Abstract:
Exposed copper regions on a semiconductor substrate can be etched by a wet etching solution comprising (i) one or more complexing agents selected from the group consisting of bidentate, tridentate, and quadridentate complexing agents; and (ii) an oxidizer, at a pH of between about 5 and 12. In many embodiments, the etching is substantially isotropic and occurs without visible formation of insoluble species on the surface of copper. The etching is useful in a number of processes in semiconductor fabrication, including for partial or complete removal of copper overburden, for planarization of copper surfaces, and for forming recesses in copper-filled damascene features. Examples of suitable etching solutions include solutions comprising a diamine (e.g., ethylenediamine) and/or a triamine (e.g., diethylenetriamine) as bidentate and tridentate complexing agents respectively and hydrogen peroxide as an oxidizer. In some embodiments, the etching solutions further include pH adjustors, such as sulfuric acid, aminoacids, and carboxylic acids.
Abstract:
Exposed copper regions on a semiconductor substrate can be etched by a wet etching solution comprising (i) one or more complexing agents selected from the group consisting of bidentate, tridentate, and quadridentate complexing agents; and (ii) an oxidizer, at a pH of between about 5 and 12. In many embodiments, the etching is substantially isotropic and occurs without visible formation of insoluble species on the surface of copper. The etching is useful in a number of processes in semiconductor fabrication, including for partial or complete removal of copper overburden, for planarization of copper surfaces, and for forming recesses in copper-filled damascene features. Examples of suitable etching solutions include solutions comprising a diamine (e.g., ethylenediamine) and/or a triamine (e.g., diethylenetriamine) as bidentate and tridentate complexing agents respectively and hydrogen peroxide as an oxidizer. In some embodiments, the etching solutions further include pH adjustors, such as sulfuric acid, aminoacids, and carboxylic acids.
Abstract:
An electrolyte, and particularly anolyte, may be circulated via an open loop having a pressure regulator, so that the pressure in the plating chamber is maintained at a constant (or substantially constant) value with respect to atmospheric pressure. In these embodiments, a pressure regulator is in fluid communication with the anode chamber.
Abstract:
An apparatus for wet etching metal from a semiconductor wafer comprises a wafer holder for rotating a wafer and a plurality of nozzles for applying separate flow patterns of etching liquid to the surface of the wafer. The flow patterns impact the wafer in distinct band-like impact zones. The flow pattern of etching liquid from at least one nozzle is modulated during a total etching time control the cumulative etching rate in one local etch region relative to the cumulative etching rate in one or more other local etch regions. Some embodiments include a lower etch chamber and an upper rinse chamber separated by a horizontal splash shield. Some embodiments include a retractable vertical splash shield used to prevent splashing of etching liquid onto the inside walls of a treatment container. An etch-liquid delivery system includes a plurality of nozzle flow paths having corresponding nozzle flow resistances, and a plurality of drain flow paths having corresponding drain flow resistances. Nozzle flow resistances and drain flow resistances are matched so that switching the flow from a nozzle to a corresponding drain flow path does not change the flow rate of etching liquid through other nozzles. A non-wafer-contacting measuring device measures a metal thickness on a rotating semiconductor wafer during metal wet etching by immersing a plurality of electrodes in etching liquid in close proximity to the wafer surface of the rotating wafer and determining electrical resistance between a plurality of electrodes.
Abstract:
An electrolyte, and particularly anolyte, may be circulated via an open loop having a pressure regulator, so that the pressure in the plating chamber is maintained at a constant (or substantially constant) value with respect to atmospheric pressure. In these embodiments, a pressure regulator is in fluid communication with the anode chamber.
Abstract:
Disclosed are pre-wetting apparatus designs and methods. These apparatus designs and methods are used to pre-wet a wafer prior to plating a metal on the surface of the wafer. Disclosed compositions of the pre-wetting fluid prevent corrosion of a seed layer on the wafer and also improve the filling rates of features on the wafer.
Abstract:
Apparatus and methods for electroplating metal onto substrates are disclosed. The electroplating apparatus comprise an electroplating cell and at least one oxidization device. The electroplating cell comprises a cathode chamber and an anode chamber separated by a porous barrier that allows metal cations to pass through but prevents organic particles from crossing. The oxidation device (ODD) is configured to oxidize cations of the metal to be electroplated onto the substrate, which cations are present in the anolyte during electroplating. In some embodiments, the ODD is implemented as a carbon anode that removes Cu(I) from the anolyte electrochemically. In other embodiments, the ODD is implemented as an oxygenation device (OGD) or an impressed current cathodic protection anode (ICCP anode), both of which increase oxygen concentration in anolyte solutions. Methods for efficient electroplating are also disclosed.
Abstract:
An electrolyte, and particularly anolyte, may be circulated via an open loop having a pressure regulator, so that the pressure in the plating chamber is maintained at a constant (or substantially constant) value with respect to atmospheric pressure. In these embodiments, a pressure regulator is in fluid communication with the anode chamber.
Abstract:
An apparatus for continuous simultaneous electroplating of two metals having substantially different standard electrodeposition potentials (e.g., for deposition of Sn—Ag alloys) comprises an anode chamber for containing an anolyte comprising ions of a first, less noble metal, (e.g., tin), but not of a second, more noble, metal (e.g., silver) and an active anode; a cathode chamber for containing catholyte including ions of a first metal (e.g., tin), ions of a second, more noble, metal (e.g., silver), and the substrate; a separation structure positioned between the anode chamber and the cathode chamber, where the separation structure substantially prevents transfer of more noble metal from catholyte to the anolyte; and fluidic features and an associated controller coupled to the apparatus and configured to perform continuous electroplating, while maintaining substantially constant concentrations of plating bath components for extended periods of use.
Abstract:
Disclosed are pre-wetting apparatus designs and methods. These apparatus designs and methods are used to pre-wet a wafer prior to plating a metal on the surface of the wafer. Disclosed compositions of the pre-wetting fluid prevent corrosion of a seed layer on the wafer and also improve the filling rates of features on the wafer.