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Briend
Anne Francoise Violette Briend, Orbe CH
| Patent application number | Description | Published |
|---|---|---|
| 20110039007 | INSTANT BEVERAGE PRODUCT - The present invention relates to an instant beverage powder and, more particularly, to an instant soluble beverage powder which forms foam on its upper surface when reconstituted with water. The powder has a foaming porosity of at least 35% an open pore volume of less than 3 ml/g and a closed pore average diameter D | 02-17-2011 |
Emmanuel Cyrille Pascal Briend, Cambridge GB
| Patent application number | Description | Published |
|---|---|---|
| 20100303867 | A COMPOSITION COMPRISING A NOTCH LIGAND AND AN ALLERGENB OR ALLERGEN BYSTANDER ANTIGEN - A method is provided for reducing an immune response to an allergen or antigenic determinant thereof in a mammal by administering a modulator of the Notch signalling pathway. | 12-02-2010 |
Pierre Briend, Seyssinet FR
| Patent application number | Description | Published |
|---|---|---|
| 20100192627 | Method And Device For The Cryogenic Separation Of A Methane-Rich Flow - A method and device for the cryogenic separation of a methane-rich flow is provided. | 08-05-2010 |
| 20110011129 | METHOD FOR RECYCLING SILANE (SiH4) - The invention relates to a method for recycling silane that comprises the following consecutive steps: a) injecting a mixture of pure silane/pure hydrogen (SiH4/H2) in a reaction chamber for making silicon-containing thin layers; b) extracting from the mixture the excess of silane not used during step a)/hydrogen (SiH4/H2) via a pump using a supply gas; c) discharging from said pump, at a pressure close to the atmospheric pressure, a mixture containing at least silane (SiH4), hydrogen (H2) and an amount different from zero of said supply gas; d) separating the silane (SiH4) from the hydrogen/supply gas mixture resulting from the mixture from step c), the silane thus obtained containing less than 100 ppm of supply gas, preferably less than 10 ppm of supply gas and more preferably less than 1 ppm of supply gas; characterised in that at least 50%, preferably 70%, and more preferably 80% of the silane (SiH4) from step b) is reused after step d) for a new step a). | 01-20-2011 |