Blasiak

Joseph D. Blasiak, Fairport, NY US

Patent application number	Description	Published
20100129181	LENS HANDLER - A lens handler includes a first arm and a second arm, the first and second arms of the lens handler being moveable relative to each other to define an open position, a closed position, and a lens handling position. The lens handler also includes a power source electrically connected to the first and second arms and configured to pass an electrical current between the first and second arms when the arms are in the closed position.	05-27-2010

Patent application number	Description	Published
20090246705	DI Water Rinse of Photoresists with Insoluble Dye Content - A method of forming a pattern in a photoresist layer which contains a dye that is insoluble in the developer solution is disclosed. A rinse liquid, typically deionized water, is dispensed onto the substrate while it is rotated at less than 750 rpm. The dye in the exposed regions is carried off by the rinse liquid, and does not accumulate in corners of exposed regions at the edge of the substrate due to centrifugal action.	10-01-2009

Patent application number	Description	Published
20100301273	BIOMASS GASIFICATION METHOD AND APPARATUS FOR PRODUCTION OF SYNGAS WITH A RICH HYDROGEN CONTENT - A biomass gasification method and apparatus for production of syngas with arich hydrogen content. In the gasification process the gasification energy is supplied by the sensible heat carried by a high temperature agent combined with the heat released by the chemical reaction between calicined lime and carbon dioxide.	12-02-2010
20110078951	TWO-STAGE HIGH-TEMPERATURE PREHEATED STEAM GASIFIER - A gasifier combines two reactors using externally generated preheated high temperature steam injection into the first reactor, where the heating demand for gasification is supplied by the sensible energy from the steam. The gasifier can produce a medium and higher LCV syngas. The first reactor is a fixed bed gasification section where the coarse feedstock is gasified, and the second reactor is an entrained-bed gasification section where the liquid and fine feedstock is gasified. Solid coarse feedstock is devolatilized in the first fixed bed reactor of the gasifier with high-temperature steam, and subsequently, in the second reactor subjected to a higher temperature sufficient to crack and destroy tars and oils. Activated carbon may be formed as co-product. The gasifier may be used with various solid and liquid feedstocks. The gasifier is capable of gasifying such different feedstocks simultaneously.	04-07-2011