AU466752B2 - Method of recovering a rare earth phospher - Google Patents
Method of recovering a rare earth phospherInfo
- Publication number
- AU466752B2 AU466752B2 AU29831/71A AU2983171A AU466752B2 AU 466752 B2 AU466752 B2 AU 466752B2 AU 29831/71 A AU29831/71 A AU 29831/71A AU 2983171 A AU2983171 A AU 2983171A AU 466752 B2 AU466752 B2 AU 466752B2
- Authority
- AU
- Australia
- Prior art keywords
- rare earth
- phosphor
- oxydizing
- salt
- earth phosphor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Description
2 9,8 3 1
Method of recovering a rare earth phosphor.
The invention relates to a method of recovering
a rare earth phosphor from a mixture which comprises this
phosphor and at least one sulphide and/or selenide of zinc
and/or cadmium. Furthermore, the invention relates to a
rare earth phosphor obtained by such a method, and to a
cathode-ray tube which comprises such a rare earth phosphor.
Cathode-ray tubes for the display of coloured
images, particularly coloured television images, generally
have a luminescent picture screen which may be excited by
electrons originating from one or more electron guns present
in the tube. Such a luminescent screen generally has a large
number of phosphor groups which are arranged on the surface
of the screen in accordance with a certain pattern. Each
phosphor group is built up from a number of, for example,
three phosphor elements in the form of lines or dots which
upon excitation by electrons emit light of a given colour,
for example, green, blue and red, respectively.
Different methods are known for the manufacture
of these colour screens. In a method which is frequently
used the starting material is an aqueous suspension which
comprises a certain phosphor to be provided on the screen
and a photosensitive material, for example, polyvinyl alhocol
and ammonium bichromate. A quantity of this suspension is
provided on the screen whereafter a large part of the suspen-
sion (the suspension excess) is removed again. The material
4 6 6,7 5 2
29,831 rn.
which is left on the screen has the shape of a thin layer having certain dried and subsequently exposed by radiation arranged in wavelengths through an apertured mask which is in the mask corre- the vicinity of the screen. The apertures formed. Under the influ- spond to the phosphor elements to be is polyme- ence of the radiation the photosensitive material so that at these rized in the irradiated areas of the screen water. Poly- areas the polyvinyl alcohol becomes insoluble in areas of the merisation is not effected in the non-exposed from screen, so that the material can readily be removed (so-called deve- these areas by means of rinsing with water remains on the lopment) and the desired phosphor pattern to be screen. This method is repeated for the phosphors a different further provided while every time exposing from
direction, so that the desired pattern of phosphor groups is
formed.
In the above-described method only a small portion the aid of a of the original phosphor material provided with residues suspension is left on the screen. The manufacturing removed from t.he formed consisting of the suspension excess have screen and the development residues removed by rinsing
a considerable value especially when a rare earth phosphor the is concerned. These rare earth phosphors, for example, oxides, known red luminescent europium cr samarium-activated are general.- vanadates or oxysulphides of a rare earth metal screen. As a result ly provided as the last material on the of pro- the manufacturing residues formed during the process
3 46 6.7 5 2
29,8 31nm
viding the rare earth phosphor not only contain polyvinyl
alcohol and chromium compounds, but also phosphor particles
originating from previously provided phosphor elements as
impurities. These previously provided phosphors generally
consist of sulphides and/or selenides of zinc and/or cadmi-
um, for example, blue luminescent silver-activated zinc
sulphide and green luminescent silver-activated zinc cadmi-
um sulphide.
Also when using methods other than the one des-
cribed above for the manufacture of colour screens manufac-
turing residues are often obtained which contain the costly
rare earth phosphors. The solid substances present in the
manufacturing residues are generally first separated from
the liquid, for example, by spinning or filtration, whereby
a wet mixture is obtained which may be optionally dried. For
a further effective use of the rare earth phosphors present
in the mixture it is necessary to remove the impurities, par-
ticularly the traces of other phosphors, which influence the
emission colours, as much as possible from these residues.
A method of recovering a rare earth phosphor from screen
manufacturing residues is known, for example, from U.S.
Patent Specification 3,474,040. In this known method the
manufacturing residues are treated with a heated mineral a--id for example, HNO HCI or H 2 S0 4 The sulphides and/or sele-
nides present in the residues dissolve in the acid used and
are subsequently removed by rinsing. A drawback of the known
method is that a portion of the rare earth phosphor is also
4 466.752
29,831I.
In the case of a often dissolved and is consequently lost. cannot be used luminescent rare earth oxide the known method dissolves at all because the rare earth oxide substantially oxysulphides of in the acids used. Also the luminescent respect so that rare earths present difficulties in this
considerable losses may occur. to provide The object of the present invention is phosphors from an improved method of recovering rare earth of the known manufacturing residues in which the drawbacks it is possible method are largely obviated and with which oxides. to recover also luminescent rare earth recover- According to the invention a method of which contains this ing a rare earth phosphor from a mixture selenide of zinc phosphor and at least one sulphide and/or the mixture is mixed and/or cadmium is characterized in that with a saltoxydizingiat an increased temperature and is
at a temperature of subsequently heated for at least 1 hour thus obtained is wast- at least 3000 C, and that the product
ed with water.
In a method according to the invention the sul-
mixture are oxydized phides and/or selenides present in the
at an increased temperature to form the oxides of zinc and/'
and/or selenium oxidoQ. or cadmium and volatile sulphur oxides are formed whose During oxydation further reaction products salt to be used and nature is determined by the oxydizing a method according which are generally soluble in water. In by washing with to the invention they are completely removed
5 466.7 9
2 9,831/n.
water. The mixture obtained from screen manufacturing resi-
dues may be dried in advance in a method according to the
invention, but it is alternatively possible to start from a
wet mixture which is mixed with the oxydizing salt.
In many cases it is desirable to remove the oxides
of zinc and/or cadmium formed during the heat treatment from
the reaction product. Therefore a method according to the
invention is preferred in which the product obtained during
the heat treatment is rinsed with a diluted acid before it
is washed with water. The oxides of zinc and cadmium complete-
ly dissolve in these diluted acids, so that they are separa-
ted from the rare earth phosphor.
A method according to the invention has the advan-
tage that it is more selective than the known method, that
is to say, the rare earth phosphor is attacked to a slighter
extent so that a larger yield of the desired rare earth
phosphor is possible. Furthermore, an important advantage
is that a method according to the invention is very suitable
notably for the recovery of rare earth oxides for which the
known method cannot be used.
The temperature at which the heat treatment is to
take place is dependent on the temperature at which the oxy-
dizing salt to be used starts to decompose and is generally
to be at least 3000 C. The heating period may be chosen within
very wide limits, on the understanding that when using a
certain oxydizing salt this period can be chosen to be shorter
466752 4 6 6,75 2
2 9,8 3 1 M1
as the temperature is chosen to be higher. It has been found
that generally the heat treatment is to take place at least
V hour. The heating temperature and period are also dependent
on the quantity of contaminating sulphides and/or selenides
and on the resistance of the sulphides and/or selenides,
which resistance is also determined by the crystal shape and
the crystal size.
All salts decomposing while forming oxygen at the
reaction temperature may be used as oxydizing salts. However,
nitrates and/or halogenates, for example, the nitrates, chlo-
rates or bromates of alkali metals or of alkaline earth me-
tals are preferred. These salts are cheap and are available
in a pure form. As an Example of a chlorate, which may be
used advantageously, potassium chlorate may be mentioned
which decomposes at already relatively low temperatures (from
approximately 3000 C) in which 1 mole of KCIO gives rise to
1 mole of in water soluble KC1 and 3 atoms of oxygen. As an
Example of a nitrate, potassium nitrate may be mentioned for
which, however, higher temperatures are required (from apprc-
ximately 4000 KNOJ decomposes at these temperatures wbiJe
forming KNO 2 soluble in water and oxygen.
In a method according to the invention the oxyd'z-
ing salt is preferably used in a quantity which is larger
than is required in accordance with'the stoichiometry for
the oxydation of the sulphide and/or selenide present, so
that an intimate mixture of the phosphor mixture and the
salts, which are in a molten state at the reaction temperature,
7 466.7 52
2 9 ,831m
is obtained. A full reaction of the zinc and/or cadmium sul-
phides and/or selenides is then ensured.
In one preferred embodiment of a. method accord-
ing to the invention the heat treatment is performed for T
to 3 hours at a temperature of between 400 and 8000 C. In
fact, it has been found that for the oxydizing salts to be
used optimum results are obtained at these values of the
heating period and temperature.
A method according to the invention may be advan-
tageously used for recovering luminescent oxides and vana-
dates of rare earth metals. Many of the red luminescent
phosphors which are most generally used in cathode-ray tubes
for the display of coloured images belong to this group of
phosphors.
It is to be noted that the polyvinyl alcohol pre-
sent in the phosphor residues is completely oxydized to form
gaseous compounds such as carbon dioxide and water vapour
and that traces of chromium compounds which are often still
present are oxydized to form chromates which are soluble in
water. Furthermore, it is to be noted that phosphor mixtures
originating from screen failures and from cathode-ray tubes
rejected during the manufacture of the tubes may alternative-
ly be treated by a method according to the invention.
In order that the invention may be readily carried
into effect, it will now be described by way of several
Examples.
Example 1.
8 4 6 6,7
29,831/71
gms of a phosphor mixture consisting of red
luminescent GdVO 4 -Eu, green luminescent (Zn,Cd)S and blue
luminescent ZnS which mixture contained 2.0 by weight of
ZnS and 0.01 by weight of CdS were mixed with 3 gms of
NaNO3 and subsequently heated for 1 hour at a temperature
of 7000 C.
Subsequently to cooling, the product obtained
was rinsed in 200 mls of aqueous 10% acetic acid solution
for 20 minutes at room temperature. The phosphor was then
washed electrolyte-free with water and dried.
The GdVO 4 -Eu obtained contained less than 0.005
by weight of sulphides and had a luminance upon electron
excitation which was equal to that of the original pure
vanadate. The quantity of gadolinium vanadate obtained was
98.5 by weight calculated on the original quantity.
Example 2.
In a manner analogous to that in Example 1, 15 gmin
of a phosphor mixture consisting of Y 0 3-Eu and approximate-
ly 2% by weight of ZnS were treated in which, however, 2 gms
of KBrO3 were used as an oxydizing salt and in which the
heat treatment was performed for 1.5 hours at 6000 C.
The Y2 0 3-Eu obtained contained less than 0.01
by weight of sulphides and bad a luminance upon electron
excitation which was equal to that of the original pure oxide.
The quantity obtained was in this case 99.2 by weight.
Example 3. In a manner analogous to that in Example 1,
9 466, 7 5 2
29,831n/71-
gms of a phosphor mixture consisting of Y202S-Eu and appro-
ximately 2% by weight of ZnS were treated in which, however,
gms of KCIO were used as an oxydizing salt and in which
the heat treatment was performed for 2 hours at 450° C.
The Y202S-Eu obtained contained less than 0.005
by weight of sulphides and had a luminance upon electron
excitation which was 95 of that of the original yttrium
oxysulphide. The quantity obtained was in this case 90.5
by weight.
10- 466.752
Claims (1)
- 29,8 3 1 n/.THE CLAIMS DEFINING TIt INVENTION ArU AS FOLLOWS:I. A method of recovering a rare earth phosphorfrom a mixture which contains said phosphor and at leastone sulphide and/or selenide of zinc and/or cadmium,characterized in that the mixture is mixed with a salt/oxydizing at'an increased temperature and is subsequentlyheated for at least V hour at a temperature of at least300° C, and that the product thus obtained is washed withwater.2. A method as claimed in Claim 1, characterizedin that the product obtained is rinsed with a diluted acidbefore it is washed with water.3. A method as claimed in Claim 1 or 2, characteriz-ed in that a nitrate is used as an oxydizing salt.4. A method as claimed in Claim 1 or 2, charact-erized in that a halogenate is used as an oxydizinG salt.A method as claimed in Claim 1, 2, 3 or 4, cha-racterized in that the oxydizing salt is used in a quanti-ty which is larger than is required in accordance with thestoichiometry for the oxydation of the sulphide and/orseienide present.6. A method as claimed in any of the precedingClaims, characterized in that the heat treatment is perform-ed for to 3 hours at a temperature of between 400 and800° C.11 46 75229,831/n.7. A method as claimed in any of the precedingClaims in which the rare earth phosphor is a member fromthe group of the oxides and vanadates.8. A method of recover ng a rare earth phosphor,substantially as herein describe9. A rare earth phosphor obtained by a method asclaimed in any of the preceding Claims.A cathode-ray tube for the display of colouredimages provided with a rare earth phosphor as claimed inClaim 9.Dated this seventh day of June 1971N.V. PHILIPS' GLOEILAMPENFABRIEKEN12 466,7 5 2
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NLNL7008684 | 1970-06-13 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU2983171A AU2983171A (en) | 1972-12-14 |
| AU466752B2 true AU466752B2 (en) | 1972-12-14 |
Family
ID=
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS5436204A (en) | Method of recovering isopren | |
| CA953903A (en) | Method of recovering a rare earth phosphor | |
| PH9701A (en) | Method of recovering nickel | |
| AU466841B2 (en) | Method for sealing earth formations | |
| CA971345A (en) | Method of forming a spacer-expander | |
| CA969347A (en) | Method of recovering a rare earth phosphor | |
| AU457256B2 (en) | Metal recovery | |
| AU2983171A (en) | Method of recovering a rare earth phospher | |
| CA996945A (en) | Bisorganoalkaline earth compounds and a method of preparing same from bisorganomercurials | |
| CA930153A (en) | Method for preparing a rare earth phosphor | |
| AU467353B2 (en) | Metal recovery method | |
| CA922133A (en) | Method of securing a tube in a tubeplate | |
| AU447983B2 (en) | Improvements relating to phosphor recovery | |
| AU458726B2 (en) | Improvements inthe recovery of metals using electrowinning | |
| AU476189B2 (en) | Well drilling method | |
| AU458585B2 (en) | Method of securing a tube in a tubeplate | |
| SU604905A1 (en) | Method of enlarging borehole | |
| CA970979A (en) | Mercury recovery process | |
| CA833003A (en) | Method of producing a smoke-preparation | |
| CA932519A (en) | Method of forming a pole structure | |
| CA928508A (en) | Rare earth intermetallic compounds produced by a reduction-fusion process | |
| CA833520A (en) | Method of recovering alkylamides | |
| CA831950A (en) | Recovery of spent etchants | |
| CA867662A (en) | Process for recovering rare earth metal values | |
| CA931384A (en) | Rare earth intermetallic compounds by reduction-diffusion process |