Abstract: An apparatus for depositing film stacks in-situ (i.e., without a vacuum break or air exposure) are described. In one example, a plasma-enhanced chemical vapor deposition apparatus configured to deposit a plurality of film layers on a substrate without exposing the substrate to a vacuum break between film deposition phases, is provided. The apparatus includes a process chamber, a plasma source and a controller configured to control the plasma source to generate reactant radicals using a particular reactant gas mixture during the particular deposition phase, and sustain the plasma during a transition from the particular reactant gas mixture supplied during the particular deposition phase to a different reactant gas mixture supplied during a different deposition phase.

Abstract: An apparatus for depositing film stacks in-situ (i.e., without a vacuum break or air exposure) are described. In one example, a plasma-enhanced chemical vapor deposition apparatus configured to deposit a plurality of film layers on a substrate without exposing the substrate to a vacuum break between film deposition phases, is provided. The apparatus includes a process chamber, a plasma source and a controller configured to control the plasma source to generate reactant radicals using a particular reactant gas mixture during the particular deposition phase, and sustain the plasma during a transition from the particular reactant gas mixture supplied during the particular deposition phase to a different reactant gas mixture supplied during a different deposition phase.

Abstract: An apparatus for depositing film stacks in-situ (i.e., without a vacuum break or air exposure) are described. In one example, a plasma-enhanced chemical vapor deposition apparatus configured to deposit a plurality of film layers on a substrate without exposing the substrate to a vacuum break between film deposition phases, is provided. The apparatus includes a process chamber, a plasma source and a controller configured to control the plasma source to generate reactant radicals using a particular reactant gas mixture during the particular deposition phase, and sustain the plasma during a transition from the particular reactant gas mixture supplied during the particular deposition phase to a different reactant gas mixture supplied during a different deposition phase.

Abstract: An apparatus for depositing film stacks in-situ (i.e., without a vacuum break or air exposure) are described. In one example, a plasma-enhanced chemical vapor deposition apparatus configured to deposit a plurality of film layers on a substrate without exposing the substrate to a vacuum break between film deposition phases, is provided. The apparatus includes a process chamber, a plasma source and a controller configured to control the plasma source to generate reactant radicals using a particular reactant gas mixture during the particular deposition phase, and sustain the plasma during a transition from the particular reactant gas mixture supplied during the particular deposition phase to a different reactant gas mixture supplied during a different deposition phase.

Abstract: A main reservoir holds cool reactant liquid. A reaction vessel for treating a substrate is connected to the main reservoir by a feed conduit. A heater is configured to heat reactant liquid in the feed conduit before the liquid enters the reaction vessel. Preferably, the heater is a microwave heater. A recycle conduit connects the reaction vessel with the main reservoir. Preferably, a recycle cooler cools reactant liquid in the recycle conduit before the liquid returns to the main reservoir. Preferably, an accumulation vessel is integrated in the feed conduit for accumulating, heating, conditioning and monitoring reactant liquid before it enters the reaction vessel. Preferably, a recycle accumulator vessel is integrated in the recycle conduit to accommodate reactant liquid as it empties out of the reaction vessel.

Abstract: During fluid treatment of a substrate surface, a carrier/wafer assembly containing a substrate wafer closes the top of a microcell container. The carrier/wafer assembly and the container walls define a thin enclosed treatment volume that is filled with treating fluid, such as electroless plating solution. The thin fluid-treatment volume typically has a volume in a range of about from 100 ml to 500 ml. Preferably a container is heated and the treating fluid is pre-heated before being injected into the container. Preferably, the chemical composition, temperature, and other properties of fluid in the thin enclosed fluid-treatment volume are dynamically variable. A rinse shield and a rinse nozzle are located above the container. A carrier/wafer assembly in a rinse position substantially closes the top of the rinse shield.

Abstract: Methods and apparatus for reducing heat load and air exposure when using an electroless plating fluid during a plating process, are presented. An electroless plating apparatus, including an electroless plating vessel and recirculation systems, is presented. The electroless plating vessel minimizes air exposure (and thus evaporative cooling and degradation) of the electroless plating fluid while the recirculation systems minimize heat load of the electroless plating fluid.

Abstract: A chemical etching system provides a mixture of sulfuric acid and hydrogen peroxide and serves as the etchant for removing residual copper from an edge bevel region of a semiconductor wafer. The etching system includes a dilution module where concentrated sulfuric acid and concentrated hydrogen peroxide are diluted to the appropriate concentrations and then stored. To reduce the likelihood that oxygen bubbles (from hydrogen peroxide decomposition) will appear in the etchant solution, stored sulfuric acid and hydrogen peroxide are mixed immediately prior to use. In this manner, the dissolved oxygen concentration in the hydrogen peroxide decreases well below the saturation level.