Method to selectively cap interconnects with indium or tin...

Semiconductor device manufacturing: process – Coating with electrically or thermally conductive material – To form ohmic contact to semiconductive material

Reexamination Certificate

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C438S678000, C438S679000

Reexamination Certificate

active

06551931

ABSTRACT:

FIELD OF THE INVENTION
The present invention relates generally to the specifically directed plating of indium and tin bronzes on copper structures, and particularly, but not by way of limitation, to coating the top surface of semiconductor interconnects with an indium, or tin bronze or an oxide thereof. The invention also relates to the interconnect so formed.
BACKGROUND
It is desirable to selectively cap copper interconnects with an alloy coating to provide improved adhesion, electromigration resistance, redundant current-strapping, improved via contact resistance, robustness, and corrosion protection. The capping must be highly selective, specifically plating only the copper wiring, so as not to require expensive and critical lithography and etching to define the cap over the interconnect and to remove it from the spaces between interconnects. Cu on-chip contacts (e.g. wire bond or C4 pads) need similar capping for robust, corrosion-resistant terminal metallurgical contact. Previously, this problem has been addressed by electroless or alloy-formed selective capping (e.g. by electroless CoP/Au, NiP/Au, or PVD-deposited In or Sn with alloying reactions to the Cu) followed by selective wet-etching. These solutions are subject to shorting across very finely-spaced interconnects. A selective process which solves this problem is the immersion (autocatalytic exchange) replacement of Cu surface atoms with Sn or other species. The Cu/Sn/O system is resistant to oxidation only to ~300° C. The Cu/In/O system of the invention is more highly resistant, with stability extending to temperatures in excess of 400° C.
In immersion (or chemical displacement) coating, the substrate, usually a metal, is coated with a film (usually metallic) from a solution that contains the coating material in ionic form. The immersion coating process does not require a separate reducing agent as in electroless or auto catalytic deposition, or electric current as in electroplating. Rather, the substrate metal acts as the reducing agent, for example as when iron (Fe) is immersed in a copper sulfate solution:
Cu
2+
+Fe→Cu+Fe
2+
Here, Fe supplies electrons to the Cu ions, reducing them to zerovalent Cu, which coats the Fe substrate. The resultant Fe
2+
ions dissolve into solution. The deposition of Cu and Fe is straightforward in that the standard electrochemical potential for CU/CU
2+
couple (0.34 V vs. the normal hydrogen electrode) is greater than that of the Fe/Fe
2+(−
0.44 V vs. the normal hydrogen electrode); since Cu is more “noble”, or thermodynamically “inert” with respect to Fe, it may be said to have a greater driving force than Fe for residing in an zerovalent state. Thus, when uncomplexed Cu
2+
ions encounter Fe metal, the Cu
2+
ions spontaneously oxidize the Fe to Fe
2+
forming zerovalent Cu, which remains on the Fe surface as a film.
The deposit thickness obtained by immersion coating is limited, since the coating metal covers the base substrate, thereby preventing access of the coating ions in solution (Cu
2+
ions in solution), and removal of the base substrate product ions (Fe
2+
in our example). Typically, coating thicknesses are in the range of 10-1000 mm.
Relatively few metals can be deposited by an immersion process, mainly because of standard potential mismatch. A well-known example is immersion deposition of tin on copper (e.g., U.S. Pat. No. 2,282,511). However, the standard potential of Sn/Sn
2+
(−0.137 V vs. the normal hydrogen electrode, NHE) is less than either the Cu/Cu
2+
(0.34 V vs. NHE) or the Cu/Cu
+
(0.51 V), indicating that Cu would tend to immersion deposit on Sn, but not Sn on Cu. Nevertheless, by complexing the Cu
+
ions in solution with a complexant such as cyanide or thiourea (often known as thiocarbamide), one can lower the standard potential of the CuL/Cu
+
couple below that of Sn/Sn
2+
. Thus, Sn now has a spontaneous tendency to immersion deposit on Cu.
The standard potential of the In/In
3+
couple is −0.34 V(NHE), and −0.126 V (NHE) for In/In
+
. However, the only stable In ion in aqueous solutions is In
3+
. The In/In
3+
couple potential (−0.34 V (NHE)) is ca. 0.2 V more negative than the of Sn/Sn
2+
(−0.137 V (NHE)), which indicates that In should be more difficult than Sn to deposit on Cu by an immersion process from solution. Immersion and/or electroless plating baths are known in the art. Bokisa et al. (U.S. Pat. No. 5,554,211) describe one such bath that differs from the present invention in that it specifically does not contain thiourea and whereas the bath of the present invention contains sulfuric acid, Bokissa et al. recite the use of fluoboric and alkane or alkanol sulfonic acids. Sricharoenchaikit et al. (U.S. Pat. No. 5,203,911) specifically require the use of low metal ion concentrations from 1 to 10 millimolar, whereas the present invention operates in the range of from about 65 to about 200 millimolar. The reference specifically recites the disadvantages of hypophosphite and alkali metals, both of which are recited in the present invention. The chemical displacement solution of King et al. (U.S. Pat. No. 5,217,751) requires, in addition to an ionic solution of the plating metal, the presence of a source of the free metal in contact with the solution. This is a disadvantage not present in the present invention. Holtzman et al. (U.S. Pat. No. 4,715,894) describe a chemical displacement composition suitable for the deposition of a layer of tin or indium. The plating solution of Senda et al. (U.S. Pat. No. 5,364,459) requires titanium salts many of which are regulated by the Toxic Substances Control Act and are likely to present disposal issues. However, each of these described systems is limited to plating a layer of metal. The problem of plating a layer of alloy was not addressed by the prior art.
As the standard and best known method for fabricating Cu interconnects is the Damascene or dual-Damascene process with electroplated Cu fill, this leaves Cu interconnects encapsulated on three sides with a refractory liner, but exposed on the top surfaces after chemical-mechanical planarization. If the top surface could also be capped with a highly adhesive, corrosion-resistant metal, then reliability would be improved, and as well there would be more freedom in the choices for subsequent processing steps, which might attack or corrode exposed Cu and could not be used in the uncapped case. It is thus desirable to selectively cap Cu interconnects with indium or tin bronze or oxides and to provide a method of controllably and selectively depositing the In or Sn bronze in very thin layers only on the exposed surfaces of Cu interconnects. Such undesired coating on the insulating surfaces between the interconnects would lead to unwanted electrical shorts. To eliminate these shorts, either an additional masking step and etching, or a selective etching step without masking would be required to removed this undesired In or Sn coating.
Due to the existence and commercial availability of an immersion Sn plating bath for Cu, the immersion-plated Cu/Sn/Au ternary system is known, and was studied here specifically for the new application of terminal wire bond metallurgy on Cu interconnects. The Au is necessary to prevent native Sn oxides from preventing good wire bonding by the thermal/ultrasonic ball-bonding or wedge-bonding techniques. The Cu—Sn—Au ternary compound layer has been investigated as a protective layer covering Cu interconnects for wire bonding, and for probe damage resistance, oxidation resistance, and as a Cu diffusion barrier. The proposed compound layer is formed by selective immersion Sn coating on Cu terminal pads formed by the Damascene process during the normal course of Cu interconnect fabrication, followed by immersion (and/or electroless) Au coating and appropriate annealing steps. RBS analysis has been used to follow the reaction products of the ternary system. The initial thickness

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