US3798141A - Technique for electroetching thin film metallization - Google Patents
Technique for electroetching thin film metallization Download PDFInfo
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- US3798141A US3798141A US00298856A US3798141DA US3798141A US 3798141 A US3798141 A US 3798141A US 00298856 A US00298856 A US 00298856A US 3798141D A US3798141D A US 3798141DA US 3798141 A US3798141 A US 3798141A
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- rhodium
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- 238000000034 method Methods 0.000 title abstract description 25
- 239000010409 thin film Substances 0.000 title abstract description 18
- 238000001465 metallisation Methods 0.000 title description 7
- 238000000866 electrolytic etching Methods 0.000 title description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract description 64
- 238000005530 etching Methods 0.000 abstract description 36
- 229910052697 platinum Inorganic materials 0.000 abstract description 32
- 229910052737 gold Inorganic materials 0.000 abstract description 27
- 239000010931 gold Substances 0.000 abstract description 27
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 abstract description 26
- 229910052703 rhodium Inorganic materials 0.000 abstract description 26
- 239000010948 rhodium Substances 0.000 abstract description 26
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 abstract description 26
- 239000002253 acid Substances 0.000 abstract description 9
- 229910000510 noble metal Inorganic materials 0.000 abstract description 7
- 239000002131 composite material Substances 0.000 description 24
- 239000003792 electrolyte Substances 0.000 description 11
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 229910052723 transition metal Inorganic materials 0.000 description 5
- 229910052763 palladium Inorganic materials 0.000 description 4
- 230000004888 barrier function Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 150000003624 transition metals Chemical class 0.000 description 3
- 229940075397 calomel Drugs 0.000 description 2
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical compound Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 238000005304 joining Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- NUKYPUAOHBNCPY-UHFFFAOYSA-N 4-aminopyridine Chemical compound NC1=CC=NC=C1 NUKYPUAOHBNCPY-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- QZPSXPBJTPJTSZ-UHFFFAOYSA-N aqua regia Chemical compound Cl.O[N+]([O-])=O QZPSXPBJTPJTSZ-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000003486 chemical etching Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- FHUGMWWUMCDXBC-UHFFFAOYSA-N gold platinum titanium Chemical compound [Ti][Pt][Au] FHUGMWWUMCDXBC-UHFFFAOYSA-N 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 229920002120 photoresistant polymer Polymers 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
Images
Classifications
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K3/00—Apparatus or processes for manufacturing printed circuits
- H05K3/02—Apparatus or processes for manufacturing printed circuits in which the conductive material is applied to the surface of the insulating support and is thereafter removed from such areas of the surface which are not intended for current conducting or shielding
- H05K3/06—Apparatus or processes for manufacturing printed circuits in which the conductive material is applied to the surface of the insulating support and is thereafter removed from such areas of the surface which are not intended for current conducting or shielding the conductive material being removed chemically or electrolytically, e.g. by photo-etch process
- H05K3/07—Apparatus or processes for manufacturing printed circuits in which the conductive material is applied to the surface of the insulating support and is thereafter removed from such areas of the surface which are not intended for current conducting or shielding the conductive material being removed chemically or electrolytically, e.g. by photo-etch process being removed electrolytically
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F3/00—Electrolytic etching or polishing
- C25F3/02—Etching
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10N—ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10N97/00—Electric solid-state thin-film or thick-film devices, not otherwise provided for
Definitions
- This invention relates to a technique for electrochemically etching thin film metallizations. More particularly, the present invention relates to a technique for selectively etching thin film metallization including noble metals by electrochemical means.
- platinum has not proven as convenient to use as palladium, it has not evidenced the interdiffusion problem with gold.
- platinum was found to be very diflicult to etch and the only material found suitable for this purpose has been aqua regia, a material which attacks photoresists. Further investigation revealed that pattern delineation of the platinum containing composite could only be effected by back sputtering, a technique which is economically undesirable and which often results in the deposition of residues. Still further, back sputtering could not be used in the fabrication of MOS devices due to the likelihood of damaging the dielectric. Accordingly, the platinum composites have been utilized primarily in the fabrication of bipolar devices. Recognizing these limitations, workers in the art have focused their interest upon the development of a technique suitable for pattern delineating all noble metals with a universal etchant.
- the invention involves etching at least one thin film material selected from among gold, rhodium and platinum in a non-oxidizing electrolyte having a pH less than one by applying a potential difference between the sample to be etched and an auxiliary electrode so as to develop a potential on the sample with respect to a reference electrode which varies periodically between anupper and a lower value.
- etching of a gold-transition metal metallization composite having a barrier layer selected from the group consisting of platinum and rhodium is effected selectively in an electrolyte comprising a non-oxidizing acid having a pH less: than one.
- Composites may be etched in the described nianner in controllable fashion at a significantly higher rate than that attainable by conventional electroetching techniques, the metals being removed selectively by adjusting the height of the potential.
- FIG. l is a schematic representation of a typical system suitable for use in the practice of the present invention.
- FIG. 2 is a graphical representation on coordinates of pulse duration in seconds against etching rate in Angstroms per minute for a titanium-platinum-gold composite pulse etched in accordance with the present invention.
- an etching vessel 11 having disposed therein thin filmj composite 12 comprising an insulating substrate 13 having deposited thereon a transition metal or glue layer 14; a noble metal 15 selected from among platinum and rhodium, and patterned gold layer 16.
- An electrolyte 17 is employed in an amount sufiicient to cover the metallized composite.
- Electrolyte 17 is a non-oxidizing acid having a pH less than one. Typical acids suitable for use in the practice of the present invention are hydrochloric, sulphuric, hydrofluoric, phosphoric and the like.
- the electrical system employed includes contacting electrode 18 which is connected to layer 14, electrode 18 being insulated from electrolyte 17 by means of insulating sheath 19.
- a second electrode 20 functions as the counter or auxiliary electrode in the system and is immersed in electrolyte 17.
- the third electrode 21 is a conventional reference electrode, typically a calomel electrode, which serves to maintain the composite 12 at a controlled potential with respect to the electrolyte, thereby permitting control of the etching process.
- Each of the electrodes is shown connected to a pulsing means 22, typically a potentiostat including a pulse generator.
- the apparatus depicted in FIG.-;l is set up and etching initiated by applyingv a difference of potential between the sample and the auxiliary electrode so as to develop a potential on the sample with respect 'to the reference electrode which varies periodically between an upper and lower value.
- this potential may range from 1450 to 1600 mv. (hydrogen scale) at the upper value and from 550 to 60 mv. (hydrogen scale) at the lower value.
- the lower value may range from 55.0 to 240 mv. and from 240 to 60 mv. for rapid etching.
- the described technique may be used selectively with respect to platinum, gold and rhodium.
- the use of higher potentials ranging from 1450 to 1600 mv. results in the etching of gold, platinum and rhodium.
- the use of higher potentials ranging from 1450 to 1600 mv. results in the etching of gold, platinum and rhodium.
- the use of higher potentials ranging from 1450 to 1600 mv
- rhodium may be etched selectively with respect to platinum and gold by maintaining the upper value of potential between 900 and 1100 mv. and rhodium and platinum selectively etched with respect to gold at upper potential values ranging from 1100 to 1450 mv. (all potential being on the hydrogen scale).
- the upper limit of 1600 mv. is dictated by considerations relating to undesirable gas evolution.
- the lower potential limit is determined by etching rate considerations.
- the period of time 'that the sample is maintained at either the upper or lower potential may conveniently range from 1 to milliseconds, the shorter time periods corresponding with the higher etching rates and the converse. It has been found that platinum may he etched at 1 millisecond durations at the rate of 4000 A. per minute and rhodium at 2000 A. per minute. However at 10 millisecond durations etching of platinum may be effected at the rate of 500 A. per minute and rhodium at the rate of 250 A. per minute.
- FIG. 2 there is shown a graphical representation on coordinates of duration of time that the sample is maintained at either the upper or lower potential with respect to the reference electrode versus etching rate in Angstroms per minute for a titaniumplatinum-gold thin film composite etched in a 25 percent hydrochloric acid solution to potentials (on the hydrogen scale) from -60 to 240 mv.
- a one millisecond duration results in etching of platinum at 4000 A. per minute and at 10 milliseconds at 500 A. per minute.
- removal of the base or glue layer may also be effected by lowering the potential to a constant negative value, or by etching to a potential between 500 and 300 mv. at durations ranging from 1 to 10 milliseconds, so resulting in a universal etching bath.
- a final chemical etching step will, of course, be used as required to remove detached residues.
- EXAMPLE 1 A composite comprising successively 500 A. titanium, 500 A. platinum and 10,000 A. of gold deposited upon a ceramic substrate member was immersed in an apparatus of the type shown in FIG. 1, a 25 weight percent hydrochloric acid solution having a pH of about 1 being employed as the electrolyte.
- the auxiliary electrode was comprised of carbon and the reference electrode was a calomel electrode.
- Etching was then effected by establishing a potential of -60 mv. on the sample with respect to the reference electrode for a duration of 1 millisecond and then establishing a potential of 1600 mv. for a duration of 1 millisecond. The procedure was continued successively until the gold was removed. Then, the procedure was repeated using a lower potential value of 60 mv. and an upper value of 1240 mv. to remove the platinum at a rate of 4000 A. per minute.
- Example 2 The procedure of Example 1 was repeated using a duration of 10 milliseconds. The platinum was etched controllably at the rate of 500 A. per minute.
- EXAMPLE 3 The procedure of Example 2 was repeated using a composite comprising 500 A. of rhodium rather than platinum, the rhodium being etched using a duration of 10 milliseconds at a rate of 250 A. per minute.
- Technique for electrochemical etching of a thin film selected from the group consisting of gold, platinum and rhodium which comprises immersing said thin film together with an auxiliary electrode and a reference electrode in an electrolyte comprising an acid having a pH less than one and etching the thin film by applying a difference of potential between the thin film and the auxiliary electrode so as to devlop a potential on the thin film with respect to the reference electrode which varies periodically between an upper value ranging up to 1600 mv. and a lower value ranging down to 60 mv., the potentials being on the hydrogen scale, the upper value of the potential ranging from 900 to 1100 mv.
- Technique for electrochemical etching of a goldtransition metal thin film composite having a noble metal selected from the group consisting of platinum and rhodium deposited intermediate the gold and the transition metal which comprises immersing the composite together with an auxiliary electrode and a reference electrode in an electrolyte comprising an acid having a pH less than one and etching the composite by applying a difference of potential between the composite and the auxiliary electrode so as to develop a potential on the composite with respect to the reference electrode which varies periodically between an upper value ranging up to 1600 mv. and a lower value ranging down to -60 mv., the potentials being on the hydrogen scale, the upper value of the potential ranging from 900 to 1100 mv.
- a technique for pattern delineation of a thin film composite comprising an insulating substrate having deposited thereon a transition metal, a noble metal selected from the group consisting of platinum and rhodium and a patterned gold layer which comprises immersing the composite together with an auxiliary electrode and a reference electrode in an electrolyte comprising an acid having a pH less than one and etching the composite by applying a difference of potential between the composite and the auxiliary electrode so as to develop a potential on the composite with respect to the reference electrode which varies periodically between an upper value ranging up to 1600 mv. and a lower value ranging down to -60 mv., the potentials being on the hydrogen scale, the upper value of the potential ranging from 900 to 1100 mv.
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- Manufacturing & Machinery (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Computer Hardware Design (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- Power Engineering (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- ing And Chemical Polishing (AREA)
- Weting (AREA)
- Manufacturing Of Printed Circuit Boards (AREA)
Abstract
PATTERN DELINEATION OF THIN FILM METALLIZATIONS INCLUDING GOLD, PLATINUM AND RHODIUM IS EFFECTED ELECTROLYTICALLY IN THE PRESENCE OF A STONG ACID HAVING A PH LESS THAN ONE. THE DESCRIBED TECHNIQUE PERMITS CONTROLLED ETCHING OF NOBLE METALS WHICH HERETOFORE HAVE BEEN ETCHED ONLY WITH DIFFICULTY.
D R A W I N G
D R A W I N G
Description
J. YAHALOM -March 19, 1974 TECHNIQUE FOR ELECTROETCHING THIN FILM METALLIZATION Filed Oct. 19, 1972 FIG.
W I MBW;
FIG. 2
ES V E2 @555 0 W 0 E w W T F. B) 0 E 0 6H 1 N( M Lm U 0 P l 4 C2 H+ 00 T 0 w H 0 nu m Q W 0 0 0 O 0. Q 0 Q 0 0 Q 0 0 O 4 3 2 PULSE DURATION (SEC) 3,798,141 Patented Mar. 19, 1974 United States Patent Office 3,798,141 TECHNIQUE FOR ELECTROETCHING THIN FILM METALLIZATION Joseph Yahalom, Maplewood, N.J., assignor to Bell Telephone Laboratories, Incorporated, Murray Hill, NJ. Filed Oct. 19, 1972, Ser. No. 298,856 Int. Cl. C23b 3/02 US. Cl. 204-12943 7 Claims ABSTRACT OF THE DISCLOSURE Pattern delineation of thin film metallizations including gold, platinum and rhodium is effected electrolytically in the presence of a strong acid having a pH less than one. The described technique permits controlled etching of noble metals which heretofore have been etched only with difiiculty.
This invention relates to a technique for electrochemically etching thin film metallizations. More particularly, the present invention relates to a technique for selectively etching thin film metallization including noble metals by electrochemical means.
In recent years miniaturization of components and circuitry coupled with the increasing complexity of modern electronic systems have created an unprecedented demand for reliability in thin film circuitry and the need for the total exploitation of the technology. This is particularly true in the case of lead attachment which has long been recognized as being a critical factor in the stability of circuit characteristics.
Early workers in the art recognized that the metallurgical compatibility of the various metallic constituents of the joining and conducting system played a prominent role in determining the parameters of interest, so motivating the use of a single metal for this purpose. Although such systems were found to be ideal from a metallurgical standpoint, they sulfered from inherent defects in that the manufacturer was necessarily restricted from the standpoint of obtaining optimum circuit characteristics. Accordingly, the interest of workers in the art was focused upon multimetal joining or conducting systems.
Unfortunately, studies have revealed that thermal degradation of adhesion of gold-transition metal thin film composites often occurs, such being attributed to diffusion and migration affects. In order to obviate this limitation, workers in the art proposed inserting a barrier, typically platinum or palladium between the gold and the other member of the composite. Although rhodium was also considered for this purpose, attempts at pattern delineation proved fruitless. 7
Studies of composites prepared utilizing palladium as the barrier layer revealed that interdiflusion between the gold and the palladium occurred at high temperatures, thereby resulting in a reduction in the conductivity of the gold and altering circuit parameters.
Although platinum has not proven as convenient to use as palladium, it has not evidenced the interdiffusion problem with gold. However, platinum was found to be very diflicult to etch and the only material found suitable for this purpose has been aqua regia, a material which attacks photoresists. Further investigation revealed that pattern delineation of the platinum containing composite could only be effected by back sputtering, a technique which is economically undesirable and which often results in the deposition of residues. Still further, back sputtering could not be used in the fabrication of MOS devices due to the likelihood of damaging the dielectric. Accordingly, the platinum composites have been utilized primarily in the fabrication of bipolar devices. Recognizing these limitations, workers in the art have focused their interest upon the development of a technique suitable for pattern delineating all noble metals with a universal etchant.
In accordance with the present invention, this end has been attained by means of a novel electrochemical etching technique Briefly, the invention involves etching at least one thin film material selected from among gold, rhodium and platinum in a non-oxidizing electrolyte having a pH less than one by applying a potential difference between the sample to be etched and an auxiliary electrode so as to develop a potential on the sample with respect to a reference electrode which varies periodically between anupper and a lower value. In a preferred em bodiment, etching of a gold-transition metal metallization composite having a barrier layer selected from the group consisting of platinum and rhodium is effected selectively in an electrolyte comprising a non-oxidizing acid having a pH less: than one. Composites may be etched in the described nianner in controllable fashion at a significantly higher rate than that attainable by conventional electroetching techniques, the metals being removed selectively by adjusting the height of the potential.
The invention will be more readily understood by reference to the following detailed description taken in conjunction With the accompanying drawing wherein:
FIG. lis a schematic representation of a typical system suitable for use in the practice of the present invention; and
FIG. 2 is a graphical representation on coordinates of pulse duration in seconds against etching rate in Angstroms per minute for a titanium-platinum-gold composite pulse etched in accordance with the present invention.
With reference now more particularly to FIG. 1 there is shown an etching vessel 11 having disposed therein thin filmj composite 12 comprising an insulating substrate 13 having deposited thereon a transition metal or glue layer 14; a noble metal 15 selected from among platinum and rhodium, and patterned gold layer 16. An electrolyte 17 is employed in an amount sufiicient to cover the metallized composite. Electrolyte 17 is a non-oxidizing acid having a pH less than one. Typical acids suitable for use in the practice of the present invention are hydrochloric, sulphuric, hydrofluoric, phosphoric and the like. The electrical system employed includes contacting electrode 18 which is connected to layer 14, electrode 18 being insulated from electrolyte 17 by means of insulating sheath 19. A second electrode 20 functions as the counter or auxiliary electrode in the system and is immersed in electrolyte 17. The third electrode 21 is a conventional reference electrode, typically a calomel electrode, which serves to maintain the composite 12 at a controlled potential with respect to the electrolyte, thereby permitting control of the etching process. Each of the electrodes is shown connected to a pulsing means 22, typically a potentiostat including a pulse generator.
In the operation of the process, the apparatus depicted in FIG.-;l is set up and etching initiated by applyingv a difference of potential between the sample and the auxiliary electrode so as to develop a potential on the sample with respect 'to the reference electrode which varies periodically between an upper and lower value. With respect to the composite described herein, this potential may range from 1450 to 1600 mv. (hydrogen scale) at the upper value and from 550 to 60 mv. (hydrogen scale) at the lower value. Studies have revealed that for slow etching, the lower value may range from 55.0 to 240 mv. and from 240 to 60 mv. for rapid etching. It has also been found that the described technique may be used selectively with respect to platinum, gold and rhodium. Thus, the use of higher potentials ranging from 1450 to 1600 mv. results in the etching of gold, platinum and rhodium. However,
rhodium may be etched selectively with respect to platinum and gold by maintaining the upper value of potential between 900 and 1100 mv. and rhodium and platinum selectively etched with respect to gold at upper potential values ranging from 1100 to 1450 mv. (all potential being on the hydrogen scale). The upper limit of 1600 mv. is dictated by considerations relating to undesirable gas evolution. The lower potential limit is determined by etching rate considerations. The period of time 'that the sample is maintained at either the upper or lower potential may conveniently range from 1 to milliseconds, the shorter time periods corresponding with the higher etching rates and the converse. It has been found that platinum may he etched at 1 millisecond durations at the rate of 4000 A. per minute and rhodium at 2000 A. per minute. However at 10 millisecond durations etching of platinum may be effected at the rate of 500 A. per minute and rhodium at the rate of 250 A. per minute.
With reference now to FIG. 2, there is shown a graphical representation on coordinates of duration of time that the sample is maintained at either the upper or lower potential with respect to the reference electrode versus etching rate in Angstroms per minute for a titaniumplatinum-gold thin film composite etched in a 25 percent hydrochloric acid solution to potentials (on the hydrogen scale) from -60 to 240 mv. It will be noted that a one millisecond duration results in etching of platinum at 4000 A. per minute and at 10 milliseconds at 500 A. per minute. It will be understood that removal of the base or glue layer may also be effected by lowering the potential to a constant negative value, or by etching to a potential between 500 and 300 mv. at durations ranging from 1 to 10 milliseconds, so resulting in a universal etching bath. A final chemical etching step will, of course, be used as required to remove detached residues.
Examples of the present invention are described in detail below. These examples are included merely to aid in the understanuing of the invention and variations may be made by one skilled in the art without departing from the spirit and scope of the invention.
EXAMPLE 1 A composite comprising successively 500 A. titanium, 500 A. platinum and 10,000 A. of gold deposited upon a ceramic substrate member was immersed in an apparatus of the type shown in FIG. 1, a 25 weight percent hydrochloric acid solution having a pH of about 1 being employed as the electrolyte. The auxiliary electrode was comprised of carbon and the reference electrode was a calomel electrode. Etching was then effected by establishing a potential of -60 mv. on the sample with respect to the reference electrode for a duration of 1 millisecond and then establishing a potential of 1600 mv. for a duration of 1 millisecond. The procedure was continued successively until the gold was removed. Then, the procedure was repeated using a lower potential value of 60 mv. and an upper value of 1240 mv. to remove the platinum at a rate of 4000 A. per minute.
EXAMPLE 2 The procedure of Example 1 was repeated using a duration of 10 milliseconds. The platinum was etched controllably at the rate of 500 A. per minute.
EXAMPLE 3 EXAMPLE 4 The procedure of Example 2 was repeated using a composite comprising 500 A. of rhodium rather than platinum, the rhodium being etched using a duration of 10 milliseconds at a rate of 250 A. per minute.
What is claimed is:
1. Technique for electrochemical etching of a thin film selected from the group consisting of gold, platinum and rhodium which comprises immersing said thin film together with an auxiliary electrode and a reference electrode in an electrolyte comprising an acid having a pH less than one and etching the thin film by applying a difference of potential between the thin film and the auxiliary electrode so as to devlop a potential on the thin film with respect to the reference electrode which varies periodically between an upper value ranging up to 1600 mv. and a lower value ranging down to 60 mv., the potentials being on the hydrogen scale, the upper value of the potential ranging from 900 to 1100 mv. for selective etching of rhodium with respect to platinum and gold, 1100 to 1450 mv. for selective etching of rhodium and platinum with respect to gold and from 1450 to 1600 mv. for etching of rhodium, platinum and gold.
2. Technique for electrochemical etching of a goldtransition metal thin film composite having a noble metal selected from the group consisting of platinum and rhodium deposited intermediate the gold and the transition metal which comprises immersing the composite together with an auxiliary electrode and a reference electrode in an electrolyte comprising an acid having a pH less than one and etching the composite by applying a difference of potential between the composite and the auxiliary electrode so as to develop a potential on the composite with respect to the reference electrode which varies periodically between an upper value ranging up to 1600 mv. and a lower value ranging down to -60 mv., the potentials being on the hydrogen scale, the upper value of the potential ranging from 900 to 1100 mv. for selective etching of rhodium with respect to platinum and gold, 1100 to 1450 mv. for selective etching of rhodium and platinum with respect to gold and from 1450 to 1600 mv. for etching of rhodium, platinum and gold.
3. Technique in accordance with claim 2 wherein said potential varies at a periodicity ranging from 1 to 10 milliseconds.
4. Technique in accordance with claim 3 wherein said lower value ranges from 550 to --60 mv.
5. Technique in accordance with claim 3 wherein said upper value ranges from 1450 to 1600 mv.
6. Technique in accordance with claim 2 wherein said acid is hydrochloric acid.
7. A technique for pattern delineation of a thin film composite comprising an insulating substrate having deposited thereon a transition metal, a noble metal selected from the group consisting of platinum and rhodium and a patterned gold layer which comprises immersing the composite together with an auxiliary electrode and a reference electrode in an electrolyte comprising an acid having a pH less than one and etching the composite by applying a difference of potential between the composite and the auxiliary electrode so as to develop a potential on the composite with respect to the reference electrode which varies periodically between an upper value ranging up to 1600 mv. and a lower value ranging down to -60 mv., the potentials being on the hydrogen scale, the upper value of the potential ranging from 900 to 1100 mv. for selective etching of rhodium with respect to platinum and gold, 1100 to 1450 mv. for selective etching of rhodium and platinum with respect to gold and from 1450 to 1600 mv. for etching of rhodium, platinum and gold.
References Cited UNITED STATES PATENTS 3,639,217 2/19'72 Shukovsky et al. 204l29.43 X 2,890,159 6/1959 Amaya 204l29.43
FREDERICK C. EDMUNDSON, Primary Examiner US. Cl. X.R. l04-129.2
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US29885672A | 1972-10-19 | 1972-10-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3798141A true US3798141A (en) | 1974-03-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US00298856A Expired - Lifetime US3798141A (en) | 1972-10-19 | 1972-10-19 | Technique for electroetching thin film metallization |
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| Country | Link |
|---|---|
| US (1) | US3798141A (en) |
| JP (1) | JPS4974140A (en) |
| BE (1) | BE806230A (en) |
| CA (1) | CA1026704A (en) |
| DE (1) | DE2351664B2 (en) |
| FR (1) | FR2203890B1 (en) |
| GB (1) | GB1408352A (en) |
| IT (1) | IT999661B (en) |
| NL (1) | NL157062B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3898141A (en) * | 1974-02-08 | 1975-08-05 | Bell Telephone Labor Inc | Electrolytic oxidation and etching of III-V compound semiconductors |
| US4125444A (en) * | 1976-12-14 | 1978-11-14 | Inoue-Japax Research Incorporated | Electrochemical polishing method |
| US4206028A (en) * | 1976-12-14 | 1980-06-03 | Inoue-Japax Research Incorporated | Electrochemical polishing system |
| WO2002030401A2 (en) | 2000-10-11 | 2002-04-18 | Microchips, Inc. | Microchip reservoir devices and facilitated corrosion of electrodes |
| US20030217930A1 (en) * | 2002-05-24 | 2003-11-27 | Yufeng Luo | Method and apparatus for electrochemical machining |
| US6875208B2 (en) | 2001-05-31 | 2005-04-05 | Massachusetts Institute Of Technology | Microchip devices with improved reservoir opening |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL7609816A (en) * | 1976-09-03 | 1978-03-07 | Philips Nv | PROCESS OF MANUFACTURING A BODY PROVIDED WITH A GOLD PATTERN AND BODY MANUFACTURED BY THE PROCESS. |
| DE3029277C2 (en) * | 1980-08-01 | 1983-10-20 | Siemens AG, 1000 Berlin und 8000 München | Build-up of metal layers |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3566358A (en) * | 1968-03-19 | 1971-02-23 | Bevier Hasbrouck | Integrated multi-computer system |
-
1972
- 1972-10-19 US US00298856A patent/US3798141A/en not_active Expired - Lifetime
-
1973
- 1973-05-09 CA CA170,822A patent/CA1026704A/en not_active Expired
- 1973-10-15 DE DE2351664A patent/DE2351664B2/en not_active Withdrawn
- 1973-10-15 NL NL7314162.A patent/NL157062B/en unknown
- 1973-10-18 FR FR7337216A patent/FR2203890B1/fr not_active Expired
- 1973-10-18 IT IT70089/73A patent/IT999661B/en active
- 1973-10-18 BE BE136820A patent/BE806230A/en unknown
- 1973-10-19 GB GB4878373A patent/GB1408352A/en not_active Expired
- 1973-10-19 JP JP48116978A patent/JPS4974140A/ja active Pending
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3898141A (en) * | 1974-02-08 | 1975-08-05 | Bell Telephone Labor Inc | Electrolytic oxidation and etching of III-V compound semiconductors |
| US4125444A (en) * | 1976-12-14 | 1978-11-14 | Inoue-Japax Research Incorporated | Electrochemical polishing method |
| US4206028A (en) * | 1976-12-14 | 1980-06-03 | Inoue-Japax Research Incorporated | Electrochemical polishing system |
| WO2002030401A2 (en) | 2000-10-11 | 2002-04-18 | Microchips, Inc. | Microchip reservoir devices and facilitated corrosion of electrodes |
| WO2002030401A3 (en) * | 2000-10-11 | 2003-01-16 | Microchips Inc | Microchip reservoir devices and facilitated corrosion of electrodes |
| US6773429B2 (en) | 2000-10-11 | 2004-08-10 | Microchips, Inc. | Microchip reservoir devices and facilitated corrosion of electrodes |
| US6875208B2 (en) | 2001-05-31 | 2005-04-05 | Massachusetts Institute Of Technology | Microchip devices with improved reservoir opening |
| US20030217930A1 (en) * | 2002-05-24 | 2003-11-27 | Yufeng Luo | Method and apparatus for electrochemical machining |
| US7175752B2 (en) | 2002-05-24 | 2007-02-13 | Federal-Mogul Worldwide, Inc. | Method and apparatus for electrochemical machining |
| US20070051618A1 (en) * | 2002-05-24 | 2007-03-08 | Yuefeng Luo | Method and apparatus for electrochemical machining |
| US7850831B2 (en) | 2002-05-24 | 2010-12-14 | Federal Mogul World Wide, Inc. | Method and apparatus for electrochemical machining |
Also Published As
| Publication number | Publication date |
|---|---|
| NL157062B (en) | 1978-06-15 |
| FR2203890B1 (en) | 1976-07-23 |
| NL7314162A (en) | 1974-04-23 |
| DE2351664B2 (en) | 1975-09-18 |
| FR2203890A1 (en) | 1974-05-17 |
| GB1408352A (en) | 1975-10-01 |
| JPS4974140A (en) | 1974-07-17 |
| DE2351664A1 (en) | 1974-05-02 |
| BE806230A (en) | 1974-02-15 |
| CA1026704A (en) | 1978-02-21 |
| IT999661B (en) | 1976-03-10 |
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