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Patent 1139827 Summary

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(12) Patent: (11) CA 1139827
(21) Application Number: 317186
(54) English Title: OXIDE CATHODE AND METHOD OF MANUFACTURING POWDER METALLURGICAL NICKEL FOR SUCH A CATHODE
(54) French Title: CATHODE D'OXYDATION ET METHODE DE PREPARATION DE LA POUDRE METALLURGIQUE DU NICKEL POUR LADITE CATHODE
Status: Expired
Bibliographic Data
(52) Canadian Patent Classification (CPC):
  • 313/183
  • 316/46
(51) International Patent Classification (IPC):
  • H01J 1/15 (2006.01)
  • C22C 1/04 (2006.01)
  • H01J 1/14 (2006.01)
  • H01J 9/04 (2006.01)
(72) Inventors :
  • DAVIS, GEORGE L. (United Kingdom)
  • SCHOL, KLAAS (Netherlands (Kingdom of the))
  • SCHUIL, ROELOF E. (Netherlands (Kingdom of the))
(73) Owners :
  • N.V. PHILIPS GLOEILAMPENFABRIEKEN (Netherlands (Kingdom of the))
(71) Applicants :
(74) Agent: VAN STEINBURG, C.E.
(74) Associate agent:
(45) Issued: 1983-01-18
(22) Filed Date: 1978-11-30
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
44332/78 United Kingdom 1978-11-14
44331/78 United Kingdom 1978-11-14
50723-77 United Kingdom 1977-12-06

Abstracts

English Abstract






ABSTRACT
By manufacturing the support of an oxide cathode
consisting of powder metallurgical nickel in such manner
that the reductor for the emissive coating consisting at
least of one alkaline earth metal and oxygen is distributed
inhomogeneously through the nickel and forms islands having
a high reductor concentration in the surface of the
support, an oxide cathode is obtained having a low
sensitivity to poisoning of the cathode at the beginning of
the operation thereof, and electric discharge tubes rapidly
having good emissive properties can be manufactured with
said cathodes.


Claims

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


PHQ. 77-012.

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE PRO-
PERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:

l. An oxide cathode comprising a cathode support
which consists substantially of powder metallurgical
nickel, which nickel comprises an activator element capa-
ble of reducing the emissive coating, which coating is
provided on the support and which consists of a compound
of at least one alkaline earth metal and oxygen, and a
heater element disposed on the side of the cathode support
remote from the emissive coating, characterized in that an
activator element is present in the powder metallurgical
nickel in the form of nickel-coated particles of an alloy
of nickel with the activator element.
2. An oxide cathode as claimed in Claim l, charac-
terized in that the activator element is at least one of
the elements Mg, Li, Ca and Al.
3. An oxide cathode as claimed in Claim 2, charac-
terized in that the support consisting of powder metallur-
gical nickel comprises from 0.05 to 0.09% by weight of Mg
and from 0.01 to 0.05% by weight of Al.
4. A method of making a nickel strip, for a
cathode as claimed in Claim 1, characterized in that the
method comprises the steps of preparing a mixture compris-
ing nickel-coated particles of an alloy of nickel with an
activator element, and carbonyl nickel powder, rolling the
mixture to form a compacted strip, sintering the compacted
strip at a temperature of from 900 to 1100°C in a reducing
atmosphere, and rolling the sintered strip so as to form a
cathode support nickel strip of the desired thickness,
wherein the activator element is capable of reducing
barium oxide to barium at the operating temperature of an
oxide cathode.
5. A method as claimed in Claim 4, characterized
in that the mixture comprises nickel-coated particles of
a magnesium-nickel alloy, and carbonyl nickel powder.
6. A method as claimed in Claim 4, characterized
in that the mixture comprises nickel-coated particles of
a magnesium-nickel alloy, an aluminium-nickel alloy and
carbonyl nickel powder.
7. A method as claimed in Claim 5 or 6, charac-


PHQ. 77-012.

terized in that the mixture contains from 0.03 to 0.15 %
by weight of magnesium.
8. A method as claimed in Claim 6, characterized
in that the mixture contains from 0.01 to 0.10 % by weight
of aluminium.
9. A method as claimed in Claim 4, 5 or 6, char-
acterized in that the reducing atmosphere consists of
hydrogen.



Description

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


:~398~7




3-10-78 1 PH~ 77-012

Oxide cathode and method of manufacturing powder mel.allur-
gical nickel for such a cathode.
The invention relates to ~ oxi~7e cathode comp.Lisin~
a cathode support which consists substantial~y of po~der
metall.urg;.cal ni.ckeI which nic~el comprises a reductor :rOr
the emissive coatlng which coati~.~ is provided on the
support and which consists of ~ compound of at ].east one
~lkal:ine earth metal and oxygen, in ~hich support a
heating element is provided
: The in~ention also relates to an electric discharge
tube ~taving such an oxide c.athode al~d to a method of
~nanufact~ring ~owde:r metallur~rical nickel for the ~support
of such an o~ide cathode.
Such oxide cathodes have a very wi.de fiel(l of
ap~lic~tion. They may be used, for e~-ample, ;n elect.roll
tubes, di.spl.ay tubes, T.V. oamera. tubes, transttlittin~r tu~es,
klys~on~, ma~netrons, and the like.
Such an oxide cathode :is known from Pbllip* ReseclrL^h
: ~eports 26, 519-531~ 1971. The oxide la-yer descr:i.be~ :i.n
I saic. reports comprises in-ter alla BaO (bari.um o~i~e). T}~e
reductol used consists of one or ~cre oi` the elements .~l,
C, Mgr, Si. or Zr, whleh el.ements reduce a part of the 13~.0 to
Ba. Th~ reductlon of the BaO takes pl.ace :in t.llat t:~.te
~educto:r ~i~fuses from tht-.~ nick.el S11~0:1'~ stril~ in th.
l~yer o~ B~O on the ~upport u:nder ,'he inf`~ence c~f tlle
thexltla1. eneI~ry of tlle hecater elemell.', and re~llce~ $1~ere
2S th~ B~O to free ~ rhic3l d.:ifru~3 to the ~1rf~ee oi` the


, '
q~

11398Z7

.

3-'l0-'7~ ~ P~Q 77-~lZ

, layer of Ba0 and f`orn]s -cherQ a l~onoat.om:ic surface layer o.t`
¦ low work function.
¦ Cathode support stri.p consistin~ of nicke~. containingr
an acti~ator element such as Al, C, Mg, Si or Zr, has bee
made by a powder r~etallurgy method in ~rhich ~I mixture o~`
the consti.tuent powders is compressed to form a blocl~, the
~ compressed block is sintered, ~nd the sinccred :Lllgot i5
f rolled. 'l`his method recluiros a. po~rerful press, ~rhich is
¦ expensive, and the centre of tlle ingot is rclatively porou.s.
'~ l0 It i5 necessary to si.Il1;er ]~rge in.gots at :relati~rely higl
temperatures :~or a lon~ -timeS Por examplo at 1300C ~or
48 hour~, in order -to recluce the porosity of the cellcre of
the ingot. However, such a process is not suitable h-ithout
taking troublesome precautions .such as encaps~ .t;:ing the
ingQt when the activator element i~s ~agllc~ium, ~rhich i~
volatile and has a bolling ~oint o:f 1'l00C.
~ isadvan.tagre of kn.own ox;de cathoclcs UsiIlg known
.~ catllode supr~ort nickel strip is that the quan-tity of` free
ba:riun~ available when the cathocle is first operated i.5
20 reduced consi.d.erably by ga3 residue~ in the electrQn tube'
in which the cathocle is used,'~hich residues form c0l1lpouuds.
' w:it'h the free bariun~. Thl3 is terrlled tlle poisoi~lr!g of thc
cathodeO Such poisoni.n.g gas r~sidue~s are :formed not only as
a result of i.nsuffic:ient evaCuati.Qn Or or leaks in the
25 elect.ron tube ( a ~rood vacuum of` 10 7 mm llg still meanC
10~9 mol o~ ~as I)er cm3) 'lut ~llso Qs a re~u'lt of hoati~
i and evvlutio.rl o~ ga.~e~s I':rom componotlts ill tlj.e tube. More-
.3 over, the cat'hode~poisoning gases can be ~ormed UpO-l im~act
of electrvlls ~ith materials and thc g~s may b~ rcleased
30 from the glass ~ra.ll o~ the electron lub~ A3 already said,
~ ca-thode poisoni.ng occurs i.n particular at the begir~ning of
it the opcration of the cal.hode so t~ t the tl~bc i.n which sai~
, cathode ic;ll.sec' i.nitially shows a pOOI Operati.Orl as a
j resul.t o~ a poGr cathode em-ission.
J 35 :C-I ;.s the-leroré~ the o~ject'o:~ the in~rention to
pro~r:ide an oxicle cat~lode whlc~rl at the~ beë~inn:i.r~ of` the
. operatio~l of said caihocle i.s cc~ls:iclerabl~r les_ xe.ls:iti.-~-c to
poisonirlg ~ncl which, whe:n used i.n a tubc, ra~ y ~chic~re~




, . ~ .

:1~39827


¦: 3-10-78 3 PHQ 77-012
I




j ' a good emiss:ion.
i ~ccording to ~he invention, such a cathode of the
kind descrlbed in the I`irst ~aragraph is characterized in
! that the reductor i 5 distribut~3d i.nhonlogeneou~ly through
the nickel ol` t~le ~upport a.nd Iorms islailds ha.~-.r;g a high
reductor concentration ill th.e surface of the support.
The activator element diPfuses from th.e intelior of
the cathode support as a reslllt of a conc~ntratlon gra~ient
~ of the aGti~ating elemt3nt being set u~ between the oxide-
T 1U bearlng sur*ace o~ the cathode .support arld tlle inte:rlor of
¦ the cathode s~pport as a result of a reaction between bari~
oxide and the activati~lg element at the surface o~` the
cathode support. Thus free barium -which was lost by reacticn
with gas residues in the electron tube is replaced.
~ 15 Diffusion occurs at acceptable~ rates as a result of` the
i high temperature of -the ca-thode support duriIlg oparation
of the cathode. The nickel coating surroundj.ng the
i particles oP an allo~r of` ni.ckel and an activator element
ma~.es it possible to si.nter the compacted strip at high
20- speeds and low temperatures, and makes the sintoring process
casier to control.
When magnesium is used as an activator el~3ment, it is
introduced into tne powder mixture in the form of nickel-
~: control particles of` a ni.ckel-magnesium alloy, for example
25 containing '15~, b~ wei~ht of magnesi.um co-tecl w:;tll ~uch a
th.icklless of lliolcc~l t'hat the m~gne,s:Lum ~ontent. of tho
l eoated partlo:L~ , 2$ hy we:L.~,rht,. B~r lntroducing the
¦ magnesium ln this manller, the ni.ckel-mag-.resium alloy i3
protected Prom oxi.dation by traces oi` o~rgen which are
30 inevitab~.y present in the si.nterlng ~1,mos~here. I~ is
oon~en.:i.enl; to i.ncorporate al.umini,urn when used in tho nlix-tu~
in the ~o-Lm oP a nlccl~,ol--aluminlu.n al3.oy contai.nin~, f`or
ex~mple 5~ ~y weight c.P .~luminill~. When the .lc~i~r~to:r
el.ement i..s ma~n~sium, -the magnesium contenl o~ e n.cliol.
3~ .strip m~y b~ f'rom 0.03 to 0015,~'. by weightO kT~len tlle nic~e:L
st,r:ip i;lClU~ alumlni.~in-l, t~e alu:nir.iulTI c:ontent o~` the
nicl~.el strip ma.y be f':rom 0~01 t~ 0.10G~ we~

11398Z7


3-10-78 4 P~IQ 77-012

Comn1ercially available carbonyl nickel powder consists of
more than 99% by weight,of` nickel, together with trace
impurities. Small quantities o~ other elements, such as
tungsten, may be included in the mixture in order to
improve the n1echanica:L properties of the nic1~elst.:rip.
The nickel-coated particles of the alloy of nickel
with an acti.va1;or element a.re thorou~hly mixed with carbo- -
nyl nicl~el powder and any ot'her ingredients of the mixture~
A strip i.s -then rolled from the mixture, the th:icknr3ss of`
th.e compact,od .strip bei11g ~roverned by the apparatus
avallable. Thc compact~d st,rip is the~ sintered, and the
sin-tered strip is then rolled so as to reduce the thickness
of the stri.p to a desired value~ l`he rolled strip ma)r be
a3lnealed ii` desired.
- l5 An embodiment of the invention ~ill now be described
with reference to the drawin.g in ~hich
Fig~lre 1 is a sectional clevat:ion of an oxide cathode,
I~`igur~ 2 is a sectional elevation of a kno~rn cathode
support bc3aring a bariulr.-calcium-stron1;ium oxide layer,
~igure 3 is a sectio3lal elevation of a cal,hode
support nickel strip made by a method a~cording to thr_
invention bcaring a barium-calcium-strorti1lm o~ide layer,
Fi.gure 4 is a plan ~rie~ of a disc of a cathode
support. ~ickel strip made 'by a method according to the
invention.
'Fi~ure 5 is a. schemal;ic slde cl.evl.tion of an ~p1~ara
tllS usc3d to makQ a sintered compncted strlp by ~ m~thoc~
a~cording to the inventlon, and
Figure 6 is a plan vie~ of the rollers of t'.he
apparatu~ sh.o~n in Fi.~ure 5.
Fi~,r~lre 1 shows an oxide~ cathode consistin~ of a
support 1 made of the strip made by the metr.od described
w:itll rcfereJ;ce -to Figrures 5 and ~ ~ecllred -to cl cathode
s'ha.~ 2. A heatcr ele-rllen~ ~ i.s sit:uate~i below t,he suppor~
1. The s~ ort. 1 bears a laye- ~ ol` (BaCaSr~0. This layer
4 is o1~taiil~d ~ spra.yl~g .1 suspens:ion oi' b~rium-ralciu~
: st.rontium carl~onat~ onto the support 'I and con.verti11g t'he
CarbO31ate il~CO (~aCa~r)0 by hea,.tir~

1~398Z7
i
1 3-10--7~ 5 ~HQ 77-012

i l~igure 2 sllows a part of a p.rior art support 1
I bearing an emissive layer 4. This prior art support was
produced from a casting of an or a high temperature sintere~
powder metallurgy alloy of nickel ancl an ac-tivator element
5 which is shown as dots homogeneous1y distributed in t~le
nickel of` the support and the activator e]ement diffllses
into the emissive la~er 4 durin.g ope:ration of the ca~nc,de.
en the emissi~re layer 4 ha.s been F~olsonec1~ the I~aO i.n
this cathod~ is not reduced suffi.c.i.ently ral~idly so that
th~ emission of the cathode cont;inues at a lower level than
was t~le case before poisoning.
Fi~ure 3 shows a part of the support 1 according to
the i.n~entlon bearing the emissi.~Te layer 4. Th~ activator
elemel1ts 6 Mg and Al are present in the n~ckel of the sup-
i l~ port and at the surface of the support in a loca].l.y ~
conceIltrated form so that the supporting consisting of
po-~der raetallurgical nicke]. colnprises I.i. 0.05 to o.oc~
by weigllt of Mg an.d from 0.01 to 0.05~ by we~ hi; of A.l~
~ A.s a :esult of thls being localiy concentrated it initially
:~ 1 20 di.. ff1lses con.siderably more rapidly i.n-to the emissive layer4 a.nd can rapidly replenish the Ba which has been lost ;-lS
a result of poisoning.
Figure 4 is a plan view of ~.he support 1 according
to tlle irl~cntion in which the islands 6 havin~ a high
con.c~ntrati.oIl of activa1;or elemen-t are si1.uated. l~
be ob~i.ous that the cat;llode n.iclcel may also be used in
other cath.od.e oonstrllctio.ns, and ~cl;i~at()r olcrncnts an~l
1' a.lka].i.. ne earth motal oxidos other than those de~cribsd may
b~ usedO
Now a method for mallllfactuLin~ n1etal].l.lr~ical nic1~l
i for su.ch a cathode wi1l be describ6d.
A magn~sl-ml-nickel a.lloy corl1;a:inin~ 15,~, by wei.gh1; o:t`
j ma~lles:L~ Ti in the .forl~ of lu.nps was crushed9 ~round and
1 s-ie~Je~ I;he matsri.al p~s~in~ a 350 mesh (mcshe~s pcr illCI' )3~ s:ievc beir~l~ coll.ected. ~rhi.5 minu~ ~50 mesn IriatcriLtl ~.~as
coated w:ith a t.~ic.n~s.s of ni.ckel suc1~. tha~ t~e Inclg-rl~s1.u~
content Or t~;le coace~ particles 1~a; 2~o ~y ~Tei~ht. Thc
part-~c.~os w~re coat;ed ~i.th nic~;~l in an autoc1ave by tlle


.
: .
,,
:, .. ~ .. .. . .. . . .. .. . ........ , .. ~ .. ... .

1~39827

3- iO-1 ~)7~ 6 PHQ 77-012

reductiLon of an aqueous ar~nonlaea . solution eol~taining
n.~ekel. sll~phate and amrllonium slllpha.t~ heated to 175C,
the au ,;oealve eontai.ning an over-pressure of 350 lbs/in2
o:f h-~7drogGn.
1~ master Dlixt;ure consis ting oI` equal weigh.ts of
tungsten powder and carbonyl. nick~al powder having average
particle ~sizes of 3/um was prepared. All alunl-lniun~-nlcke].
(52/~l~3 by weight) ~:~owrlGr was sleved through a I-()O mesh
sieve and t.he rni.l~us IIOC mesh :fraetion w~s use-l.
A m~ tu~e \~as pri3parod consistilng of
80 g o:f thc3 ll:icke~ l-coa ted magne~sillm-lli.cke:l. alloy
parti.cles
1 . (:'j g C!:~ th~a n1intl.s 1loo mesh alumillium-nic3~el. alloy
powder
80 ~ o:L` th~ tungsten arid ea-.rborl~_ niekel master
mix-l;ure
1 ælTO g o:E` earbonyl nickel po~del .
This mi:~ture eor~a:Lns 0.08 ~ llg, 0,04 % by woig~nt
Al arl.d 2 G~ y we igh t W .
Re:ferring -to l?igures 5 and 6 o:L` the dr~3wings, po~rder
mixture 1 0 was fed i~to a h.opper 11 I`rc,m l~Thi.Ch the powder
pQ,ssed i.lltO a o.6 rr!rn wide gap 12 bet~eerl t~-To 15G mn~
~liameter rollers 13, 14 xu.nning in th(3 hori~,ontal plan~.
The eoJrpacted stri.p 15 l~as.sed over suppor-t rollers 16, 1 ~
and læ b~3fc-re enterLn~ a mu:Erle tube 19 o:f a muI:E:le furn~ce
ZO l.n whieh the strip 15 l~as si.nte:led. .Puret dry h5~clrogre
wa~ passed throuT~r~h th.e muf:fle ttub~3 1~3 ~llcl t.h~ st;r.ip
passed l;hl ou~r,h t;he lu:r]lace at ~ueh a r at.c~ t llat: a peak
tenll~t3ral:uro o:~ 1050~C wa~s appli.ed :Eor 3 m:L~ .tos, Thc
s-lntc3r~ed s~tr.:ip 21 em~r~in~ rrorn ~t~ e n~ f.fle tUb? 1~3 w~
J;~ 011~ 1 Go(,) Itlm d:~arl~et~ SpO~ I 2'> ~ ~rll~3 sillte c`e~' s~ i
~as 0. 7 ~ t~li.C~:' arld ~ra~; SUbs(?r~L~:(37:ltLs~ I`OLleCi to ~i~e a
fll,xl thlcl~ne~ of 100/u~n~ Thi.~; 100/un; strip I a~ nsi3c~ lo
rnali.f3 t~ 3 oxi.~r2 Cat'rlOQ'3 suppox~t~




., . ~ . ~

Representative Drawing

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Administrative Status

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Administrative Status

Title Date
Forecasted Issue Date 1983-01-18
(22) Filed 1978-11-30
(45) Issued 1983-01-18
Expired 2000-01-18

Abandonment History

There is no abandonment history.

Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $0.00 1978-11-30
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
N.V. PHILIPS GLOEILAMPENFABRIEKEN
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 1994-01-05 6 304
Drawings 1994-01-05 2 33
Claims 1994-01-05 2 63
Abstract 1994-01-05 1 37
Cover Page 1994-01-05 1 15