Abstract: High pressure spatial chemical vapor deposition apparatuses and related process are disclosed for forming thin films on a substrate. An enclosure includes plural process chambers fluidly isolated from each other by radial separating barriers. Each chamber contains a different source gas comprising one or more volatile reactive species. The substrate is supported beneath the chambers on a rotating heated susceptor. Rotation of the susceptor carries the substrate in a path which consecutively exposes the substrate to the volatile reactive species in each process chamber. The gases first mix in the gaseous boundary layer formed adjacent the substrate. A thin film gradually grows in thickness on the substrate with each successive pass and exposure to the volatile reactive species in each of the individual process chambers. The film may be grown at high pressures exceeding 1 atmosphere in some implementations. A modular design includes an outer shell and different interchangeable process inserts.

Abstract: High pressure spatial chemical vapor deposition apparatuses and related process are disclosed for forming thin films on a substrate. An enclosure includes plural process chambers fluidly isolated from each other by radial separating barriers. Each chamber contains a different source gas comprising one or more volatile reactive species. The substrate is supported beneath the chambers on a rotating heated susceptor. Rotation of the susceptor carries the substrate in a path which consecutively exposes the substrate to the volatile reactive species in each process chamber. The gases first mix in the gaseous boundary layer formed adjacent the substrate. A thin film gradually grows in thickness on the substrate with each successive pass and exposure to the volatile reactive species in each of the individual process chambers. The film may be grown at high pressures exceeding 1 atmosphere in some implementations. A modular design includes an outer shell and different interchangeable process inserts.

Abstract: A method and apparatus for growing a Group-III nitride crystal using multiple interconnected reactor vessels to modify growth conditions during the ammonothermal growth of the Group-III nitride crystal, such that, by combining two or more vessels, it is possible to modify the conditions under which the Group-III nitride crystals are grown. In addition, the reactor vessel may use carbon fiber containing materials encapsulating oxide ceramic materials as structural elements to contain the materials for growing the Group-III nitride crystals at pressures or temperatures necessary for growth of the Group-III nitride crystals.

Abstract: An ammonothermal growth of group-III nitride crystals on starting seed crystals with at least two surfaces making an acute, right or obtuse angle, i.e., greater than 0 degrees and less than 180 degrees, with respect to each other, such that the exposed surfaces together form a concave surface.

Abstract: Reactor designs for use in ammonothermal growth of group-III nitride crystals. Internal heating is used to enhance and/or engineer fluid motion, gas mixing, and the ability to create solubility gradients within a vessel used for the ammonothermal growth of group-III nitride crystals. Novel baffle designs are used for control and improvement of continuous fluid motion within a vessel used for the ammonothermal growth of group-III nitride crystals.

Abstract: Reactor designs for use in ammonothermal growth of group-III nitride crystals. Internal heating is used to enhance and/or engineer fluid motion, gas mixing, and the ability to create solubility gradients within a vessel used for the ammonothermal growth of group-III nitride crystals. Novel baffle designs are used for control and improvement of continuous fluid motion within a vessel used for the ammonothermal growth of group-III nitride crystals.

Abstract: Boron-containing compounds, gasses and fluids are used during ammonothermal growth of group-III nitride crystals. Boron-containing compounds are used as impurity getters during the ammonothermal growth of group-III nitride crystals. In addition, a boron-containing gas and/or supercritical fluid is used for enhanced solubility of group-III nitride into said fluid.

Abstract: Boron-containing compounds, gasses and fluids are used during ammonothermal growth of group-Ill nitride crystals. Boron-containing compounds are used as impurity getters during the ammonothermal growth of group-Ill nitride crystals. In addition, a boron-containing gas and/or supercritical fluid is used for enhanced solubility of group-Ill nitride into said fluid.

Abstract: A method and apparatus for growing crystals in a reactor vessel, wherein the reactor vessel uses carbon fiber containing materials as a structural element to contain the materials for growing the crystals as a solid, liquid or gas within the reactor vessel, such that the reactor vessel can withstand pressures or temperatures necessary for the growth of the crystals. The carbon fiber containing materials encapsulate at least one component of the reactor vessel, wherein stresses from the encapsulated component are transferred to the carbon fiber containing materials. The carbon fiber containing materials may be wrapped around the encapsulated component one or more times sufficient to maintain a desired pressure differential between an exterior and interior of the encapsulated component.

Abstract: A method of producing a Group-III nitride crystal by coating at least one surface of the seed with a thin wetting layer or film comprised of one or more Group-III and alkali metals.

Abstract: An ammonothermal growth of group-III nitride crystals on starting seed crystals with at least two surfaces making an acute, right or obtuse angle, i.e., greater than 0 degrees and less than 180 degrees, with respect to each other, such that the exposed surfaces together form a concave surface.

Abstract: A group-III nitride solar cell is grown on a thin piece of a group-III nitride crystal that has been mounted on a carrier comprised of a foreign material. The thin piece is a thin layer with a thickness that ranges from approximately 5 microns to approximately 300 microns.

Abstract: A method for ammonothermally growing group-III nitride crystals using an initially off-oriented non-polar and/or semi-polar growth surface on a group-III nitride seed crystal. Group-III-containing source materials and group-III nitride seed crystals are placed into a vessel, wherein the seed crystals have one or more non-polar or semi-polar growth surfaces. Group-III nitride crystals are ammonothermally grown by filling the vessel with a nitrogen-containing solvent for dissolving the source materials and transporting a fluid comprised of the solvent with the dissolved source materials to the seed crystals for growth of the group-III nitride crystals on the seed crystals. The growth surfaces are initially off-oriented growth surfaces, wherein the growth surfaces are off-oriented m-plane or highly vicinal m-plane growth surfaces. The growth surfaces of the seed crystals may be created by cutting group-III nitride crystals at a desired angle with respect to an m-plane.

Abstract: A method to improve the crystal purity of a group-I11 nitride crystal grown in an ammonothermal growth system by removing any undesired material (i.e., impurities) from within the system prior to, in-between, or after the growth steps for the group-I11 nitride crystal. Impurities are removed from the ammonothermal growth system by first bringing the impurities into solution and then removing part or all of the solution from the growth system. The result is a high purity group-I11 nitride crystal grown in the ammonothermal growth system.

Abstract: Boron-containing compounds, gasses and fluids are used during ammonothermal growth of group-Ill nitride crystals. Boron-containing compounds are used as impurity getters during the ammonothermal growth of group-Ill nitride crystals. In addition, a boron-containing gas and/or supercritical fluid is used for enhanced solubility of group-Ill nitride into said fluid.

Abstract: Reactor designs for use in ammonothermal growth of group-III nitride crystals. Internal heating is used to enhance and/or engineer fluid motion, gas mixing, and the ability to create solubility gradients within a vessel used for the ammonothermal growth of group-III nitride crystals. Novel baffle designs are used for control and improvement of continuous fluid motion within a vessel used for the ammonothermal growth of group-III nitride crystals.

Abstract: A method for controlling the relative and absolute growth rates of all possible crystallographic planes of a group-III nitride crystal during ammonothermal growth. The growth rates of the various exposed crystallographic planes of the group-III nitride crystal are controlled by modifying the environment and/or conditions within the reactor vessel, which may be subdivided into a plurality of separate zones, wherein each of the zones has their own environment and conditions. The environment includes the amount of atoms, compounds and/or chemical complexes within each of the zones, along with their relative ratios and the relative motion of the atoms, compounds and/or chemical complexes within each of the zones and among the zones. The conditions include the thermodynamic properties each of the zones possess, such as temperatures, pressures and/or densities.

Abstract: A method for adding hydrogen-containing and/or nitrogen-containing compounds to a nitrogen-containing solvent used during ammonothermal growth of group-Ill nitride crystals to offset decomposition products formed from the nitrogen-containing solvent, in order to shift the balance between the reactants, i.e. the nitrogen-containing solvent and the decomposition products, towards the reactant side.

Abstract: Reactor designs for use in ammonothermal growth of group-III nitride crystals envision a different relative placement of source materials and seed crystals with respect to each other, and with respect to the vessel containing a solvent. This placement results in a difference in fluid dynamical flow patterns within the vessel.

Abstract: The present invention provides a method for growing group III-nitride crystals wherein the group III-nitride crystal growth occurs on an etched seed crystal. The etched seed is fabricated prior to growth using a temperature profile which produces a high solubility of the group III-nitride material in a seed crystals zone as compared to a source materials zone. The measured X-ray diffraction of the obtained crystals have significantly narrower Full Width at Half Maximum values as compared to crystals grown without etch back of the seed crystal surfaces prior to growth.