Abstract: A structure for a chemical vapor deposition reactor desirably includes a reaction chamber having an interior, a spindle mounted in the reaction chamber, and a wafer carrier releasably mounted onto the spindle for rotation therewith. The spindle desirably has a shaft extending along a vertical rotational axis and a key projecting outwardly from the shaft. The wafer carrier preferably has a body defining oppositely-facing top and bottom surfaces and at least one wafer-holding feature configured so that a wafer can be held therein with a surface of the wafer exposed at the top surface of the body. The wafer carrier desirably further has a recess extending into the body from the bottom surface of the body and a keyway projecting outwardly from a periphery of the recess along a first transverse axis. The shaft preferably is engaged in the recess and the key preferably is engaged into the keyway.

Abstract: Wafer treatment process and apparatus is provided with a wafer carrier arranged to hold wafers and to inject a fill gas into gaps between the wafers and the wafer carrier. The apparatus is arranged to vary the composition, flow rate, or both of the fill gas so as to counteract undesired patterns of temperature non-uniformity of the wafers.

Abstract: An MOCVD reactor such as a rotating disc reactor (10) is equipped with a gas injector head having diffusers (129) disposed between adjacent gas inlets. The diffusers taper in the downstream direction. The injector head desirably has inlets (117) for a first gas such as a metal alkyl disposed in radial rows which terminate radially inward from the reactor wall to minimize deposition of the reactants on the reactor wall. The injector head desirably also has inlets (125) for a second gas such as ammonia arranged in a field between the rows of first gas inlets, and additionally has a center inlet (135) for the second gas coaxial with the axis of rotation.

Abstract: In a rotating disk reactor for growing epitaxial layers on substrate or other CVD reactor system, gas directed toward the substrates at gas inlets at different radial distances from the axis of rotation of the disk has both substantially the same gas flow rate/velocity and substantially the same gas density at each inlet. The gas directed toward portions of the disk remote from the axis may include a higher concentration of a reactant gas than the gas directed toward portions of the disk close to the axis, so that portions of the substrate surfaces at different distances from the axis receive substantially the same amount of reactant gas per unit area, and a combination of carrier gases with different relative molecular weights at different radial distances from the axis of rotation are employed to substantially make equal the gas density in each region of the reactor.

Abstract: A chemical vapor deposition reactor and method. Reactive gases, such as gases including a Group III metal source and a Group V metal source, are introduced into the chamber (10) of a rotating-disc reactor and directed downwardly onto a wafer carrier (32) and substrates (40) which are maintained at an elevated substrate temperature, typically above about 400° C. and normally about 700-1100° C. to deposit a compound such as a III-V semiconductor. The gases are introduced into the reactor at an inlet temperature desirably above about 75° C. and most preferably about 100°-350° C. The walls of the reactor may be at a temperature close to the inlet temperature. Use of an elevated inlet temperature allows the use of a lower rate of rotation of the wafer carrier, a higher operating pressure, lower flow rate, or some combination of these.

Abstract: A chemical vapor deposition reactor and method. Reactive gases, such as gases including a Group III metal source and a Group V metal source, are introduced into a rotating-disc reactor and directed downwardly onto a wafer carrier and substrates which are maintained at an elevated substrate temperature, typically above about 400° C. and normally about 700-1100° C. to deposit a compound such as a III-V semiconductor. The gases are introduced into the reactor at an inlet temperature desirably above about 75° C. and most preferably about 100°-250° C. The walls of the reactor may be at a temperature close to the inlet temperature. Use of an elevated inlet temperature allows the use of a lower rate of rotation of the wafer carrier, a higher operating pressure, lower flow rate, or some combination of these.

Abstract: A system and method for evenly heating a substrate placed in a wafer carrier used in wafer treatment systems such as chemical vapor deposition reactors, wherein a first pattern of wafer compartments is provided on the top of the wafer carrier, such as one or more rings of wafer carriers, and a second pattern of inlaid material dissimilar to the wafer carrier material is inlaid on the bottom of the wafer carrier, and the second pattern of inlaid material is substantially the opposite of the first pattern of wafer compartments, such that there are at least as many material interfaces in intermediate regions without wafer compartments as there are in wafer carrying regions with wafers and wafer compartments.

Abstract: A cleaning carrier for in-situ cleaning of a process chamber of a material deposition tool and method for in-situ cleaning using a cleaning carrier. The cleaning carrier includes a body formed symmetrically about a central axis and having a geometry generally corresponding to the geometry of the removable wafer carrier for use with the tool, and a tool interface that facilitates mounting of the cleaning carrier body on a portion of the material deposition tool that accepts the removable wafer carrier. A set of deployable and retractable brushes are operatively coupled with the cleaning carrier body via a corresponding set of deployment and retraction mechanisms, the brushes being movable between a retracted position for handling of the cleaning carrier and a deployed position for cleaning an interior surface of the process chamber.

Abstract: A chemical vapor deposition reactor and a method of wafer processing are provided. The reactor includes a reaction chamber having an interior, a gas inlet manifold communicating with the interior of the chamber, an exhaust system including an exhaust manifold having a passage and one or more ports, and one or more cleaning elements mounted within the chamber. The gas inlet manifold can admit process gasses to form a deposit on substrates held within the interior. The passage can communicate with the interior of the chamber through the one or more ports. The one or more cleaning elements are movable between (i) a run position in which the cleaning elements are remote from the one or more ports and (ii) a cleaning position in which the one or more cleaning elements are engaged in the one or more ports.

Abstract: An MOCVD reactor such as a rotating disc reactor (10) is equipped with a gas injector head having diffusers (129) disposed between adjacent gas inlets. The diffusers taper in the downstream direction. The injector head desirably has inlets (117) for a first gas such as a metal alkyl disposed in radial rows which terminate radially inward from the reactor wall to minimize deposition of the reactants on the reactor wall. The injector head desirably also has inlets (125) for a second gas such as ammonia arranged in a field between the rows of first gas inlets, and additionally has a center inlet (135) for the second gas coaxial with the axis of rotation.

Abstract: An MOCVD reactor such as a rotating disc reactor (10) is equipped with a gas injector head having diffusers (129) disposed between adjacent gas inlets. The diffusers taper in the downstream direction. The injector head desirably has inlets (117) for a first gas such as a metal alkyl disposed in radial rows which terminate radially inward from the reactor wall to minimize deposition of the reactants on the reactor wall. The injector head desirably also has inlets (125) for a second gas such as ammonia arranged in a field between the rows of first gas inlets, and additionally has a center inlet (135) for the second gas coaxial with the axis of rotation.

Abstract: A chemical vapor deposition reactor and method. Reactive gases, such as gases including a Group III metal source and a Group V metal source, are introduced into the chamber (10) of a rotating-disc reactor and directed downwardly onto a wafer carrier (32) and substrates (40) which are maintained at an elevated substrate temperature, typically above about 400° C. and normally about 700-1100° C. to deposit a compound such as a III-V semiconductor. The gases are introduced into the reactor at an inlet temperature desirably above about 75° C. and most preferably about 100°-350° C. The walls of the reactor may be at a temperature close to the inlet temperature. Use of an elevated inlet temperature allows the use of a lower rate of rotation of the wafer carrier, a higher operating pressure, lower flow rate, or some combination of these.

Abstract: A chemical vapor deposition reactor and a method of wafer processing are provided. The reactor includes a reaction chamber having an interior, a gas inlet manifold communicating with the interior of the chamber, an exhaust system including an exhaust manifold having a passage and one or more ports, and one or more cleaning elements mounted within the chamber. The gas inlet manifold can admit process gasses to form a deposit on substrates held within the interior. The passage can communicate with the interior of the chamber through the one or more ports. The one or more cleaning elements are movable between (i) a run position in which the cleaning elements are remote from the one or more ports and (ii) a cleaning position in which the one or more cleaning elements are engaged in the one or more ports.

Abstract: Wafer treatment process and apparatus is provided with a wafer carrier arranged to hold wafers and to inject a fill gas into gaps between the wafers and the wafer carrier. The apparatus is arranged to vary the composition, flow rate, or both of the fill gas so as to counteract undesired patterns of temperature non-uniformity of the wafers.

Abstract: An MOCVD reactor such as a rotating disc reactor (10) is equipped with a gas injector head having diffusers (129) disposed between adjacent gas inlets. The diffusers taper in the downstream direction. The injector head desirably has inlets (117) for a first gas such as a metal alkyl disposed in radial rows which terminate radially inward from the reactor wall to minimize deposition of the reactants on the reactor wall. The injector head desirably also has inlets (125) for a second gas such as ammonia arranged in a field between the rows of first gas inlets, and additionally has a center inlet (135) for the second gas coaxial with the axis of rotation.

Abstract: An MOCVD reactor such as a rotating disc reactor (10) is equipped with a gas injector head having diffusers (129) disposed between adjacent gas inlets. The diffusers taper in the downstream direction. The injector head desirably has inlets (117) for a first gas such as a metal alkyl disposed in radial rows which terminate radially inward from the reactor wall to minimize deposition of the reactants on the reactor wall. The injector head desirably also has inlets (125) for a second gas such as ammonia arranged in a field between the rows of first gas inlets, and additionally has a center inlet (135) for the second gas coaxial with the axis of rotation.

Abstract: A gas distribution injector for chemical vapor deposition reactors has precursor gas inlets disposed at spaced-apart locations on an inner surface facing downstream toward a substrate carrier, and has carrier openings disposed between the precursor gas inlets. One or more precursor gases are introduced through the precursor gas inlets, and a carrier gas substantially nonreactive with the precursor gases is introduced through the carrier gas openings. The carrier gas minimizes deposit formation on the injector. The carrier gas openings may be provided by a porous plate defining the surface or via carrier inlets interspersed between precursor inlets. The gas inlets may removable or coaxial.

Abstract: A chemical vapor deposition reactor and method. Reactive gases, such as gases including a Group III metal source and a Group V metal source, are introduced into a rotating-disc reactor and directed downwardly onto a wafer carrier and substrates which are maintained at an elevated substrate temperature, typically above about 400° C. and normally about 700-1100° C. to deposit a compound such as a III-V semiconductor. The gases are introduced into the reactor at an inlet temperature desirably above about 75° C. and most preferably about 100°-250° C. The walls of the reactor may be at a temperature close to the inlet temperature. Use of an elevated inlet temperature allows the use of a lower rate of rotation of the wafer carrier, a higher operating pressure, lower flow rate, or some combination of these.

Abstract: An MOCVD reactor such as a rotating disc reactor (10) is equipped with a gas injector head having diffusers (129) disposed between adjacent gas inlets. The diffusers taper in the downstream direction. The injector head desirably has inlets (117) for a first gas such as a metal alkyl disposed in radial rows which terminate radially inward from the reactor wall to minimize deposition of the reactants on the reactor wall. The injector head desirably also has inlets (125) for a second gas such as ammonia arranged in a field between the rows of first gas inlets, and additionally has a center inlet (135) for the second gas coaxial with the axis of rotation.

Abstract: A system and method for uniform deposition of material layers on wafers in a rotating disk chemical vapor deposition reaction system is provided, wherein a plurality of wafers are rotated on a susceptor at a first rate around a first axis by a first motor, and the plurality of wafers rotate independently exhibiting planetary motion at a second rate through application of a vibrational force from a vibration source in a direction transverse to the first axis of rotation.