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Patent 1206507 Summary

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(12) Patent: (11) CA 1206507
(21) Application Number: 488467
(54) English Title: ELECTRICAL DEVICES COMPRISING CONDUCTIVE POLYMER COMPOSITIONS
(54) French Title: DISPOSITIFS ELECTRIQUES COMPRENANT DES POLYMERES CONDUCTEURS
Status: Expired
Bibliographic Data
(52) Canadian Patent Classification (CPC):
  • 26/123
  • 309/85
(51) International Patent Classification (IPC):
  • H05B 1/00 (2006.01)
  • H01C 7/02 (2006.01)
  • H05B 3/14 (2006.01)
(72) Inventors :
  • KAMATH, HUNDI P. (United States of America)
  • LEDER, JEFFREY C. (United States of America)
(73) Owners :
  • RAYCHEM CORPORATION (Not Available)
(71) Applicants :
(74) Agent: MARKS & CLERK
(74) Associate agent:
(45) Issued: 1981-08-11
Reissued: 1986-06-24
(22) Filed Date: 1977-12-12
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
750,149 United States of America 1976-12-13

Abstracts

English Abstract



ABSTRACT OF THE DISCLOSURE

A process for the manufacture of a device compris-
ing at least two electrodes and a conductive polymer compos-
tion in contact therewith, which process comprises (1) heat-
ing a conductive polymer composition to a temperature above
its melting point (Tm); (2) heating at least two electrodes,
out of contact with the conductive polymer composition; (3)
melt-extruding the molten conductive polymer composition
from step (1) over the pre-heated electrodes from step (2),
the electrodes being at a temperature Te and the conductive
polymer being at a temperature Tp when the electrodes and
the conductive polymer are first contacted with each other;
and (4) cooling the electrodes and the conductive polymer
composition; the conditions of the process being such that
the electrodes and the conductive polymer composition in
contact therewith are at a temperature above Tm for a time
which is sufficient to reduce the contact resistance between
them and which is less than five minutes.


Claims

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



The embodiments of the invention in which an exclusive property
or privilege is claimed are defined as follows:
1. A process for the manufacture of a device comprising an
electrode and a conductive polymer composition in contact
therewith, which process comprises
(1) heating a conductive polymer composition to a
temperature (Tp) above its melting point (Tm);
(2) heating an electrode, out of contact with the
conductive polymer composition, to a temperature
(Te) above the melting point of the conductive
polymer composition,
(3) contacting the electrode, while it is at a
temperature above Tm, with the molten polymer
composition; and
(4) cooling the electrode and conductive polymer
composition in contact therewith.

2. A process according to Claim 1 wherein the conductive
polymer composition exhibits PTC behavior.

3. A process according to Claim 1 or Claim 2 wherein the
polymeric composition is thermoplastic.

4. A process according to Claim 1 wherein T? is at least
(Tp-55)°C.

5. A process according to Claim 1 wherein both Tp and Te
are at least 20°C above Tm.

12


6. A process according to Claim 5 wherein both Tp and Te
are at least 55°C above Tm.

7. A process according to Claim 1 wherein both Tp and Te
are above the Ring-and-Ball softening point of the conductive
polymer composition.

8. A process according to Claim 1 wherein the conductive
polymer composition is melt-extruded over at least two spaced-
apart electrodes.

9. A process according to Claim 8 wherein the conductive
polymer composition is extruded over a pair of stranded wire
electrodes.

10. A process according to Claim 9 wherein the electrodes
are separated by a distance of 0.15 to 1 cm.

11. A process according to any one of Claim 8 to 10 wherein
the electrodes are silver-coated copper wires or nickel-coated
copper wires.

12. A process according to any one of Claims 8 to 10 wherein
the conductive polymer composition is extruded as an extrudate
having a cross-section which the largest dimension is not
more than 3 times the smallest dimension.

13




13. A process according to Claim 1 wherein the conductive
polymer composition exhibits PTC behaviour and has a resistivity
at 21°C of 100 to 50,000 ohm. cm.

14. A process according to Claim 1 wherein the conductive
polymer composition contains at least 15% by weight of carbon
black.

15. A process according to Claim 1 wherein the conductive
polymer composition contains carbon black dispersed in a
crystalline polymer and exhibits PTC behaviour.

16. A process according to Claim 1 which also comprises the
further step of cross-linking the conductive composition.

17. A process according to Claim 16 wherein the cross-linking
is effected by irradiation.

18. A strip heater comprising
(1) an elongate core of a conductive polymer
composition which exhibits PTC behaviour, which
comprises carbon black, and in which, if the
content (L) of carbon black in percent by weight
is less than 15, L and the resistivity (R) of
the composition in ohm. cm at room temperature
are such that

2L + S log10 R > 45;

14


(2) at least two longitudinally extending electrodes
embedded in said composition parallel to each
other; and
(3) an outer layer of a protective and insulating
composition;
the average linearity ratio between any pair of electrodes being
at most 1.2.

19. A strip heater according to Claim 18 wherein the average
linearity ratio between any pair of electrodes is at most 1.10.

20. A strip heater according to Claim 18 or 19 wherein the
electrodes are silver-coated wires or nickel-costed copper wires.



21. A process for the manufacture of a device
comprising at least two electrodes and a conductive polymer
composition in contact therewith, which process comprises

(1) heating a conductive polymer composition to a tem-
perature above its melting point (Tm);

(2) heating at least two electrodes, out of contact
with the conductive polymer composition;

(3) melt-extruding the molten conductive polymer com-
position from step(1) over the pre-heated electro-
des from step(2), the electrodes being at a
temperature Te and the conductive polymer being at
a temperature Tp when the electrodes and the con-
ductive polymer are first contacted with each
other; and

(4) cooling the electrodes and the conductive polymer
composition;

the conditions of the process being such that the electrodes
and the conductive polymer composition in contact therewith are
at a temperature above Tm for a time which is sufficient to
reduce the contact resistance between them and which is less
than five minutes.

22. A process according to Claim 21 wherein Te is at
least (Tp-55)°C.

23. A process according to Claim 21 wherein Te is at
least (Tp-30)°C.

16


24. A process according to Claim 21 wherein Te is at
least (Tm-25)°C.

25. A process according to Claim 21 wherein Te is
greater than 65°C.

26. A process according to Claim 21 wherein Te is
greater than 82°C.

27. A process according to Claim 21 wherein Te is at
least about 165°C.

28. A process according to Claim 21, 22 or 26 which
comprises heating the electrodes and the conductive polymer in
contact therewith.

29. A process according to Claim 21, 22 or 26 which
comprises heating the electrodes and the conductive polymer
in contact therewith by resistance heating of the electrodes.

30. A process according to Claim 21, 22 or 26 which
comprises, after step(3), heating the electrodes and the con-
ductive polymer in contact therewith, said heating of the
electrodes after step(3) being insufficient substantially to
reduce the resistivity of at least part of the conductive
polymer extrudate.

31. A process according to Claim 21, 22 or 26 which
comprises, after step(3), heating the electrodes and the con-
ductive polymer in contact therewith, said heating of the
electrodes after step(3) being such that, if the same process
is carried out without said heating the electrodes after step(3),
the resistivity at 21°C of the conductive polymer in the pro-
duct is less than 50,000 ohm.cm.

17


32. A process according to Claim 21, 22 or 26 wherein

(a) the conductive polymer comprises carbon black
dispersed in a crystalline polymer, and exhibits
PTC behavior;

(b) the conductive polymer is melt-extruded over two
parallel electrodes; and

(c) the process conditions are such that the device which
is manufactured is a self-regulating strip heater
having an average linearity ratio of at most 1.2.

33. A process according to Claim 21, 22 or 26 wherein

(a) the conductive polymer comprises carbon black
dispersed in a crystalline polymer, and exhibits
PTC behavior;

(b) the conductive polymer is melt-extruded over two
parallel stranded wire electrodes; and

(c) the process conditions are such that the device which
is manufactured is a self-regulating strip heater
having an average linearity ratio of at most 1.1.

34. A process according to Claim 21, 22 or 26 wherein

(a) the conductive polymer comprises carbon black
dispersed in a crystalline polymer, and exhibits
PTC behavior;

(b) the conductive polymer is melt-extruded over two
parallel electrodes; and

18


(c) after step(3), the electrodes and the conductive
polymer in contact therewith are heated under con-
ditions such that the resistivity of at least part of
the conductive polymer extrudate is not substantially
reduced by said heating of the electrodes after
step(3).

35. A process according to Claim 21, 22 or 26 wherein

(a) the conductive polymer comprises carbon black
dispersed in a crystalline polymer, and exhibits
PTC behavior;

(b) the conductive polymer is melt-extruded over two
parallel electrodes; and

(c) after step(3), the electrodes and the conductive
polymer composition in contact therewith are heated
under conditions such that, if the same process is
carried out without said heating of the electrodes
after step(3), the resistivity at 21°C of the conduc-
tive polymer in the product is less than 50,000
ohm.cm.

36. A process according to Claim 21, 22 or 26 wherein

(a) the conductive polymer comprises carbon black
dispersed in a crystalline polymer, and exhibits
PTC behavior;

(b) the conductive polymer is melt-extruded over two
parallel electrodes which are at a temperature Te
which is greater than Tm when the electrodes and the

19



conductive polymer are first contacted with each
other; and

(c) the process conditions are such that the device which
is manufactured is a self-regulating strip heater
having an average linearity ratio of at most 1.2.


Description

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


I 49/ 201
.
lZ(~507
n~ ~ ntiO . relat~ to elec~ic~l de~lc~ in whict~ an


.

a~pris~ o~Anlc E~lym rs h~vir~ d~rs~ ~r~in ~ ~n~ly divid~d
S ~ ill, ~ a~m blac:3c or a p4rtia~lAt ~etal.
5~ ~uch ~ ath~bit ~d P~C (Po~i~ve 5~~
C~icient) ~vior. m~ ~y ~ h~ b~ used in the p~t
to de~ P~C b~vior ~ variabl- ad o~ ~r-ci~. ~n

c ~ ositicn~ d-note a o~mpo~it~ ving at t~ant on
t ~ ture rang- (herQina~t~r c211~d a critic~l rang~) wh~ch i~
~ithin th- llmit~ o~ -lOO-C an~-ak~ut 250-Cs at th ~ ginning of which
the oo~pw ition haJ a resi~tivity.bolo~ about 105 ohQ. c~.~ and ~n
which the ccnpw ltion ha~ an ~4 valu- o~ at l~t 2.S ~r an ~0O v~lu~
of at le~st 10 ~And p~ferably both), and pr~f~rably ha an ~ 0 valu
of at least 6, where ~4 i3 th~ rat~o of the red~tiviti~ at the ~nd
an~ the begi ~ of a 14-C rang~, ~0O is th~ rat~o of th~
re~i~tivitics at th 2nd ~nd the bQginnlng of a lOO-C r~nq-, and ~0 i~
the ratio of the r L~tlviti~ at th~ end and the beginnlng of a 30-C
range. The tcr~ ~PTC el~mentR i~ us~d herein b~ denotc an element
ccmpo~d of a PrC oompo ition as definod abov-. A plot of the lcg of
the r i~tance of a PTC element, meaJur-d between two electrode~ Ln
oontact with tha element, against tcmptratux~, will often, t ~ h by no
me~n~ invarlably, ~ho~ ~ aharp ch4ng- in ~16Qe w er a pa~t o~ th
cr~tical t6np~raburo r~ng~, ~n~ In such ca~e~, th~ ter~ ~witch~ng
trmperab~r~ (usually abbr-viat~d to T5) i~ u~d her~in to denot- the
to~peratur- at th~ ~nO~rs ctlon point o~ exten~on~ of the
sub~tantially ~traight portion~ of ~uch a plot whlch li- elther ~ide of
th~ portion s~wirq th- sharp chang~ . m~ Prc c~mFo~ition in
~ a PrC de~t i~ de~crib~d h~in ~ h~ u~ful T~. me
prefera~ly b~n ~ and 17S-C., ~.g. 50-C to 120-C.

12(~6S~7
Ca~uctive p~lymer c~T~sitions, especially PrC ç~sitions,
are u~eful in elec~lc~l d~ccs ~n whi~ the o:snposition i~ in contact
with an elec~cde, u~uaLly of met2Llr Device~ of this ~cind are usually
manufactl~red by metldq ~pr~3~ng at~l~ or mou~d~ng the m~ltal
S polymer ~ sition ~round or ag~ ~st tl~ electr~de or el ~ des. ~n
the known methods, the electrode it not he~te~ prlor to oontict with
the polymer w utusition or i~ heated only to a l~mitsd extent, for
examçlc t~ a temperature well below the melting point of thc
.~u~u~ition, for example not re than 65-C as in conventional wire-
ooatinq tech~iques. ~Temperaeures ~.o in C throughout thi5
specifica ion.~ Wkll known exAmçle~ o~ such t~vices are n exl~le st-ip
heater~ which ~I~Li9~ a gener~lly ribbonrsh~ped o~re of the conductive
polymer compo~itlon, a pair o~ lonqitLdinally extendLng electrcdcs,
gener~lly of stranded wire, mboddod in the o~re near the edges
thereof, and an outer layer of a protective and msl~latlng ccmposition.
Particularly useful heater~ are those in which th~ composition e~hibits
PrC behavior, and which are therefore self-regulating. In the
preparation of such heaters in whlch the comFosition contains less than
15% of carbon black, the prior art has taught that it is necessary, m
order to obtain a sufficiently lcw resistivity, to anneal the heater
for an extended period such that

ZL + 5 logl~ R< 45
where L i5 the percent hy weight of carbon and R is the resistivity in
ohm.c~. at roon temperature.

A disadvantage which a~rlse~ with devices o~mprising an
d ectrcde and a conductiv~ polymer oomposition in contact wnth the
electrodc, and in particular with strip heater~, is that the longer
they are in ser~rice, the bigh is t!~eir resistance and t~e lo~e- is
their E~wer out~t, partlcularly ~hen ~hey are s~ject b~ thennal
cycling.

lZ(~6S~t~
It is ~n t~at var~ au, ~n device ~ device, of the
~ntact resi~t~nce betw~ electr~e~ arr3 carb~lack-filled rub~
lt an obst~cle ~ c3~ari90n of tl e electrlcal characteristi~ of such
devices ar~ e acc~at~ measureneslt of the re~i tiYity of such
S rubbers, par~:ioularly at high re~ vitie~ and low voltages; ar~ it
has be~ su~ted that the saDe i~ ~ue of oth~r conductive polymer
amE~itions. Variou~ method~ h~ve bean su~qested for re~ucir~ the
~ntact resi tance bet~ c~bl~ck-fi1led n~ers and test
ele~e~ plac~d in ccntaot therewith.. m~ preferr~ methcsd is
vulcan~s~ the rubb~ while it i~ in contact with a bra~ el~ode.
Otl~ ~etlx~ds includ~ ~pcr-~lat~r~, vacw~ating ~nth ~old, ar~ the
use of coLtoidal solutions of graphite betwe~ the electrcde arx3 the
test plece. Ebr de~ s, r~ference s ~ ld bo made t~ ~ upter 2 of
~Conductive Rubber3 and Pla~tics~ by R ~. Nor~an, published by Applied.
15 Science P~blisher~ ~1970), from which it will be clear that the factor~
which govern the size of such 03ntact re~istance arc not well
understood.

We have now disow ered ~hat the less is the initial contact
resist~nce ~etween an electrode and a conductive polyme comFosition,
the smaller i~ the incrc~s~ in total resistance with tLme. ~e have
also disc~vered that by placiny or m~intaining an elect cde and a
polymer composition in oontaot wit~ each other while both are at a
temperature above the melt~nq point of the ~ vsition~ the oontact
re~istance between the~ is reduc~d. The teDm ~melting po m t of the
oomposition" is used hein to denote the ~rature at which the
oomFo~ition begin~ t~ m d t. The time for which the electrcde and the
03mpo~ition ne~d be in oontact with each other, ~hile e~ch is at a
temperature above the meltlng point of the composition, in orde- to
achieve the desired r ult, i~ quite short. TLmes in exces~ of five

lZ(~6S(~7

m m utes do not result in any substantial fucther ceduction of cont~ct
rc~i~tance, and often times les~ than 1 m m ute are quite a~equate and
are therefore preferre~. Thus the ~reatment time is of a quite
diff ent order from ~hae requl~ed by the known annealing treatments bo
deccease the resastlvity of the ccmçosition, as described for exæmple
in ~.S. Patents No~. 3,823,217 and 3,914,363.

In one aspect, therefore, the inv~ntion prcvide~ a ~ ess
~or t~e prqparation or modification o~a device ~L~ ng an elect ode
and a con~uctiv~ polymcr oomp w ition i~ oontact wi~h the clectrode,
0 whic~ xoe3~ CampriX3 contaCt~ng~ or mdintain~ng conta~t bet~een, the
~uctive p~lymcr ocmposltlon and the d ectrcde whlle the oonduc~ive
polymer oomposition i3 at a te~Feraturc ~$p) ab~ve it~ melting polr.t
(Tm) and the electrode is at a t~nperature ~Te~ abcve the m d ting poin~
of the conductive ccn~oo~ition, Tp and Te beinq the same or different,
for a time which is sufficient to reduce the oantac~ resis nce between
the electrode and the conductive polymer composition but whidh is not
sufficient-substanti~lly to reduce the resistivity of the oonductive
Folymer. Preferably both Tpa~d Te are at leas~ 20-C, especially at
least 55-C, above Tm~ It is often preferable that both Tp and Te
2~ should be above the Ring-and-Ball softening t~mpera e of the polymer.
ocmposition.
Preferably the conductive polymer conposi~ion is subjected
to pre5sure to assist m bringing it into c!ose ~onfo~ity with the electrode.
The p¢essure i~ gen ally at lea~t 14 kg/c~2, prefcrably at least 2l.
kg/c~2, for example 21 to 200 hg/cm2, especially at lea~t 35 hg/cm2,
e.g. 3S-70 kg/cm2.

-. lZ~6S~7
We ~ave als~ foun~ that the contact resistance c~n be
~rrelated ~th the force ne~ded to pull the elecl.L.~le fmn the Folymer
c~ltial. Acc~rd~r~ly the ~nv~elctl further prwide~ ~ deviY
ccn~rising N~ ele~e ~ contac~ ~ith a ~nd~elve polyme~
~ltion, especi~lly a ~tr~ded w~re electrode ~ dded.~n a
ccx~ductive polysner ~sieio~n, the pull s~cren3th (P~ of ehe elec~ode
fr~m the de,lice beir~ equal t~ at least 1.4 time~ PO, where PO i3 the
p~lll stre~th of an ident~c~l elec~cde fml~ a devi~e whieh .~ises
~n idultical elec~de in clt~ct. with an identical conductive p~lymer
0 c~mposi~ and which ha~ pared b~ a pro~ess whi~:h con~ist~ of
contacting the el~c~ode, while it is at a temperature not greater than
24e~, w~th the x l~en oonductive polymer oomçosition, an~ allownng t~e
polymer coDposition to ~col in contact ~ith the electrode. The pull
strengths P and PO are detesmined ~t 21C as describçd in detail below.

A 5.1 cm long sæmple of thc heater strip (or other device),
contaLninq a-straight 5.1 cm length of the electrcd~s, i5 cut off. At
one end of the samçle, 2~5 cm of the electrcde is stzipped bare of
polym OE . rhe bared elect-cde is passed dcwnwardly t.~rough a hole
slightly larger than the electrcde in a rigid metal plate fixed in t~e
horiDontal plane. The end of the bared electrode is fi~ly clamFed in
a mcvable clamp below the plate, and the other end of the sample is
lightly cla~ç~d above the plate, so that the electrcde is vertic~l.
m e movable cl~mp i~ then moved vertically dcwnwards at a speed of 5.1
cm~min~, and the pe~k force needed to pull th; conductor ~ut of ~he
sample is me~sured.




.. _ _ .. _ _ .. . . _ . . _ . _ . _ ~ . .

lZ-~S~7
Wk h~ve also found that ~or strip heaters, curren ~y the most
widely ~lCAd d~vic~s m which current is passed through conductive
polymer oompo~it~on~, e~e oontact resi-~tance can be o~rrelated with the
linearity ratio, a qu~nt$ty which can re~dily be ~easured as described
bel~w. Accordingly th~ 1nventlon ~ur~her provides a strip heatcr
oomprising:
(1) an elongatc core o a conductive poly~er comçosition
which exhibits ~TC beh~lor, whlch comprise-~ car~on blac*, and in
which, if the oontent (L) of carboQ black Ln percent by weight is less.
~han lS, L and the resi~t$vity R o~ the oompo3ition in oh~. om are such
that
2~ ~ 5 log10 ~ > 45
~2) at least tw~ longit~dinally extending electrcoes
embedded Ln said composition par~llel to e~ch other: and
IS `(3) an out~r layer o~ a protectlve and msulatmg
comFo~ition;
the average line~rity ratio (and prefcrably the linearity ratio at 211
points~ betwe~n ~ny pair o~ elect mde~ being at ~ost 1.2, pre~erably at
most 1.15, especially at mcst 1.10. m e l m e~rity ratio of a strip
heater is defined as
Resistance at 30 MV.
Resistance at 100 V.
the resiQtances be mg m~swr~d at 21C between tw~ electrodes which are
contacted by prcbe~ push~d thro~yh the outer jacket and the oonductive
polymeric sore oS the strip heater. The o~ntact re-~istance i~
neql~gible at 100 V., ~o that the closcr the l~n ity ratio i3 bo 1,
the lower the contact re~istance.
The LnVention i~ useful with any txpe of electIode, for
exaTçle~plates, strip~ or wires, but particularly so with electrcdes
haYiny Dn irregular surfac~, e.g. str nded wire electrcdes as
conventionally used ln ~trip hcaters, br~ided wire electrode~ (for
examçle a descr~bed ~n Ger~an Offenl q ungschrift No. 2,635,000.5)

~2~6S07
and expar~able elect~de5 as describ~ in Gerrran Off~legungs*~ift No.
2,655,543.1. Preferred ~tranded wire~ are silver-)at~d and nic~
~ated copper w~res, wh1~h are 1e~Q su~tible to difficultie5, such
as melt~ or oxidatiotn, than t~coats~ or unc~ted copper wire~,
S t~uqh the latter can ~e usad wit~ut difficulty pr~vid~ng the
t~at~es ~r~l~d are not too high.

The c~uctive polyn~ c~psitioru ~sed in thi~ ~nves~tion
gener~lly c:on~n car~on black a~ the conductive filler~ e.g. in zn~t
gre~ter or le53 than 15% by weight, f~r example greater t~an 17% or 20%
by wcight. In many caxs, lt ~ prderr~d that the ca~sitionJ s~ld
exhibit ~C behavior. The resistivity of the c~osition i5 generally
le~s than 50,000 oh~ at 21-C, for ex ~ le 100 to 50,000 ohm.~n. Fbr
strip h~ters designed bo b~ powered by A.C. of 115 ~olts or more, the
composition generally ha~ a resis~vity o~ 2,000 to 50,000 ohm.c~, e.g.
2,000 to 40,000 ohm.cm. 5he oomposition 1~ pr~ferably thesmoplastic.
~owever, it may be ligh~ly cro59-linked, or be in the process of being
cross,linked, provided that it is sufficiently fluid under the
contacting condition to conform closely to the electrode surface.
The polymer is preferably a cry-st lline polymer.

The strip heater~ with which the invention is concerned
generally have two electrcde~ separat~d by a distance of O.lS to 1 c~,
:-: but gre~ter separations, e.g. up to 2.5 cm. or even more, can be used.
m e o3re of oonductive polymer can be of c~nventional shape, but
preferably it has a cros~-sectl~n which is not re than 3 times,
especi lly nct re than 1.5 times, e.g. not more than 1.1 times, its
smallest dimension, especially a round cross-sect~on.




_7_

lZ~65~7

In one pre~erred embcdiment of the ~nveneion, the electrcde
and the polymer composition are hea~ed ~epara~ely ~efore be mg
contacted. In this ol~Jlment, it i~ p~eferred that the coTposition
should be melt-e~truded cver the electrcde, e.g~ by ~xtrusion around a
S pa~r of spaced-apart wire electrodes using a cross-head die. m e
el ~ e i3 pre-heated to a t2mperature (Te) which may be greater or
les~ than the melt temperab~re of the polymer .~4usition (Tp) bu~ i~
gen ally more than ~Tp-55) and prefer~bly more than (Tp-30). Tp will
norm~lly be substanti~lly ab w e the meltlng point of the oomposi~on,
tO ~or examçle 30 to 80C abcv~. Of o~urse, nelther the elec ~ ~de nor the
ocmp~ition sh2uld b~ he~tod to a t3mp~rature at which ~t undergocs
substanti 1 ox~dation or oth degradation.

In another embodiment of the m vention, the coTposition is
shaped in contact w~th the elec W e (wnthout pre-heating the
electrode) and the elec~rode and the composition are then heated, while
in oontac~ wnth each other, to a t~mperature ab~ve the melting ~OLnt of
the composition. Care is needed to ensure a useful reduction in the
contact resistance by this method. The optimum conditions wlll
depend upon the electrode and the ~usitiGn~ but inc~eased ti~e,
t~mperablre and pressure help to ac~ieve the desired result. me
pressure may be applled for examç~e in a press or by means of nip
roller~ is embodiment o~ tbe ~nvention is particularly use~ul when
tbc need for, or deeir~bility of, an anneAling treatment does not arise
at all, for exam~le, w~hen the ocmposition ha~ a c~rbon blac~ oontent
gre~ter than 1~% by weight, e.g. greater than 17% or 20% by weight, or
when only a limlted anne ling treatment is carried out, such that at
the end of the annealing tbe o~ntent of c~rbon black tL) and the
resis~ivity (R) are sucb that 2L + 5 log10 > 45.

one w~y of heatlng the eleotrcde and the ccmposition
surr~unding it is to pas~ a high current ~hrough the electrcde and thus
produce tbe desired he~t by res~stance heating of thc electrcde.

:12(~65~7
~n another ~mbodlment Of the invention, the conductive
polymer 03mposition is initialiy in the fonm of a shaped article, e.g.
one or xre pill~ or pellet~, whlch ha~ not been 5hyped in contac~ with
the electrode, and the electrode an~ the c~l~us~tion are heated
bogether under pretsurc, for e ~ o ln a compresslon mould.

. 2~rticularly when the oonductive poly~er oompo d tion exhibits
PTC behavior, it ~ often des~rahl~ that Ln the final prcduct the
ccmposition sh~uld be crc~-linkod. Cr~3s-linking c~n be carried out
as a separate strp after thQ troat~ent b~ reduce oaQtact resistance; in
10- this c~se, cro3s-linking with aid of radla~ion ls preferr~d.
Alternatively crc~rl~nkinq c m be c~rriod out simultan~eously with the
said treat~ent, ~n which case che~ical cross-l~nking with the aid of
cross-linXing lnitiators such as peroxides is preferred.

me invention is illustrated by th~ foll~ ExamFles, scre
of which are canparative E~mple~.

In ea~ of the Example3 a strip heat ~QS prepared as
describff~ below The cor~uctive p~lymer ccrnFosition wa5 obtained by
blend$ng a ~edi~ den~ity poly~thyl~ne containing ~ antiox$dant wit~
carbon black ma~ter batch ~npr$s$nq an ethsylene,/ethyl aylate
c~lymer to giv~ ~ ~5it$0n containing the indicated perc&nt bv
weight of ca~on black ¦ ~Ihe m~t~ng po~nt o~ th~ ~os~t~on waa ~out f
~115-6~ me ccmp~$tian wa~ melt-extn~ed at a mclt temperatl~re of aba~t
180-C through a cro~ he~ d$e h~v$ng a circular or~ice 0 36 a~ in
diameter over a pair of ~randed ilvcr-coated oopper wires, each w$re
having a di m et r of 0.08 cm and o~mpr~inq 19 st:ands, and the a~es
of the wires being on a di3meter of the ori ice and 0.2 cm aFart.
Before reaching th~ crosJ-head die, th~ wires were pre-heated by
passing th~m through an oven 60 c~ long at 800-C. m e temperature of
the wires entering the die w~s 82-C in the comparative EXa~ples 1, 4
and 6, in which the speed of the wires thr3ugh the cven and the die


_g_


was 21m/m~, 165-C in Ex~e~ 2 ~ 7 and 193C in E~amples 3 ar~ 5.

me extr~ate wQ.~ then given an insl?lating j~cket by melt-
ex~ud~ng aro~d lt ~ layer 0.051 ~n thick of ~lorinat~ F~lyethylene
or an ethylene~te~ r~etl~lene copolymer. me coats~ ~xtru~at~ was
t~ irr~iated in order to os9-link the c~ ctive polyner
cc~sition.

EX~ES 1-3

5hese E~ople~, in which Exa:nE~e 1 is a c~nparative Ex2~21e,
domonstrate the inQ uence of ~inearity R~tio (LR) on Pcwer ~utput wh~n
the heater is subjected to te~perature changes~ In eadh Ex~mple, tbe
Linearity Ratio of the he~t ~as me~sured and the heater wQ~ then
oonnected to a 120 volt AC supply and the ambient temperature was
changed continuously over a 3 minute cycle, being raised frJR -37-C bo
65C over a pericd of 90 seconds and then reduced to -37C 3gain cver
the next 90 seconds.

m e peak power out2ut of the heater du- m~ each cycle ~as
measured initi~lly and at interval and expressed as a ~roportion ( ~ )
of the initial peak power output.

m e polymer ccm~vsition used in EXample 1 oontained a~out 25
carb~n black. T~he polymer compwitlon used in E~amçles 2 and 3
contained about 22~ carbon black.

12~651~7
~he results obt~ined are ~ in Table 1 below.

LE 1

. of C~cles ~Ec2mple 1 Example 2 Eurr~le 3
PN ~R PN ~R N
None 1 1.3 1 1.1
500 0.5 1.6 1.3 - 1 1
1100 0.3 2~1 1.2 - 1 1
ltOO - - 1.1 1.1 1 1
~a~arative E~nple

E~MP~ 4-7

These E~c~mple~, which are Sumnarised in Table 2 below,
da~ns~ate thc effect of pre-heating the ~ec~odes on t!le Linearity
Ratio arYI Pull Strength of the produ::t.

~.BLE 2

.
l; E:xample No. ~ Carbon_31ac!c Lirle ~ ~tio

~4 22 1.6
~2 1.0
*6 23 1.3S
7 23 1.1
20~Ca~arative E~t~nple

The r2tio of the pull ~trengt~s of the heater strlps of
B~eq 7 and 6 (P/PO) was 1.45.

Representative Drawing

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Administrative Status

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Administrative Status

Title Date
Forecasted Issue Date 1981-08-11
(22) Filed 1977-12-12
(45) Issued 1981-08-11
Reissued 1986-06-24
Expired 1998-08-11

Abandonment History

There is no abandonment history.

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $0.00 1985-08-09
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
RAYCHEM CORPORATION
Past Owners on Record
None
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Description 1993-06-28 11 402
Drawings 1993-06-28 1 6
Claims 1993-06-28 9 209
Abstract 1993-06-28 1 25
Cover Page 1993-06-28 1 14