The present invention generally relates to recycle a substrate and in particular to an apparatus and method for recycling the same by electrolytic etching and chemical stripping of a substrate surface. The present invention more specifically relates to the use of an electrolytic etching apparatus and method applied to remove metal materials from the surface of a metallic workpiece (i.e., a substrate) for patterning.
In the microelectronics industry, semiconductor components are fabricated in a layer process which includes steps, such as spin coating or sputtering, to deposit organic layers and inorganic metal layers, namely an organic-inorganic composite sheet, onto a substrate surface. One such electronic component comprises the organic-inorganic composite sheet is a color filter substrate of a LCD panel, which includes a glass substrate 91 on which is coated with organic layers of a resin black matrix 92, a RGB photoresist 93 and an overcoat 94, and a metal layer of an ITO film 91 covered on the outmost, as depicted in
Typically, semiconductor components are fragile and require a complicated manufacturing process which causes a low yield. Any problem such as particles, defective films, dislocation or high impedance may cause a defective substrate. These defective ones from the process, as well as household waste products, such as LCD wastes, have become serious environmental pollutants.
Various techniques are employed to recycle the defective workpieces, i.e., substrates, during processing so as to reduce the loss due to the low yield and to reduce the pollution of the environment. Two prior art techniques are found in Taiwan Pat. No. 546,264 and No. 546,265, which disclose chemical processes for recycling a defective Cr-BM color filter substrate and a defective Resin-BM color filter substrate respectively. The prior arts mainly describe the methods comprises the steps of dipping the defective color filter substrate into acidic etchants; brushing through the substrate surface and cleaning the same to obtain a reusable glass substrate with Cr-black matrix remained thereon according to No. 546,264 or a renewed mother glass substrate according to No. 546,265.
However, the acidic etchants strips not only the organic layers of the color filter substrate but also the metal layers thereof, which generates a poisonous waste liquid with heavy metal therein, thereby causes a secondary pollution. What is desired, therefore, is a recycling system and process which is not subject to the secondary pollution.
With respect to etching techniques for patterning of thin metallic films, the process of drying etching, wet etching or electroetching is widely employed. For examples of the uses of the electroetching process, see Taiwan Pat. No. I223350, and U.S. Pat. Nos. 5,284,554 and 6,103,554. These references all relate to the electrochemical micromachining of a sample. Wherein, the Taiwan Pat. No. I223350 discloses a completely submerged electroetching apparatus used for the electroetching of a relative large surface, in which a workpiece is served as anode and is connected to a positive electrode of a power supply, and an electrolyte solution is connected to a negative electrode of the power supply. In practice, however, a completely submerged electroetching system tends to pose certain problems including high power requirements. In order to alleviate such problems, the U.S. Pat. Nos. 5,284,554 and 6,103,554 each discloses an electroetching system which progressively treats only a small portion of the wafer to be etched. To this end, a multi-nozzle cathode assembly is provided which has a small width relative to the overall dimensions of the surface to be etched. This cathode assembly is then used to deliver the electrolyte to limited portions of the surfaces as the nozzle assembly is scanned across the surface of the wafer.
Heretofore the electrolytic etching techniques have been practiced by the workpiece (anode) in touch with the positive electrode terminal of the power supply, which poses many limits to an automated continuous process.
What is desired, therefore, is an electrolytic system for removing metallic material effectively and completely and for suitably applying to the automated continuous process.
It is therefore an object of this invention to provide an improved recycling system and method which can be used to recycle a workpiece without the secondary pollution.
It is another objective of this invention is to provide an improved electrolytic assembly and method for removing metal from the surface of the workpiece selectively and efficiently.
It is still another objective of this invention to provide an improved electrolytic assembly adapted to an automated continuous process.
To achieve these and other objects, the present invention provides a system for recycling a workpiece, comprising an electrolytic etching assembly for etching a metal layer of the workpiece. The electrolytic etching assembly has an electroetching unit, a working stage, a power supply and an electrolyte source supply. The electroetching unit has an anode, a cathode next to the anode and an insulting covering, wherein the cathode and the anode are separated by the insulting covering which covers the anode. The working stage is provided for carrying the workpiece so as to allow the metal layer to face the anode and the cathode. The power supply has a positive electrode connected with the anode of the electroetching unit, and a negative electrode connected with the cathode. In addition, the electrolyte source supply is communicated with the insulting covering of the electroetching unit, and pours an electrolyte solution onto the anode and thereafter impinging upon the workpiece and passing through a passage defined by the workpiece and the anode.
In this state, the electroetching unit of the electrolytic assembly is used to both deliver the electrolyte solution and scan across a surface, i.e. metal layer, of the workpiece, while contacting with the workpiece by neither the anode nor the cathode, so called “Contactless Electrolytic Etching Method”.
Preferably, the system further comprises a chemical stripping assembly for etching the organic layer of the workpiece. This means the present invention treats the metal layer and the organic layer separately; thereby cause not the secondary pollution when compared with the prior arts.
Preferably, the system further comprises a metal recycling unit for recycling a metal material of the metal layer, such as a noble metal, or for restoring the electrolytic solution.
Preferably, the system further comprises a waste treatment assembly for recycling an organic waste generated from the chemical stripping assembly.
A method of recycling a workpiece of an organic-inorganic composite sheet consistent with the present invention comprises steps of electroetching a metal layer of the workpiece; and chemically stripping an organic layer of the workpiece. Thus, it is possible to avoid the secondary pollution while recycling a substrate with an organic-inorganic composite film.
Further benefits and advantages of the present invention will become apparent after a careful reading of the detailed description with appropriate reference to the accompanying drawings.
The invention will now be elucidated by reference to the following description, appended claims, and accompanying drawings where
With reference to
As can be seen from the
The working stage 2 is provided for carrying the workpiece 8 so as to allow the metal layer 81 of the workpiece 8 to face upwardly to the anode 10 and the cathodes 11. The power supply 3 has a positive electrode (presented by a plus sign) connected with the anode 10 of the electroetching unit 1, and a negative electrode (presented by a minus sign) connected with the cathodes 11, thereby provides power for the need of electrolysis. The electrolyte source supply 4 is communicated with the insulting covering 12 of the electroetching unit 1, and pours an electrolyte solution 41 onto the anode 10 and thereafter impinging upon the workpiece 8 and passing through a passage 14 defined by the workpiece 8 and the cathodes 11. In other words, the passage 14 is continuously filled with the electrolyte solution 41 in a steady state so that the anode 10, the cathodes 11 and the metal layer 81 get electrically connected together via the electrolyte solution 41. Accordingly, a specific portion of the metal layer 81, which sits directly underneath the anode 10, will be etched due to the electrolysis via the electrolytic solution 41 which pours from the anode 10. It should be understood that neither the anode 10 nor the cathodes 11 contact directly with the workpiece, which differs from those of the prior arts. The present invention is a pioneer in deploying the innovative “Contactless Electrolytic Etching Method”.
In order to act steadily without being corroded seriously, the anode 10 is made of an insert material, such as platinum or semiconductor materials. Furthermore, the anode 10 may be arranged to be capable of rotation in order to prolong a period of time. While rotating, outer peripheral surfaces of the anode 10 can be corroded lightly and evenly as time processes. Thus, the rotatable anode 10 can has a longer lift span when compared with the stationary one, and can perform a better, uniform etching effect.
In addition, either the electroetching unit 1 or the working stage 2 may be movable in a lateral direction in order that the electrolytic solution 41 can be impinged against the entire metal layer 81 by either moving the electroetching unit 1 laterally over the working stage 2, as depicted in
Referring to
Alternatively, as shown in
Referring back to the
Referring back to
Referring back to
Oxidation reaction of the metal layer 81:
M→M+Z+z e−
In the meantime, a portion of the metal ions dissolved in the electrolyte solutions 41 are herein reduced into metal atoms, namely the electroplated metals, and deposited onto a side of the cathodes 11. Such a reaction, for example, is represented as follows:
First reduction reaction: (a portion of the metal ions)
M+Z+z e−→M
Next, a worker can easily take out the electroplated metals from the side of the cathodes 11 by using a scraper and bring to the selective smelter 4 which is capable of melting and separating a first metal (M1) from electroplated metals. Take the color filter substrate as an example, the Indium metal has a lower melting point (156.60° C.) than that of the Sn metal (231.91° C.) so that the Indium metal can be melted out first to separate from the Sn metal.
Another portion of the metal ions dissolved in the electrolyte solutions 41 is drained out from the reservoir 5 and is passed to the filtration unit 21 which is provided for purifying the used electrolyte solution 41 by a filter material thereof, and then is passed to the settling tank 22 where particles suspended in the electrolyte solution 13 are allowed to sink to the bottom of the reservoir 5 for another purification. Accordingly, after the double purification by the filtration unit 21 and the settling tank 22, the clean electrolyte solution 41 containing the other portion of the metal ions is derived.
Next, the clean electrolyte solution 41 may be brought into the electroplating assembly 30 which is capable of applying a specific bias voltage to educe a second metal (M2) from the clean electrolyte solution 41. The general chemical reaction herein is the same with the first reduction reaction happened in the electrolytic etching assembly 100 and is herein presented again as:
Second reduction reaction: (another portion of the metal ions)
M+Z+z e−→M
As depicted in
After the metal ions are taken out from the electrolyte solution 41 by electroplating, the electrolyte solution 41 which contains no or less metal ions can be either returned back to the electrolytic etching assembly 100 by a conduit 17, as shown in
In order to purify the first metal (M1) and the second metal (M2), which are specially made of the same chemical element, such as a noble metal Indium, and are respectively generated from the cathode 11 of electrolytic etching assembly 100 and the electroplating assembly 30, the recycling system further comprises a refining furnace 50 for using heat to refine the metals M1 and M2 to a ultra-pure metal.
In the foregoing description, the electrolytic etching assembly 100 is used to etching the metal layer 81 of the workpiece 8 so as to recycle a reusable workpiece. And, the metal recycling unit 300 is used to recycle the metal materials of the metal layer out of the electrolyte solution 41 without causing the secondary pollution. It should be noted that the recycling system has the benefit to recycle any workpiece with a metal layer, without limits to a workpiece having both a metal layer and an organic layer, namely an organic-inorganic composite sheet.
Moreover, the chemical stripping assembly 200 of recycling system is provided for stripping the organic layer (not shown) of the workpiece 8 by using an alkaline solution, such as a Sodium Hydroxide solution, unlike a concentrated acid solution used by the prior art. The concentrated sulfuric acid can etch not only organic layers but also metal layers. However, it is to be understood that the chemical stripping assembly may still use the acid solution to strip the organic layer only if the workpiece 8 has been checked to have no metal components thereon. Thus, in the recycling system according to the present invention, the metal layer and the organic layer are processed separately in order to avoid generating toxic heavy metal contaminated waste water which causes the secondary pollution.
Referring yet again to
As noted above, the recycling system of the present invention uses the electrolytic etching assembly 100 and the chemical stripping assembly 200 to process the metal layer and the organic layer respectively so as to recycle the reusable workpiece. More particularly, the recycling system further uses the metal recycling unit 300 to recycle the metal materials and the electrolyte solution, and uses the waste treatment assembly 400 to treat the organic waste. These make the recycling system of the present invention the most ideal and environment-friendly system ever conceived.
Referring to
As for the sequence of the steps, it depends on which kind of layer is at the topmost of the workpiece 8 in consideration of environment protection. If the metal layer is on the top, the electroetching 70 is preferred to be performed first than the chemical stripping 71. On the contrary, if the organic layer is covered on the topmost, it is better to perform the step of the chemical stripping 71 first.
Next, the method further comprises steps of collecting 73 an electrolyte solution generated by electroetching 70; electroplating 75 a first metal 77 from the electrolyte solution; collecting 74 electroplated metals generated by electroetching 70; and smelting 76 the electroplated metals to separate a second metal 78 from the electroplated metals.
Suppose that the first metal 77 and the second metal 78 are noble metals made of the same chemical element, the method may further comprising steps of refining 79 the first metal and the second metal so as to return the metals 77, 78 into a ultra-pure metal.
Moreover, the method further comprises a step of applying ozone, or UV radiations to decompose 72 organic waste generated by the chemical stripping 71. Accordingly, the organic waste may be transformed into a clean solution for recycling without polluting the environment.
Thus, the recycling system and method of the present invention is the most ideal, and environment-friendly system ever conceived.
Numerous characteristics and advantages of the invention have been set forth in the foregoing description, together with details of the structure and function of the invention, and the novel features thereof are pointed out in appended claims. The disclosure, however, is illustrative only, and changes may be made in detail, especially, in matters of shape, size and arrangement of parts, materials and the combination thereof within the principle of the invention, to the full extent indicated by the broad general meaning of the terms in which the appended claims are expressed.
Number | Date | Country | Kind |
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094126877 | Aug 2005 | TW | national |
094144992 | Dec 2005 | TW | national |