An apparatus that performs a film forming process includes: a rotary table having one surface on which substrates are placed and for revolving the substrates around a rotary shaft; a vacuum container configured to accommodate the rotary table and configured such that a space formed between the vacuum container and the one surface is separated into a first processing region and a second processing region, and the substrates repeatedly and alternately pass through the first and second processing regions; a vacuum chuck mechanism provided in the rotary table and including suction ports opened to placement regions on which the substrates are placed, to suction and fix the substrates, and suction flow paths provided to communicate with the suction ports; and a switching mechanism configured to switch an operation status of the vacuum chuck mechanism between a full fixed state and a selective release state.

An apparatus for depositing organic layers on a substrate includes a gas-mixing device with one or more inlets, each for supplying a gas flow consisting of previously vaporized organic molecules that are conveyed by a carrier gas and have a molar mass greater than 300 g/mol or 400 g/mol, gas diversion elements which homogeneously mix the organic molecules in the carrier gas, and an outlet from which a homogeneous gas mixture discharges. The apparatus also comprises a conveying pipe which is connected to the outlet, and a gas inlet element that has a gas distribution volume, into which the conveying pipe leads and which has a gas outlet face that has gas outlet openings and faces a substrate holder for receiving the substrate. Furthermore, layers are deposited on the substrate using such an apparatus. The lateral homogeneity of the deposited layers is improved by one of several techniques.

A thin film deposition system deposits a thin film on a substrate in a thin film deposition chamber. The thin film deposition system deposits the thin film by flowing a fluid into the thin film deposition chamber. The thin film deposition system includes a byproducts sensor that senses byproducts of the fluid in an exhaust fluid. The thin film deposition system adjusts the flow rate of the fluid based on the byproducts.

The invention relates to methods for the chemical application of coatings by the decay of gaseous compounds, in particular to methods for injecting gases into a reaction chamber. The invention also relates to means for feeding gases into a reaction chamber, said means providing for the regulation of streams of reactive gases, and ensures the possibility of obtaining multi-layer epitaxial structures having set parameters and based on nitrides of group III metals while simultaneously increasing the productivity and cost-effectiveness of the process of the epitaxial growth thereof. Before being fed into a reactor, all of the gas streams are sent to a mixing chamber connected to the reactor, and are then fed into the reactor via a flux former under laminar flow conditions. The mixing chamber and the flux former are equipped with means for maintaining a set temperature. As a result of these solutions, a gaseous mixture with set parameters is fed into the reactor, and the formation of vortices is simultaneously prevented. The maximum allowable volume of the mixing chamber is chosen to take into account the process parameters and the required rarity of heterojunctions.

Processes and apparatus are described for atmospheric pressure plasma jet deposition onto a substrate. The process comprises feeding a solution comprising a dissolved metal precursor into a plasma jet. The dissolved metal precursor comprises a precursor metal selected from Groups 2 to 16, with the proviso that the precursor metal does not comprise Mn. The plasma jet is directed towards a surface of the substrate such that material from the plasma jet becomes deposited onto the surface of the substrate. The process provides a means to manufacture conductive, semiconducting or insulating deposits on a substrate in a material-efficient manner without the need for high-temperature post-treatment steps.

A deposition apparatus, includes a chamber having at least one first gas inlet therein. A fixed chuck is installed in the chamber and an electrostatic chuck is installed on the fixed chuck. An edge ring is disposed on an edge of the electrostatic chuck. A shower head is disposed above the edge ring. A baffle is disposed above the shower head and an upper electrode is disposed above the baffle. A gas guide member is disposed above the upper electrode so that a flow path provided in the upper electrode and the first gas inlet are connected. The gas guide member has a flow path hole penetrating in upward and downward directions, and a plurality of guide holes are provided on an inner surface of the gas guide member.

Provided is a polycrystalline SiC molded body wherein the resistivity is not more than 0.050 Ωcm and, when the peak strength in a wave number range of 760-780 cm.sup.−1 in a Raman spectrum is regarded as “A” and the peak strength in a wave number range of 790-800 cm.sup.−1 in the Raman spectrum is regarded as “B”, then the peak ratio (A/B) is not more than 0.100.

A raw material supply apparatus includes: a container configured to store a solution obtained by dissolving a first solid raw material in a solvent or a dispersion system obtained by dispersing the first solid raw material in a dispersion medium; an injection part configured to spray the solution or the dispersion system to inject the solution or the dispersion system into the container; an exhaust port configured to exhaust an inside of the container; a heating part configured to heat a second solid raw material formed by removing the solvent or the dispersion medium from the solution or the dispersion system; and a deposition part provided between the injection part and the exhaust port in the container and configured to deposit the second solid raw material.

Precursor container, comprising a first volume formed by a first chamber to house precursor material, a second volume formed by a second chamber and separated from the first volume by a partition wall, and a conduit passing through the partition wall and extending from the first volume to the second volume providing the precursor material housed within the first volume with a route to the second volume following a pressure increase in the first volume. The partition wall is a gas-permeable wall allowing gas from the first volume to permeate to the second volume.

The disclosed technology relates generally to semiconductor processing and more particularly to liquid precursor injection apparatus and methods for depositing thin films. A method of injecting a liquid precursor into a thin film deposition chamber comprises delivering a vaporized liquid precursor into the thin film deposition chamber by atomizing the liquid precursor into atomized precursor droplets using a liquid injection unit and vaporizing the atomized precursor droplets into the vaporized liquid precursor in a vaporization chamber. The liquid injector unit and the liquid precursor are such that operating the liquid precursor delivery unit under a lower stability condition, including a first liquid precursor temperature at the liquid injection unit, a first liquid precursor pressure upstream of the liquid precursor injection unit and a first gas pressure downstream of the liquid precursor injection unit, causes a mass flow rate of the liquid precursor to vary by more than 10% relative to an average mass flow rate of the liquid precursor during a first time duration. Delivering the vaporized liquid precursor into the thin film deposition chamber comprises operating the liquid precursor delivery unit under a higher stability condition. The higher stability includes one or more of: a second liquid precursor temperature at the liquid injection unit that is lower than the first liquid temperature; a second liquid pressure upstream of the injection unit that is higher than the first liquid pressure; and a second gas pressure downstream of the liquid injection unit that is higher than the first Gas pressure. The higher stability is such that that the mass flow rate of the liquid precursor varies by less than 10% relative to an average mass flow rate during a second time duration having the same time duration as the first time duration.