing, core material of
valve, hose, sealing material, diaphragm Aircraft Aircraft Fuel
line Diaphragm, O-ring (square), valve, tube, packing, hose,
sealing material Rocket Rocket Fuel line same as above Ship Ship
Fuel line same as above Chemical Chemicals Plant Processes for pro-
Lining, valve, ducing chemicals packing, roll, such as pharma-
hose, diaphragm, ceutical, agri- O-ring (square), culture chemical,
tube, sealing paint and resin, material (Petroleum) Pharmaceutical
Medicines Plug for Plug for chemicals chemicals Machinery
Photograph Developer Film developing Roll machine X-ray film devel-
Roll oping machine Printing Printing machine Printing roll Roll
Painting Painting facilities Coating roll Roll Physical and Tube
chemical appliances for analysis Foods Plant Foods processing
Lining, valve, process packing, roll, hose, diaphragm, O-ring
(square), tube, sealing material Metal Steel making Steel plate
Steel plate Roll processing processing roll facilities
TABLE-US-00002 TABLE 2 Field of industry Needed characteristics
Electrical Plasma resistance, acid resistance, alkali resistance,
amino resistance, ozone resistance, gas resistance, chemical
resistance, cleanliness, heat resistance Transportation Heat
resistance, amino resistance means Heat resistance, amino
resistance Fuel resistance, fuel permeability, heat resistance Fuel
resistance, fuel permeability, heat resistance Fuel resistance,
fuel permeability, heat resistance Fuel resistance, fuel
permeability, heat resistance Chemical Chemical resistance, solvent
resistance, heat resistance Chemical resistance, solvent
resistance, heat resistance Cleanliness Machinery Chemical
resistance Chemical resistance Solvent resistance Solvent
resistance Foods Chemical resistance, solvent resistance, heat
resistance Metal Heat resistance, acid resistance
TABLE-US-00003 TABLE 3 Field of industry Parts Electrical O-ring
and sealing material for gate valve of corresponding product O-ring
and sealing material for quartz window of corresponding product
O-ring and sealing material for chamber of corresponding product
O-ring and sealing material for gate of corresponding product
O-ring and sealing material for bell jar of corresponding product
O-ring and sealing material for coupling of corresponding product
O-ring and sealing material for pump of corresponding product
O-ring and sealing material for gas control device for
semiconductor of corresponding product O-ring and sealing material
for resist developing solution and peeling solution O-ring and
sealing material for wafer cleaning solution Diaphragm for pump of
corresponding product Hose for resist developing solution and
peeling solution Hose and tube for wafer cleaning solution Roll for
transferring wafer Lining and coating for resist developing
solution tank and peeling solution tank Lining and coating for
wafer cleaning solution tank Lining and coating for wet etching
tank Transportation Engine head gasket means Metal gasket Crank
shaft seal Cam shaft seal Valve stem seal Manifold packing Oil hose
ATF hose Injector O-ring Injector packing O-ring and diaphragm for
fuel pump Fuel hose Chemical Machinery Developing roll Developing
roll Gravure roll Guide roll Gravure roll for coating line in
production of magnetic tape Guide roll for coating line in
production of magnetic tape Various coating rolls Foods Metal
The present invention is then explained based on examples but is
not limited to those examples.
PREPARATION EXAMPLE 1
(Synthesis of Elastomeric Segment A)
A 47-liter stainless steel autoclave having no ignition source was
charged with 30 liters of pure water, 300 g of
C.sub.7F.sub.15COONH.sub.4 as an emulsifying agent and 300 g of
disodium hydrogenophosphate.12H.sub.2O as a pH control agent, and
after replacing the inside of a system with nitrogen gas
sufficiently, the autoclave was heated up to 50.degree. C. with
stirring at 200 rpm and a gas mixture of TFE and perfluoro (methyl
vinyl ether) (PMVE) (32/68 in mole ratio) was introduced so that
the inside pressure became 8.0 kgf/cm.sup.2G. Then 100 ml of an
aqueous solution of ammonium persulfate (APS) having a
concentration of 55.8 mg/ml was fed with pressurized nitrogen to
initiate a reaction.
At the time when the inside pressure lowered down to 7.0
kgf/cm.sup.2G with advance of polymerization, 27.24 g of diiodine
compound I(CF.sub.2).sub.4I and 234 g of aqueous solution of 10% by
weight of C.sub.7F.sub.15COONH.sub.4 were introduced with
pressurized nitrogen. Then 60 g of TFE was fed with self-pressure
thereof and 58 g of PMVE was fed under pressure with a plunger pump
(TFE/PMVE=63/37 in mole ratio) so that the pressure became 8.0
kgf/cm.sup.2G. Thereafter TFE and PMVE were fed in the same manner
under pressure with advance of the reaction, and thus increasing
and lowering of the pressure were repeated between 7 kgf/cm.sup.2G
and 8 kgf/cm.sup.2G.
Twelve hours after starting of the polymerization reaction, when a
total charging amount of TFE and PMVE reached 6,000 g, the
autoclave was cooled and un-reacted monomer was released to give an
aqueous dispersion having a solid content of 18.04% by weight.
A part of the aqueous dispersion was sampled, frozen, coagulated
and thawed, followed by washing a coagulated product with water and
then vacuum-drying to give a rubber-like polymer. A Mooney
viscosity ML.sub.1+10 (100.degree. C.) of the polymer was 94. An
intrinsic viscosity ".eta." was 0.654 (dl/g, 35.degree. C., FC-75
(available from Three-M Co., Ltd.)).
As a result of .sup.19F-NMR analysis, monomer components of the
polymer were TFE/PMVE=60/40% by mole, and Tg (center value)
measured according to DSC analysis was 2.degree. C.
PREPARATION EXAMPLE 2
(Synthesis of Elastomeric Segment A)
A 47-liter stainless steel autoclave having no ignition source was
charged with 30 liters of pure water, 300 g of
C.sub.7F.sub.15COONH.sub.4 as an emulsifying agent and 300 g of
disodium hydrogenophosphate.12H.sub.2O as a pH control agent, and
after replacing the inside of a system with nitrogen gas
sufficiently, the autoclave was heated up to 50.degree. C. with
stirring at 200 rpm and a gas mixture of TFE/PMVE (32/68 in mole
ratio) was introduced so that the inside pressure became 8.0
kgf/cm.sup.2G. Then 100 ml of an aqueous solution of ammonium
persulfate (APS) having a concentration of 27.9 mg/ml was fed with
pressurized nitrogen to initiate a reaction.
At the time when the inside pressure lowered down to 7.0
kgf/cm.sup.2G with advance of polymerization, 13.62 g of diiodine
compound I(CF.sub.2).sub.4I and 117 g of aqueous solution of 10% by
weight of C.sub.7F.sub.15COONH.sub.4 were introduced with
pressurized nitrogen. Then 60 g of TFE was fed with self-pressure
thereof and 58 g of PMVE was fed under pressure with a plunger pump
(TFE/PMVE=63/37 in mole ratio) so that the pressure became 8.0
kgf/cm.sup.2G. Thereafter TFE and PMVE were fed in the same manner
under pressure with advance of the reaction, and thus increasing
and lowering of the pressure were repeated between 7 kgf/cm.sup.2G
and 8 kgf/cm.sup.2G.
Sixteen hours after starting of the polymerization reaction, when a
total charging amount of TFE and PMVE reached 6,000 g, the
autoclave was cooled and un-reacted monomer was released to give an
aqueous dispersion having a solid content of 18.16% by weight.
A part of the aqueous dispersion was sampled, frozen, coagulated
and thawed, followed by washing a coagulated product with water and
then vacuum-drying to give a rubber-like polymer. A Mooney
viscosity ML.sub.1+10 (100.degree. C.) of the polymer could not be
measured because the polymer did not melt. An intrinsic viscosity
".eta." was 1.387 (dl/g, 35.degree. C., FC-75 (available from
Sumitomo Three-M Co., Ltd.)).
As a result of .sup.19F-NMR analysis, monomer components of the
polymer were TFE/PMVE=60/40% by mole, and Tg (center value)
measured according to DSC analysis was 2.degree. C.
PREPARATION EXAMPLE 3
(Synthesis of Elastomeric Segment A)
A 47-liter stainless steel autoclave having no ignition source was
charged with 30 liters of pure water, 300 g of
C.sub.7F.sub.15COONH.sub.4 as an emulsifying agent and 2.7 g of
disodium hydrogenophosphate.12H.sub.2O as a pH control agent, and
after replacing the inside of a system with nitrogen gas
sufficiently, the autoclave was heated up to 50.degree. C. with
stirring at 200 rpm and a gas mixture of TFE/PMVE (32/68 in mole
ratio) was introduced so that the inside pressure became 8.5
kgf/cm.sup.2G. Then 100 ml of an aqueous solution of ammonium
persulfate (APS) having a concentration of 87.35 mg/ml was fed with
pressurized nitrogen to initiate a reaction.
At the time when the inside pressure lowered down to 7.5
kgf/cm.sup.2G with advance of polymerization, 61.59 g of diiodine
compound I(CF.sub.2).sub.4I, 100.4 g of
CF.sub.2.dbd.CFOCF.sub.2CF.sub.2CH.sub.2I and 1,392 g of aqueous
solution of 10% by weight of C.sub.7F.sub.15COONH.sub.4 were
introduced with pressurized nitrogen. Then 60 g of TFE was fed with
self-pressure thereof and 66.4 g of PMVE was fed under pressure
with a plunger pump (TFE/PMVE=60/40 in mole ratio) so that the
pressure became 8.5 kgf/cm.sup.2G. Thereafter TFE and PMVE were fed
in the same manner under pressure with advance of the reaction, and
thus increasing and lowering of the pressure were repeated between
7.5 kgf/cm.sup.2G and 8.5 kgf/cm.sup.2G.
Sixty-nine hours after starting of the polymerization reaction,
when a total charging amount of TFE and PMVE reached 14 kg, the
autoclave was cooled and un-reacted monomer was released to give an
aqueous dispersion having a solid content of 30% by weight.
A part of the aqueous dispersion was sampled, frozen, coagulated
and thawed, followed by washing a coagulated product with water and
then vacuum-drying to give a rubber-like polymer. A Mooney
viscosity ML.sub.1+10 (100.degree. C.) of the polymer was 68.
As a result of .sup.19F-NMR analysis, monomer components of the
polymer were TFE/PMVE=60/40% by mole, and Tg (center value)
measured according to DSC analysis was -4.degree. C.
PREPARATION EXAMPLE 4
(Synthesis of Elastomeric Segment A)
A 100-liter stainless steel autoclave having no ignition source was
charged with 60 liters of pure water, 600 g of
C.sub.7F.sub.15COONH.sub.4 as an emulsifying agent and 600 g of
disodium hydrogenophosphate.12H.sub.2O as a pH control agent, and
after replacing the inside of a system with nitrogen gas
sufficiently, the autoclave was heated up to 50.degree. C. with
stirring at 120 rpm and a gas mixture of TFE/perfluoro (methyl
vinyl ether) (PMVE) (25/75 in mole ratio) was introduced so that
the inside pressure became 8.0 kgf/cm.sup.2G. Then 100 ml of an
aqueous solution of ammonium persulfate (APS) having a
concentration of 55.8 mg/ml (APS: 5.58 g) was fed with pressurized
nitrogen to initiate a reaction.
At the time when the inside pressure lowered down to 7.0
kgf/cm.sup.2G with advance of polymerization, an aqueous solution
prepared by emulsifying 27.3 g of diiodine compound
I(CF.sub.2).sub.4I with 90 g of aqueous solution of 10% by weight
of C.sub.7F.sub.15COONH.sub.4 was introduced with pressurized
nitrogen. Then 120 g of TFE was fed with self-pressure thereof and
116 g of PMVE was fed under pressure with a plunger pump
(TFE/PMVE=63/37 in mole ratio) so that the pressure became 8.0
kgf/cm.sup.2G. Thereafter TFE and PMVE were fed in the same manner
under pressure with advance of the reaction, and thus increasing
and lowering of the pressure were repeated between 7 kgf/cm.sup.2G
and 8 kgf/cm.sup.2G.
At the time when a total charging amount of TFE and PMVE reached 12
kg after starting of the polymerization reaction, the autoclave was
cooled and un-reacted monomer was released to give 73.6 kg of an
aqueous dispersion having a solid content of 16.0% by weight.
A part of the aqueous dispersion was sampled, frozen, coagulated
and thawed, followed by washing a coagulated product with water and
then vacuum-drying to give a rubber-like polymer. A Mooney
viscosity ML.sub.1+10 (140.degree. C.) of the polymer was 80.
As a result of .sup.19F-NMR analysis, monomer components of the
polymer were TFE/PMVE=64/36% by mole, and Tg (center value)
measured according to DSC analysis was 3.degree. C.
EXAMPLE 1
(Block Copolymerization with Non-elastomeric Segment B)
A 3-liter stainless steel autoclave was charged with 1,096 g of the
aqueous dispersion obtained in Preparation Example 1 and 4.15 g of
perfluoro(propyl vinyl ether) (PPVE). After replacing the inside of
a system with nitrogen gas sufficiently, the inside temperature was
kept at 80.degree. C. With stirring at 400 rpm, tetrafluoroethylene
was introduced under pressure so that the inside pressure became
8.0 kgf/cm.sup.2G.
Then a solution prepared by dissolving 10 mg of ammonium persulfate
in 2 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, at the time when it lowered to 7.0
kgf/cm.sup.2G, it was again raised with a tetrafluoroethylene gas
up to 8.0 kgf/cm.sup.2G, and thus increasing and lowering of the
pressure were repeated.
At the time when 29.6 g of tetrafluoroethylene was consumed after
starting of polymerization, supplying thereof was stopped, the
autoclave was cooled and un-reacted monomer was released to give
1,132 g of a semi-transparent aqueous dispersion.
A polymer content of the obtained aqueous dispersion was 19.6% by
weight, and a particle size thereof measured by dynamic light
scattering method was 55.3 nm.
A proportion of the non-elastomeric fluorine-containing polymer
chain segment to the whole polymer which was calculated from an
increase in yield of polymer, namely ((Yield of polymer obtained in
post polymerization)-(Amount of polymer charged))+(Yield of polymer
obtained in post polymerization).times.100 was 16.2% by weight.
The obtained aqueous dispersion was frozen and coagulated, and the
precipitated polymer was washed and dried to give a white
solid.
According to .sup.19F-NMR analysis, components of the
non-elastomeric fluorine-containing polymer chain segment in the
obtained fluorine-containing multi-segment polymer was
TFE/PPVE=99.5/0.5% by mole. Also according to DSC analysis, a glass
transition temperature of the elastomeric fluorine-containing
polymer chain was 2.degree. C. and a crystalline melting point of
the non-elastomeric fluorine-containing polymer chain segment was
324.degree. C. A melt flow rate measured under conditions of
preheating at 372.degree. C. for five minutes at a load of 7
kgf/cm.sup.2 by using Koka-type flow tester and nozzles of 2 mm
diameter.times.8 mm length was 43 g/10 min.
EXAMPLE 2
(Block Copolymerization with Non-elastomeric Segment B)
A 3-liter stainless steel autoclave was charged with 993.7 g of the
aqueous dispersion obtained in Preparation Example 2 and 10.3 g of
perfluoro(propyl vinyl ether) (PPVE). After replacing the inside of
a system with nitrogen gas sufficiently, the inside temperature was
kept at 80.degree. C. With stirring at 400 rpm, tetrafluoroethylene
was introduced under pressure so that the inside pressure became
8.0 kgf/cm.sup.2G.
Then a solution prepared by dissolving 10 mg of ammonium persulfate
in 2 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, at the time when it lowered to 7.0
kgf/cm.sup.2G, it was again raised with tetrafluoroethylene gas up
to 8.0 kgf/cm.sup.2G, and thus increasing and lowering of the
pressure were repeated.
At the time when 57.0 g of tetrafluoroethylene was consumed after
starting of polymerization, supplying thereof was stopped, the
autoclave was cooled and un-reacted monomer was released to give
1,200 g of a semi-transparent aqueous dispersion.
A polymer content of the obtained aqueous dispersion was 20.0% by
weight, and a particle size thereof measured by dynamic light
scattering method was 53.4 nm.
A proportion of the non-elastomeric fluorine-containing polymer
chain segment to the whole polymer which was calculated from an
increase in yield of polymer, namely ((Yield of polymer obtained in
post polymerization)-(Amount of polymer charged))+(Yield of polymer
obtained in post polymerization).times.100 was 24.8% by weight.
The obtained aqueous dispersion was frozen and coagulated, and the
precipitated polymer was washed and dried to give a white
solid.
According to .sup.19F-NMR analysis, components of the
non-elastomeric fluorine-containing polymer chain segment in the
obtained fluorine-containing multi-segment polymer was
TFE/PPVE=98.9/1.1% by mole. Also according to DSC analysis, a glass
transition temperature of the elastomeric fluorine-containing
polymer chain was 2.degree. C. and a crystalline melting point of
the non-elastomeric fluorine-containing polymer chain segment was
310.degree. C. A melt flow rate was 8 g/10 min (at 372.degree. C.,
at a load of 5kgf/cm.sup.2).
EXAMPLE 3
(Block Copolymerization with Non-elastomeric Segment B)
A 3-liter stainless steel autoclave was charged with 694 g of the
aqueous dispersion obtained in Preparation Example 1, 368 g of pure
water and 17.5 g of perfluoro(propyl vinyl ether) (PPVE). After
replacing the inside of a system with nitrogen gas sufficiently,
the inside temperature was kept at 80.degree. C. With stirring at
400 rpm, tetrafluoroethylene was introduced under pressure so that
the inside pressure became 8.0 kgf/cm.sup.2G.
Then a solution prepared by dissolving 10 mg of ammonium persulfate
in 2 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, at the time when it lowered to 7.0
kgf/cm.sup.2G, it was again raised with tetrafluoroethylene gas up
to 8.0 kgf/cm.sup.2G, and thus increasing and lowering of the
pressure were repeated.
At the time when 125 g of tetrafluoroethylene was consumed after
starting of polymerization, supplying thereof was stopped, the
autoclave was cooled and un-reacted monomer was released to give
1,205 g of a semi-transparent aqueous dispersion.
A polymer content of the obtained aqueous dispersion was 21.3% by
weight, and a particle size thereof measured by dynamic light
scattering method was 68.8 nm.
A proportion of the non-elastomeric fluorine-containing polymer
chain segment to the whole polymer which was calculated from an
increase in yield of polymer, namely ((Yield of polymer obtained in
post polymerization)-(Amount of polymer charged))+(Yield of polymer
obtained in post polymerization).times.100 was 51.7% by weight.
The obtained aqueous dispersion was frozen and coagulated, and the
precipitated polymer was washed and dried to give a white
solid.
According to 19F-NMR analysis, components of the non-elastomeric
fluorine-containing polymer chain segment in the obtained
fluorine-containing multi-segment polymer was TFE/PPVE=99.0/1.0% by
mole. Also according to DSC analysis, a glass transition
temperature of the elastomeric fluorine-containing polymer chain
was 2.degree. C. and a crystalline melting point of the
non-elastomeric fluorine-containing polymer chain segment was
314.degree. C. A melt flow rate was 15 g/10 min (at 372.degree. C.,
at a load of 5 kgf/cm.sup.2).
EXAMPLE 4
(Block Copolymerization with Non-elastomeric Segment B)
A 3-liter stainless steel autoclave was charged with 349 g of the
aqueous dispersion obtained in Preparation Example 1, 685 g of pure
water and 26.4 g of perfluoro(propyl vinyl ether) (PPVE). After
replacing the inside of a system with nitrogen gas sufficiently,
the inside temperature was kept at 80.degree. C. With stirring at
400 rpm, tetrafluoroethylene was introduced under pressure so that
the inside pressure became 8.0 kgf/cm.sup.2G.
Then a solution prepared by dissolving 10 mg of ammonium persulfate
in 2 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, at the time when it lowered to 7.0
kgf/cm.sup.2G, it was again raised with a tetrafluoroethylene gas
up to 8.0 kgf/cm.sup.2G, and thus increasing and lowering of the
pressure were repeated.
At the time when 189 g of tetrafluoroethylene was consumed after
starting of polymerization, supplying thereof was stopped, the
autoclave was cooled and un-reacted monomer was released to give
1,231 g of a semi-transparent aqueous dispersion.
A polymer content of the obtained aqueous dispersion was 20.2% by
weight, and a particle size thereof measured by dynamic light
scattering method was 82.3 nm.
A proportion of the non-elastomeric fluorine-containing polymer
chain segment to the whole polymer which was calculated from an
increase in yield of polymer, namely ((Yield of polymer obtained in
post polymerization)-(Amount of polymer charged))+(Yield of polymer
obtained in post polymerization).times.100 was 74.7% by weight.
The obtained aqueous dispersion was frozen and coagulated, and the
precipitated polymer was washed and dried to give a white
solid.
According to .sup.19F-NMR analysis, components of the
non-elastomeric fluorine-containing polymer chain segment in the
obtained fluorine-containing multi-segment polymer was
TFE/PPVE=97.1/2.9% by mole. Also according to DSC analysis, a glass
transition temperature of the elastomeric fluorine-containing
polymer chain was 2.degree. C. and a crystalline melting point of
the non-elastomeric fluorine-containing polymer chain segment was
314.degree. C. A melt flow rate was 11 g/10 min (at 372.degree. C.,
at a load of 5 kgf/cm.sup.2).
EXAMPLE 5
(Block Copolymerization with Non-elastomeric Segment B)
A 6-liter stainless steel autoclave was charged with 3,000 g of the
dispersion obtained in Preparation Example 3. After replacing the
inside of a system with nitrogen gas sufficiently, the inside
temperature was kept at 80.degree. C. With stirring at 600 rpm,
tetrafluoroethylene was introduced under pressure so that the
inside pressure became 2.0 kgf/cm.sup.2G.
Then a solution prepared by dissolving 10 mg of ammonium persulfate
in 2 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, at the time when it lowered to 1.5
kgf/cm.sup.2G, it was again raised with tetrafluoroethylene gas up
to 2.0 kgf/cm.sup.2G, and thus increasing and lowering of the
pressure were repeated.
At the time when about 10 g of tetrafluoroethylene was consumed
after starting of polymerization, supplying thereof was stopped,
the autoclave was cooled and un-reacted monomer was released to
give 3,011 g of a semi-transparent aqueous dispersion.
A polymer content of the obtained aqueous dispersion was 31.3% by
weight. A proportion of the non-elastomeric fluorine-containing
polymer chain segment to the whole polymer which was calculated
from an increase in yield of polymer, namely ((Yield of polymer
obtained in post polymerization)-(Amount of polymer
charged))+(Yield of polymer obtained in post
polymerization).times.100 was 4.5% by weight.
The obtained aqueous dispersion was frozen and coagulated, and the
precipitated polymer was washed and dried to give a white
solid.
According to DSC analysis, a glass transition temperature of the
elastomeric fluorine-containing polymer chain was -4.degree. C. and
a crystalline melting point of the non-elastomeric
fluorine-containing polymer chain segment was 263.degree. C. A
Mooney viscosity ML.sub.1+10 (140.degree. C.) of the
fluorine-containing multi-segment polymer was 101.
EXAMPLE 6
(Block Copolymerization with Non-elastomeric Segment B)
A 6-liter stainless steel autoclave was charged with 300 g of the
dispersion obtained in Preparation Example 3. After replacing the
inside of a system with nitrogen gas sufficiently, the inside
temperature was kept at 80.degree. C. With stirring at 600 rpm,
tetrafluoroethylene was introduced under pressure so that the
inside pressure became 2.0 kgf/cm.sup.2G.
Then a solution prepared by dissolving 10 mg of ammonium persulfate
in 2 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, at the time when it lowered to 1.5
kgf/cm.sup.2G, it was again raised with a tetrafluoroethylene gas
up to 2.0 kgf/cm.sup.2G, and thus increasing and lowering of the
pressure were repeated.
At the time when about 120 g of tetrafluoroethylene was consumed
after starting of polymerization, supplying thereof was stopped,
the autoclave was cooled and un-reacted monomer was released to
give 3,137 g of a semi-transparent aqueous dispersion.
A polymer content of the obtained aqueous dispersion was 19.6% by
weight, and a particle size measured by dynamic light scattering
method was 55.3 nm.
A proportion of the non-elastomeric fluorine-containing polymer
chain segment to the whole polymer which was calculated from an
increase in yield of polymer, namely ((Yield of polymer obtained in
post polymerization)-(Amount of polymer charged))+(Yield of polymer
obtained in post polymerization).times.100 was 18.5% by weight.
The obtained aqueous dispersion was frozen and coagulated, and the
precipitated polymer was washed and dried to give a white
solid.
According to DSC analysis, a glass transition temperature of the
elastomeric fluorine-containing polymer chain was -4.degree. C. and
a crystalline melting point of the non-elastomeric
fluorine-containing polymer chain segment was 328.degree. C. A
Mooney viscosity (140.degree. C.) of the fluorine-containing
multi-segment polymer could not be measured because the polymer did
not melt.
REFERENCE EXAMPLE 1
(Synthesis of Fluorine-containing Multi-segment Polymer having an
Elastomeric Fluorine-containing Polymer Chain Segment Comprising
Structural Units other than Perhaloolefin)
(1) Synthesis of Elastomeric Fluorine-containing Polymer Chain
Segment
A 6-liter stainless steel autoclave was charged with 3,000 g of
pure water and 6 g of ammonium perfluorooctanoate. After the inside
of the autoclave was replaced with pure nitrogen gas completely, a
pressure inside the autoclave was increased up to 15 kg/cm.sup.2G
at 80.degree. C. with stirring with a gas mixture of vinylidene
fluoride/tetrafluoroethylene/hexafluoropropylene (VdF/TFE/HFP) of
69/11/20% by mole. Since lowering of a pressure occurred
immediately after 4 g of 1% aqueous solution of APS was introduced
under pressure, a reaction was continued while a gas mixture of
VdF/TFE/HFP (50/20/30 in mole ratio) was fed under pressure to keep
the pressure. At the time when 2 g of the additional gas mixture
was consumed, 3.1 g of 1,4-diiodoperfluorobutane was fed under
pressure. Thereafter the reaction was continued for 15 hours while
feeding 2 g of 1% aqueous solution of APS under pressure every
three hours. Then the temperature was lowered rapidly and gas was
released to terminate the reaction. Thus a white aqueous dispersion
having a solid content of 25% was obtained. A part of the
dispersion was sampled, and coagulated with a line mixer having a
strong shearing force. The coagulate was washed with water and
dried to give a colorless transparent elastomeric polymer.
According to .sup.19F-NMR analysis, components of the copolymer
were VdF/TFE/HFP=50/20/30% by mole, and according to DSC analysis,
a glass transition temperature thereof was -10.degree. C. and
".eta." was 0.65 (dl/g, 35.degree. C., MEK). A Mooney viscosity
ML.sub.1+20 (100.degree. C.) was 75.
(2) (Block Copolymerization with Non-elastomeric Segment B)
A 6-liter stainless steel autoclave was charged with 3,000 g of the
dispersion obtained in above (1). After the inside of a system was
replaced with nitrogen gas sufficiently, a temperature inside the
system was maintained at 80.degree. C. With stirring at 200 rpm,
tetrafluoroethylene was fed under pressure so that the inside
pressure became 1.0 kgf/cm.sup.2G.
Then a solution prepared by dissolving 10 mg of ammonium persulfate
in 2 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, at the time when it lowered to 0
kgf/cm.sup.2G, it was again raised with tetrafluoroethylene gas up
to 1.0 kgf/cm.sup.2G, and thus increasing and lowering of the
pressure were repeated.
At the time when about 40 g of tetrafluoroethylene was consumed
after starting of polymerization, supplying thereof was stopped,
the autoclave was cooled and un-reacted monomer was released to
give 3,061 g of a semi-transparent aqueous dispersion.
A polymer content of the obtained aqueous dispersion was 25.5%, and
a proportion of the non-elastomeric fluorine-containing polymer
chain segment to the whole polymer which was calculated from an
increase in yield of polymer, namely ((Yield of polymer obtained in
post polymerization)-(Amount of polymer charged))+(Yield of polymer
obtained in post polymerization).times.100 was 4.5% by weight.
The obtained aqueous dispersion was frozen and coagulated, and the
precipitated polymer was washed and dried to give a white
solid.
According to DSC analysis, a glass transition temperature of the
elastomeric fluorine-containing polymer chain segment was
-4.degree. C. and a crystalline melting point of the
non-elastomeric fluorine-containing polymer chain segment was
305.degree. C. A Mooney viscosity ML.sub.1+20 (100.degree. C.) of
the fluorine-containing multi-segment polymer was 89 and
ML.sub.1+10 (140.degree. C.) thereof was 41.
REFERENCE EXAMPLE 2
(Blend of Elastomeric Fluorine-containing Polymer Chain Segment A
and Non-elastomeric Fluorine-containing Polymer Chain Segment
B)
13.5 G (15% by weight) of a copolymer (NEOFLON PFA AP-201 available
from DAIKIN INDUSTRIES, LTD.) of tetrafluoroethylene and
perfluoro(propyl vinyl ether) was put in a Brabender mixer of 60
cm.sup.3 which was set at 350.degree. C. After melting at 10 rpm
for three minutes, 73.5 g (85% by weight) of a polymer consisting
of the elastomeric fluorine-containing polymer chain segment
obtained in Preparation Example 1 was added and kneading was
carried out at 30 rpm for five minutes to give a composition.
REFERENCE EXAMPLE 3
(Blend of Elastomeric Fluorine-containing Polymer Chain Segment A
and Non-elastomeric Fluorine-containing Polymer Chain Segment
B)
A composition was prepared by kneading in the same manner as in
Reference Example 2 except that 22.5 g (25% by weight) of the
copolymer (same as in Reference Example 2) of tetrafluoroethylene
and perfluoro(propyl vinyl ether) and 67.5 g (75% by weight) of the
polymer consisting of the elastomeric fluorine-containing polymer
chain segment obtained in Preparation Example 1 were used.
REFERENCE EXAMPLE 4
(Blend of Elastomeric Fluorine-containing Polymer Chain Segment A
and Non-elastomeric Fluorine-containing Polymer Chain Segment
B)
A composition was prepared by kneading in the same manner as in
Reference Example 2 except that 42.5 g (50% by weight) of the
copolymer (same as in Reference Example 2) of tetrafluoroethylene
and perfluoro(propyl vinyl ether) and 42.5 g (50% by weight) of the
polymer consisting of the elastomeric fluorine-containing polymer
chain segment obtained in Preparation Example 1 were used.
REFERENCE EXAMPLE 5
(Blend of Elastomeric Fluorine-containing Polymer Chain Segment A
and Non-elastomeric Fluorine-containing Polymer Chain Segment
B)
A composition was prepared by kneading in the same manner as in
Reference Example 2 except that 60.0 g (75% by weight) of the
copolymer (same as in Reference Example 2) of tetrafluoroethylene
and perfluoro(propyl vinyl ether) and 20.0 g (25% by weight) of the
polymer consisting of the elastomeric fluorine-containing polymer
chain segment obtained in Preparation Example 1 were used.
EXAMPLES 7 to 11 AND COMPARATIVE EXAMPLES 1 to 2
(Measurement of Blocking Ratio)
A blocking ratio was measured by the method mentioned below with
respect to the fluorine-containing multi-segment polymers obtained
in Examples 1 to 4 and 6 and Reference Example 1 and the
composition obtained in Reference Example 2. The results are shown
in Table 4.
(Measurement of Blocking Ratio)
The blocking ratio represents a ratio indicating what percentage of
the elastomeric fluorine-containing polymer which is a starting
material is blocked (or segmented) in a process for preparing a
fluorine-containing multi-segment polymer by post-polymerizing a
polymer obtained in the first step (synthesis of elastomeric
fluorine-containing polymer). The blocking ratio was measured by
the following method.
The obtained fluorine-containing multi-segment polymers were put in
FLORINATE (registered trademark) FC-75 (available from Sumitomo
Three M Co., Ltd.) in an amount of D g, respectively (polymers of
Examples 1, 2 and 4) and in acetone in an amount of 5% by weight
(polymer of Reference Example 1), followed by sealing and allowing
to stand at 60.degree. C. for 24 hours.
Since polymer molecules consisting of the elastomeric
fluorine-containing polymer chain segment which had not been
blocked were eluted, the solution and insoluble substance were
separated and the solution was taken and dried at 120.degree. C.
for one hour. Then a concentration of the polymer elution in the
solution was measured and an amount (C) of eluted polymer
(consisting of an elastomeric fluorine-containing polymer) was
determined. Thus a blocking ratio was calculated by the following
equation. .times. .times..times. .times..times. .times..times.
.times..times..times..times. .times..times.
.times..times..times..times. .times..times. .times..times.
.times..times.
.times..times..times..times..times..times..times..times..times.
.times..times. .times..times. .times..times..times..times.
.times..times. ##EQU00001##
TABLE-US-00004 TABLE 4 Ex. 7 Ex. 8 Ex. 9 Ex. 10 Ex. 11 Com. Ex. 1
Com. Ex. 2 Sample used Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 6 Ref. Ex. 1
Ref. Ex. 2 Elastomer TFE/PMVE TFE/PMVE TFE/PMVE TFE/PMVE TFE/PMVE
VDF/TFE/ Blended components HFP composition Non-elastomer TFE/PPVE
TFE/PPVE TFE/PPVE TFE/PPVE TFE TFE of elastomer components of
Content of 16.2 24.8 51.7 74.7 81.5 4.5 Preparation non-elastomer
Example 1 components and PFA (% by weight) (85/15) Content of 83.8
75.2 48.3 25.3 18.5 95.5 elastomer components (% by weight)
Blocking ratio 94 99 100 100 97 45.5 3 (%)
EXAMPLES 12 to 16 AND COMPARATIVE EXAMPLES 3 to 7
(Measurement of Physical Properties)
The fluorine-containing multi-segment polymers and blended
compositions of elastomeric segment A and non-elastomeric segment B
which were obtained in Examples 1 to 4 and Reference Examples 2 to
5 and PFA (NEOFLON PFA AP230 available from DAIKIN INDUSTRIES, LTD)
were put in a metal die of 100 mm diameter, respectively and set on
a press machine set at 350.degree. C. After preheating for 30
minutes, compression molding was carried out at 70 kg/cm.sup.2 for
one minute to give a film of about 0.5 mm thick.
With respect to the fluorine-containing multi-segment polymer
obtained in Example 5, compression molding was carried out in the
same manner as above except that a press machine of 160.degree. C.
was used, to give a sheet of about 2 mm thick.
The following various physical properties were measured by using
the obtained molded film and sheet. The results are shown in Table
5.
(1) Hardiness
Hardness A and hardness D were measured according to JIS K
6301.
(2) Tensile Strength
The above-mentioned respective films and sheet were cut to a form
of dumbbell described in ASTM-1467, and measurements were carried
out at a cross head speed of 200 mm/min by using a TENSILON
universal tester available from Orientec Corporation.
(3) Visco-elasticity
The films and sheet were cut to a form of strip of about 35.times.5
mm and set on a visco-elasticity meter RSA-2 available from
Rheometric Co., Ltd. Then a visco-elasticity was measured at a
frequency of 1 Hz at each temperature.
TABLE-US-00005 TABLE 5 Com. Ex. 12 Ex. 13 Ex. 14 Ex. 15 Ex. 16 Ex.
3 Sample used Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 6 Ref. Ex. 2
Non-elastomer TFE/ TFE/ TFE/ TFE/ TFE Blended components PPVE PPVE
PPVE PPVE compo- Content of 16.2 24.8 51.7 74.7 4.5 sition
non-elastomer of components Prepa- (% by weight) ration Example 1
and PFA (85/15) Hardness (A) 66 77 82 89 64 64 (D) 18 24 30 35 --
18 Tensile strength 43 103 210 207 64 14 (kgf/cm.sup.2) Tensile
modulus (dyn/cm.sup.2) 25.degree. C. 7.2 .times. 10.sup.7 3.4
.times. 10.sup.8 1.2 .times. 10.sup.9 3.8 .times. 10.sup.8 -- 8.4
.times. 10.sup.7 50.degree. C. 6.2 .times. 10.sup.7 2.4 .times.
10.sup.8 8.4 .times. 10.sup.8 2.8 .times. 10.sup.8 -- 7.1 .times.
10.sup.7 100.degree. C. 5.4 .times. 10.sup.7 1.6 .times. 10.sup.8
4.1 .times. 10.sup.8 8.1 .times. 10.sup.8 -- 2.7 .times. 10.sup.7
150.degree. C. 4.4 .times. 10.sup.7 1.3 .times. 10.sup.8 2.8
.times. 10.sup.8 4.3 .times. 10.sup.8 -- 7.8 .times. 10.sup.5 Com.
Com. Com. Com. Ex. 4 Ex. 5 Ex. 6 Ex. 7 Sample used Ref. Ex. 3 Ref.
Ex. 4 Ref. Ex. 5 -- Non-elastomer Blended Blended Blended TFA
components compo- compo- compo- Content of sition sition sition
non-elastomer of of of components Prepa- Prepa- Prepa- (% by
weight) ration ration ration Example Example Example 1 and 1 and 1
and PFA PFA PFA (75/25) (50/50) (25/75) Hardness (A) 74 82 92 --
(D) 24 30 38 59 Tensile strength 31 75 170 250 (kgf/cm.sup.2)
Tensile modulus (dyn/cm.sup.2) 25.degree. C. 2.1 .times. 10.sup.8
1.7 .times. 10.sup.9 3.9 .times. 10.sup.9 5.3 .times. 10.sup.9
50.degree. C. 1.8 .times. 10.sup.8 1.2 .times. 10.sup.9 3.7 .times.
10.sup.9 4.6 .times. 10.sup.9 100.degree. C. 9.1 .times. 10.sup.7
3.9 .times. 10.sup.8 1.0 .times. 10.sup.9 1.5 .times. 10.sup.9
150.degree. C. 4.6 .times. 10.sup.7 2.0 .times. 10.sup.8 5.4
.times. 10.sup.8 8.1 .times. 10.sup.8
EXAMPLE 17 AND COMPARATIVE EXAMPLE 8
(Abrasion Resistance Test)
The fluorine-containing multi-segment polymer of Example 3 and the
blend of the elastomeric segment A and non-elastomeric segment B of
Reference Example 4 were compression-molded in the same manner as
in Example 12 to give films of about 0.5 mm thick.
(Abrasion Resistance Test)
An abrasion loss of each film was determined at room temperature at
a load of 1 kg by using an abrasion wheel CS-17 after 1,000, 2,000,
3,000 and 4,000 rotations, respectively. The results are shown in
Table 6.
TABLE-US-00006 TABLE 6 Ex. 17 Com. Ex. 8 Sample used Ex. 3 Ref. Ex.
4 Non-elastomer TFE/PPVE Blended composition components of
Preparation Content of non- 51.7 Example 1 and PFA elastomer
components (50/50) (% by weight) Abrasion loss (mg) 1,000 rotations
44 34 2,000 rotations 56 83 3,000 rotations 66 122 4,000 rotations
81 156
EXAMPLES 18 TO 21 and COMPARATIVE EXAMPLES 9 to 11
(Non-sticking Property Test)
Films of about 0.5 mm thick were produced by compression molding in
the same manner as in Example 12 by using the fluorine-containing
multi-segment polymers of Examples 1 to 4 and Reference Example 1
and PFA (same as in Reference Example 2).
Further a film of about 0.5 mm thick was produced by compression
molding by using DAIEL Thermoplastic T530 (available from DAIKIN
INDUSTRIES, LTD.) in the same manner as in Example 12 except that a
press machine set at 300.degree. C. was used.
Non-sticking property test was carried out as mentioned below by
using the above-mentioned seven films (water contact angle and
contact angle of 31 dyne solution). The results are shown in Table
7.
(Water Contact Angle)
A water contact angle on the film surface was measured at room
temperature by using a contact angle meter.
(Contact Angle of 31 Dyne Solution)
A solution (31 dyne solution) having a surface tension of 31
dyne/cm was prepared by mixing 97.5 (v/v %) of ethylene glycol and
2.5 (v/v %) of formaldehyde.
A contact angle of 31 dyne solution was measured by using a contact
angle meter.
TABLE-US-00007 TABLE 7 Com. Ex. Com. Ex. Ex. 18 Ex. 19 Ex. 20 Ex.
21 9 10 Com. Ex. 11 Sample used Ex. 18 Ex. 19 Ex. 20 Ex. 21 Ref.
Ex. 4 -- -- Elastomer component TFE/ TFE/ TFE/ TFE/ VdF/TFE/ PFA
DAIEL PMVE PMVE PMVE PMVE HFP Thermoplastic Non-elastomer TFE/ TFE/
TFE/ TFE/ TFE T-530 component PPVE PPVE PPVE PPVE Content of non-
16.2 24.8 51.7 74.7 4.5 elastomer component (% by weight) Water
contact angle 106 110 114 110 85 110 89 (degree) Contact angle of
31 47 53 54 58 25 55 28 dyne solution (degree)
EXAMPLE 22
(Synthesis of Fluorine-containing Segmented Polymer)
A 170-liter glass-lined autoclave was charged with 68.5 kg of the
aqueous dispersion obtained in Preparation Example 4 (content of
polymer: 16%, about 11 kg), 16.0 kg of pure water and 990 g of
perfluoro(propyl vinyl ether (PPVE). After replacing the inside of
a system with nitrogen gas sufficiently, the inside temperature was
kept at 50.degree. C. With stirring at 120 rpm, tetrafluoroethylene
was introduced so that the inside pressure became 5.5
kgf/cm.sup.2G.
Then a solution prepared by dissolving 1.2 g of ammonium persulfate
in 100 ml of water was introduced with pressurized nitrogen to
initiate a reaction.
Since the inside pressure lowered down with advance of
polymerization reaction, tetrafluoroethylene was supplied
continuously to maintain the inside pressure at 5.5
kgf/cm.sup.2G.
After starting of polymerization, every time when 1.04 kg of
tetrafluoroethylene was consumed, 57 g of PPVE was supplied under
pressure with nitrogen gas. PPVE was supplied four times in total
(228 g in total) in the same manner.
At the time when 5.2 kg of tetrafluoroethylene was consumed after
starting of polymerization, supplying thereof was stopped, the
autoclave was cooled and un-reacted monomer was released to give
90.4 kg of a semi-transparent aqueous dispersion. A polymer content
of the obtained aqueous dispersion was 19.5% by weight.
A proportion of the non-elastomeric fluorine-containing polymer
chain segment to the whole polymer which was calculated from an
increase in yield of polymer, namely ((Yield of polymer obtained in
post polymerization)-(Amount of polymer charged))+(Yield of polymer
obtained in post polymerization).times.100 was 37.8% by weight.
The obtained aqueous dispersion was coagulated with nitric acid,
and the precipitated polymer was washed and dried to give 16.5 kg
of white solid.
According to .sup.19F-NMR analysis, components of the
non-elastomeric fluorine-containing polymer chain segment in the
obtained fluorine-containing multi-segment polymer was
TFE/PPVE=96.0/4.0% by mole. According to DSC analysis, a glass
transition temperature of the elastomeric fluorine-containing
polymer chain segment was 3.degree. C. and a crystalline melting
point of the non-elastomeric fluorine-containing polymer chain
segment was 324.degree. C. A melt flow rate measured with a
Koka-type flow tester was 6 g/10 min (372.degree. C. at a load of 5
kgf/cm.sup.2).
EXAMPLE 23
(Fluorination Treatment of Fluorine-containing Multi-segment
Polymer)
The white solid obtained in Example 22 was put in an electric oven
maintained at 230.degree. C., and after replacing the inside of
oven with nitrogen, 20% by volume of fluorine gas (80% by volume of
nitrogen) was flowed into the oven for five hours at a rate of 0.5
liter/min. After that, the inside of the oven was replaced with
nitrogen gas sufficiently and then cooled to give a white
solid.
EXAMPLE 24
(Measurement of Blocking Ratio, Physical Properties and
Non-sticking Property)
A blocking ratio was measured in the same manner as in Example 7 by
using the white solid of fluorine-containing multi-segment polymer
obtained in Example 23. Also after producing a 0.5 mm thick film by
compression molding in the same manner as in Example 12, a hardness
and tensile strength were measured similarly by using the film, and
further non-sticking property was determined in the same manner as
in Example 18. The results are shown in Table 8.
TABLE-US-00008 TABLE 8 Ex. 24 Sample used Ex. 23 Content of
non-elastomer 37.8 components (% by weight) Blocking ratio (%) 99
Hardness (A) 64 (D) 18 Tensile strength at break 297 (kg/cm.sup.2G)
Elastic modulus (kg/cm.sup.2G) 182 Elongation at break (%) 347
Water contact angle (degree) 118 Contact angle of 31 dyne solution
59 (degree)
EXAMPLE 25
(Production of Tube)
The white solid of fluorine-containing multi-segment polymer
obtained in Example 23 was extruded at 350.degree. to 370.degree.
C. with an extruder to give pellets.
The obtained pellets were melt-extruded at 350.degree. to
370.degree. C. with an extruder having a ring die to give a tube
having an outer diameter of 10 mm and a thickness of 100 .mu.m.
EXAMPLE 26
(Production of Roll)
The roll provided with an outermost layer of fluorine-containing
segmented polymer having flexibility and an intermediate layer of
silicone rubber was produced by putting the tube obtained in
Example 25 into a cylindrical molded article having a stainless
steel substrate of 3 mm outer diameter in the center thereof so
that the inner surface of the molded article was contacted to the
outer surface of the tube and a space was provided between the
above-mentioned substrate and the inner surface of the tube, and
then pouring a silicone type liquid rubber into the space between
the substrate and the inner surface of the tube, carrying out
vulcanization and taking out the outside cylindrical molded
article.
COMPARATIVE EXAMPLE 12
(Production of Roll having Outermost Layer of PFA)
A tube having an outer diameter of 10 mm and a thickness of 100
.mu.m was produced in the same manner as in Example 25 except that
PFA (NEOFLON (registered trademark) PFA AP230 available from DAIKIN
INDUSTRIES, LTD.) was used instead of the fluorine-containing
multi-segment polymer. Then a roll having an outermost layer of PFA
and an intermediate layer of silicone rubber was produced in the
same manner as in Example 26.
EXAMPLE 27 and COMPARATIVE EXAMPLES 13 to 14
(Evaluation of Surface Flexibility)
A surface hardness, i.e. a hardness A of the rolls obtained in
Example 26 and Comparative Example 12 was measured according to JIS
K 6301 (Example 27 and Comparative Example 12)
Further a part of the fluorine-containing multi-segment polymer on
the roll surface of Example 26 was peeled and a hardness of only
intermediate layer of silicone rubber was measured in the same
manner as above. The results are shown in Table 9.
TABLE-US-00009 TABLE 9 Ex. 27 Com. Ex. 13 Com. Ex. 14 Roll Roll of
Ex. 26 Roll of Com. Silicone Ex. 12 rubber roll Outermost
Fluorine-containing PFA (100 .mu.m) Silicone surface layer
multi-segment rubber polymer (100 .mu.m) Hardness (A) 25 48 18
INDUSTRIAL APPLICABILITY
According to the present invention, it is possible to provide the
heat resistant material and coating material for OA equipments
which comprise a fluorine-containing multi-segment polymer having
heat resistance, abrasion resistance, non-sticking property against
toner and oil resistance in addition to flexibility and are used
particularly on surfaces of roll and belt of a fixing part.
* * * * *