Patent Application
20100062673
The invention relates to a method for integral recycling of cathode ray tubes.
Electrical and electronic equipment production is a greatly expanding field in the Western world.
Technological innovation and market expansion are continuing to speed up the replacement process of products having a lifetime which does not exceed 3 years. Thus, in 2000, the production of end-of-life electrical and electronic waste in France was evaluated at 1.5 million tonnes, half of which being household waste. Since then, a progression of 3 to 5% per year of this figure has been observed. European deposits of these waste products are estimated at 400,000 T/year, 90% of which still end up in landfills. This is why new directives stringently regulate this type of waste, the latest to date being directive 2002/96/CE of 27 Jan. 2003.
These new rules for management of such products impose minimum recycling rates. Cathode ray tubes do however represent a relatively large proportion of end-of-life electrical appliances and electronic equipment. Therefore, to achieve the required global recycling rate, it is imperative to achieve high recycling rates for cathode ray tubes.
A colour cathode ray tube comprises a faceplate glass containing among others barium and strontium oxides, and a cone glass containing a large quantity of lead oxide. These two parts are joined to one another by a seal and are coated with layers called “functional layers” formed by metal oxides, rare earths, graphite and iron. Metal parts in the form of plates are placed inside the tubes before the latter are closed. In particular the layer deposited on the inside surface of the faceplates is composed of Zinc, Cadmium, Yttrium and Europium-based electroluminescent materials. All these compounds tend to give the cathode ray tube as a whole a toxic nature, which is why various solutions have been proposed for treatment of these cathode ray tubes.
U.S. Pat. No. 4,858,833 describes a cathode ray tube recycling method by crushing, then treatment with fluoroboric acid followed by selective separation of the various components. This method presents several drawbacks, in particular on account of mixing of the glasses, dissolution of metal parts and the use of fluoroboric acid. In particular, this acid has shown its limits in waste treatment in particular through all the attempts to perform industrialization of the processes (in particular in battery recycling). The glasses obtained by mixing the faceplate (barium-based) and the cone (lead-based) are difficult to recycle as-is.
It has therefore proved indispensable to proceed with opening of the tubes and to separate the tubes. The first method used is the diamond slitting wheel. This technique ensures good opening, but is accompanied by large emissions of glass particles and requires manual operations.
It is to overcome this drawback that Patent DE4234706 describes a method for opening and separating the two components by means of a heating wire. This separation can only be performed if notches are made over the whole perimeter of the cathode ray tube, and the rate at which this type of operation can be performed limits the productivity and requires very precise placing of the wire after the notches have been made.
Moreover, the luminophore layer composed of electroluminescent materials is at present removed by any physical means and the powders obtained are sent to a toxic waste storage centre.
No operational industrial process providing an outlet for these powders has as yet been established.
In general manner, methods using oxalate for separation of rare earths have been known for a very long time, as they have already been proposed since the early 1900's and have been extensively implemented (C. James, J. Am. Chem. Soc. vol. 30, p. 979, 1908). They are efficient for mixtures of lanthanum, thorium, yttrium and cerium. The full processes are moreover extensively described in the reviews Journal of Soc. Chem. Eng, (R. W Urie, 46(437) year 1947 and E. S Pilkington 46(387) year 1947) and J. Appl. Chem. [E. S Pilkington 2(265) year 1952 and 4(568) year 1954]. The presence of zinc, cadmium and yttrium on the other hand singularly complicates operations. In addition, the precipitate, which is very fine, gives rise to impurities (in particular the etching acid anions). Finally, formation of oxalate complexes with the other products results in over-consumption of oxalate.
It is for this reason that various different methods have been proposed. We have already seen that U.S. Pat. No. 4,858,833 describes a process for recycling these powders via a fluoroboric method followed by precipitation of oxalates. In addition to the drawbacks of fluoroboric acid, the oxalates have to be calcinated to obtain recyclable oxides, which leads to emission of CO2.
Patent DE19918793 describes a process for recycling these powders by etching with nitric acid followed by carbonate precipitation and then calcination to obtain oxides. There again, the drawbacks are mainly related to emissions of nitrogen oxide and CO2.
The object of the invention is to provide a method for integral recycling of cathode ray tubes enabling these different drawbacks to be overcome.
According to the invention, this object is achieved by the appended claims.
More particularly, this object is achieved by the fact that the method enables the glasses composing said cathode ray tubes and the luminophores deposited on the internal surface of screens to be recycled by associating the following steps:
Other advantages and features will become more clearly apparent from the following description of particular embodiments of the invention given for non-restrictive example purposes only and represented in the accompanying drawings, in which:
As illustrated in
The cathode ray tubes are opened by means of a laser source, such as a CO2 laser with a power comprised between 300 mW and 3 kW and a wavelength comprised between 10 μM and 11 μm.
A first advantage of this opening method lies in the fact that opening does not require an initial notch. This is advantageous as the notches have the consequence of considerably reducing the opening time. A second advantage stems from the fact that the power of the laser is sufficient to destroy the seal completely, which provides a direct opening at the junction between the faceplate and the cone, whereas opening by saw or by heating wire leaves about a centimeter of the faceplate glass joined to the body of the cone.
Once the cathode ray tubes have been opened, for a good valorization of the glasses it is important that all the coating products situated on the internal surface of the faceplate and on the internal and external surfaces of the cones be totally eliminated.
In order to provide protection of the workstation operators and to achieve an efficient surface treatment, techniques such as direct dry brushing are discarded. With a concern for protection of the environment and to avoid eliminating large quantities of waste water, washing with water is discarded.
The surface oxides are thus removed by dry treatment by means of a surface treatment agent (cleaning agent) in solid state. The agents used are preferably chosen from steel shot, sodium bicarbonate and calcite. These three products have in fact given satisfactory results in so far as the layers are totally eliminated, in particular on the layers where they are very adherent, as illustrated in
These three products are preferably chosen for the ease of subsequent treatment of the mixed fractions comprising the surface treatment agent and the products resulting from the surface treatment.
When steel shot is used for treating the faceplate and the cone, the products obtained are treated by magnetic separation to separately obtain the luminophores or other oxides on the one hand and the steel shot on the other hand.
When sodium bicarbonate or calcite is used for treating the faceplate, these products are eliminated during treatment of the luminophores.
The luminophores powders are treated by a method that does not involve either oxalate or ammonia. The electroluminescent assembly comprises an aluminium sheet and a layer of luminophores powders. A very large majority of the powders are able to be separated by screening at 500 microns.
The fraction larger than 500 microns is mainly composed of aluminium foil as shown by
The fine fraction is mainly composed of zinc and yttrium with the presence of europium, iron and manganese, as shown by scanning electron microscope observation (
After the screening operation, the chemical process proper is implemented as represented in
The powder resulting from the treatment described above (references 1 and 2 in
In this step (reference 4 in
Neutralization can advantageously be performed by means of soda or potash with a concentration comprised between 10% and 35% in weight. The neutralized solution is then mixed with an alkaline fluoride solution (for example potassium or sodium fluoride) heated at 50° C. and in a stoichiometric ratio equal to that of the Yttrium+Europium content increased by 10% weight. The precipitate formed is then separated and then washed with industrial water at a temperature comprised between 30° and 40° C. This washing water is then used in the first step of the process for preparing the 2N acid from concentrated acid.
The solid is then suspended in a soda solution at 30% (reference 5 in
The cathode ray tubes are composed of two types of glass:
For a good valorization, the glasses have to be treated separately. To avoid pollution, in particular of the barium glass by the lead, melting is performed in an externally cooled inductive loop, thus forming a self-crucible. This self-crucible presents a large number of advantages, one of which is formation of a frozen layer of glass around the crucible, which avoids any use of refractory material and any pollution of the glasses.
To obtain a constant composition on output, the silica, barita and strontium carbonate contents are adjusted by making addition to the crucible. The high-frequency electric field lines cause turbulences in the molten bath which have the huge advantage of homogenizing the molten material. This enables uniform melting to be obtained, and consequently results on output in a glass of homogeneous composition with a total absence of unfused material.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/FR2005/001711 | 7/4/2005 | WO | 00 | 12/28/2007 |
