Abstract: Mass-transfer rate control arrangement and method in which a process precursor mixture is produced containing carrier gas and a process precursor gas. A quantity of the process precursor present in the process precursor mixture is acoustically sensed to produce a sensor output. A dilution gas is provided and the process precursor mixture and the dilution gas are separately conveyed to a dilution point, at which a diluted mixture of the dilution gas and the process precursor mixture is achieved. A relative flow rate of the carrier gas and the dilution gas is automatically controlled in response to the sensor output such that the diluted mixture at the dilution point has a prescribed mass transfer rate of the precursor gas.

Abstract: According to embodiments, systems and methods are described herein that facilitate use of a Chemical Vapor Deposition (CVD) system continuously. The systems and methods shown herein include multiple precursor gas sources, and structures for independently connecting or disconnecting those sources for replacement. Furthermore, by providing user inputs for diluting the outputs of these multiple precursor gas sources, mixtures of precursor gas in carrier gas can be generated that have sufficiently low concentrations to be routed to a remove CVD system even at relatively low temperatures. Therefore, in embodiments many precursor gas sources, located remotely from the CVD chamber, can be independently operated and replaced as needed without interrupting a supply of precursor gas to the CVD chamber.

Abstract: Mass-transfer rate control arrangement and method in which a process precursor mixture is produced containing carrier gas and a process precursor gas. A quantity of the process precursor present in the process precursor mixture is acoustically sensed to produce a sensor output. A dilution gas is provided and the process precursor mixture and the dilution gas are separately conveyed to a diution point, at which a diluted mixture of the dilution gas and the process precursor mixture is achieved. A relative flow rate of the carrier gas and the dilution gas is automatically controlled in response to the sensor output such that the diluted mixture at the dilution point has a prescribed mass transfer rate of the precursor gas.