Patent classifications
C04B35/12
MULTILAYER COATING FOR CORROSION RESISTANCE
Exemplary methods of coating a metal-containing component are described. The methods are developed to increase corrosion resistance and improve coating adhesion to a metal substrate. The methods include forming a bonding layer on a metal substrate, where the bonding layer includes an oxide of a metal in the metal substrate. The coating methods further include depositing a stress buffer layer on the bonding layer, where the stress buffer layer is characterized by a stress buffer layer coefficient of thermal expansion (CTE) that is less than a metal substrate CTE and a bonding layer CTE. The coating methods also include depositing an environmental barrier layer on the stress buffer layer, where a ratio of the metal substrate CTE to an environmental barrier layer CTE is greater than or about 20:1, and where the environmental barrier layer includes silicon oxide. The metal-containing components may be used in fabrication equipment for electronic devices.
MULTILAYER COATING FOR CORROSION RESISTANCE
Exemplary methods of coating a metal-containing component are described. The methods are developed to increase corrosion resistance and improve coating adhesion to a metal substrate. The methods include forming a bonding layer on a metal substrate, where the bonding layer includes an oxide of a metal in the metal substrate. The coating methods further include depositing a stress buffer layer on the bonding layer, where the stress buffer layer is characterized by a stress buffer layer coefficient of thermal expansion (CTE) that is less than a metal substrate CTE and a bonding layer CTE. The coating methods also include depositing an environmental barrier layer on the stress buffer layer, where a ratio of the metal substrate CTE to an environmental barrier layer CTE is greater than or about 20:1, and where the environmental barrier layer includes silicon oxide. The metal-containing components may be used in fabrication equipment for electronic devices.
Chromia refractory brick with carbon treatment
The disclosure provides a refractory brick system comprising a chromia refractory brick for operation in the slagging environment of an air-cooled gasifier. The chromia refractory brick comprises a ceramically-bonded porous chromia refractory having a porosity greater than 9% and having carbon deposits residing within the pores. The brick may be further comprised of Al.sub.2O.sub.3. The air-cooled gasifier generates a liquefied slag in contact with the refractory brick and generally operates at temperatures between 1250 C. and 1575 C. and pressures between 300 psi to 1000 psi, with oxygen partial pressures generally between 10.sup.4 and 10.sup.10 atm. The refractory brick performs without substantial chromium carbide or chromium metal formation in the low oxygen partial pressure environment. The inclusion of carbon without chromium carbide formation provides for significant mitigation of slag penetration and significantly reduced refractory wear.
Chromia refractory brick with carbon treatment
The disclosure provides a refractory brick system comprising a chromia refractory brick for operation in the slagging environment of an air-cooled gasifier. The chromia refractory brick comprises a ceramically-bonded porous chromia refractory having a porosity greater than 9% and having carbon deposits residing within the pores. The brick may be further comprised of Al.sub.2O.sub.3. The air-cooled gasifier generates a liquefied slag in contact with the refractory brick and generally operates at temperatures between 1250 C. and 1575 C. and pressures between 300 psi to 1000 psi, with oxygen partial pressures generally between 10.sup.4 and 10.sup.10 atm. The refractory brick performs without substantial chromium carbide or chromium metal formation in the low oxygen partial pressure environment. The inclusion of carbon without chromium carbide formation provides for significant mitigation of slag penetration and significantly reduced refractory wear.
Chromia refractory brick with carbon treatment
The disclosure provides a refractory brick system comprising a chromia refractory brick for operation in the slagging environment of an air-cooled gasifier. The chromia refractory brick comprises a ceramically-bonded porous chromia refractory having a porosity greater than 9% and having carbon deposits residing within the pores. The brick may be further comprised of Al.sub.2O.sub.3. The air-cooled gasifier generates a liquefied slag in contact with the refractory brick and generally operates at temperatures between 1250 C. and 1575 C. and pressures between 300 psi to 1000 psi, with oxygen partial pressures generally between 10.sup.4 and 10.sup.10 atm. The refractory brick performs without substantial chromium carbide or chromium metal formation in the low oxygen partial pressure environment. The inclusion of carbon without chromium carbide formation provides for significant mitigation of slag penetration and significantly reduced refractory wear.
Salt separation and destruction of PFAS utilizing reverse osmosis and salt separation
Per- and polyfluoroalkyl substances (PFAS) are destroyed by oxidation in supercritical conditions. PFAS in water is concentrated in a reverse osmosis step and salt from the resulting solution is removed in supercritical conditions prior to destruction of PFAS in supercritical conditions.
Salt separation and destruction of PFAS utilizing reverse osmosis and salt separation
Per- and polyfluoroalkyl substances (PFAS) are destroyed by oxidation in supercritical conditions. PFAS in water is concentrated in a reverse osmosis step and salt from the resulting solution is removed in supercritical conditions prior to destruction of PFAS in supercritical conditions.
Salt Separation and Destruction of PFAS Utilizing Reverse Osmosis and Salt Separation
Per-and polyfluoroalkyl substances (PFAS) are destroyed by oxidation in supercritical conditions. PFAS in water is concentrated in a reverse osmosis step and salt from the resulting solution is removed in supercritical conditions prior to destruction of PFAS in supercritical conditions.
Salt Separation and Destruction of PFAS Utilizing Reverse Osmosis and Salt Separation
Per-and polyfluoroalkyl substances (PFAS) are destroyed by oxidation in supercritical conditions. PFAS in water is concentrated in a reverse osmosis step and salt from the resulting solution is removed in supercritical conditions prior to destruction of PFAS in supercritical conditions.
Lithography-based process for the production of transparent ceramic bodies with at least two zones of different composition and transparent ceramic bodies thus obtained
It is described a process for producing transparent ceramic bodies with at least two zones having different garnet composition, in particular in which one of said zones has composition Y.sub.3AI.sub.5O.sub.12. The invention is especially useful for the production of transparent ceramic bodies having preset complex shapes and/or a controlled complex distribution of doping ions.