Abstract: Described herein is a fermentation medium for production of a plant health promoting microorganism. The fermentation medium includes nicotinic acid and biotin. A concentration of nicotinic acid in the fermentation medium is at least 0.1 mg/l, and a concentration of biotin in the fermentation medium is at least 0.01 mg/l. The fermentation medium also includes methionine. A concentration of methionine in the fermentation medium is at least 0.01 g/l.

Abstract: The present invention refers to release matrices which include a material that can be released in a controlled way or with predefined kinetics into a surrounding medium, reaction vessels comprising said release matrices, and release system further comprising a medium which is able to dissolve the embedded material. The present invention further refers to the use of release matrices in several applications and the production method for such matrices. The present invention also relates to a method that al lows control of the release rate of materials from polymer matrices with several factors.

Abstract: The present invention refers to release matrices which include a material that can be released in a controlled way or with predefined kinetics into a surrounding medium, reaction vessels comprising said release matrices, and release system further comprising a medium which is able to dissolve the embedded material. The present invention further refers to the use of release matrices in several applications and the production method for such matrices. The present invention also relates to a method that al lows control of the release rate of materials from polymer matrices with several factors.

Abstract: Disclosed are a method and a device for feeding and/or discharging fluids in microreactor arrays through one or several fluid ducts that extend into each individual microreactor and can be individually controlled and regulated, in order to control, regulate, influence, and/or verify processes. The fed or discharged amounts of fluid are introduced into or discharged from the volume of the reaction liquid during a continuous shaking process and are evenly mixed as a result of the shaking process. The continuous shaking process causes sufficient mass transfer and thorough mixing of the reaction partners or fluids while the reaction is not limited or restricted by the mass transfer conditions.

Abstract: A microreactor with at least one cavity, which comprises a bottom, a side wall and an opening disposed opposite the bottom, has a cross-section intersecting the side wall parallel to the bottom, the cross-section having a shape diverging from a round, square or rectangular shape.

Abstract: A microreactor with at least one cavity, which comprises a bottom, a side wall and an opening disposed opposite the bottom, has a cross-section intersecting the side wall parallel to the bottom, the cross-section having a shape diverging from a round, square or rectangular shape.

Abstract: Disclosed are a method and a device for feeding and/or discharging fluids in microreactor arrays through one or several fluid ducts that extend into each individual microreactor and can be individually controlled and regulated, in order to control, regulate, influence, and/or verify processes. The fed or discharged amounts of fluid are introduced into or discharged from the volume of the reaction liquid during a continuous shaking process and are evenly mixed as a result of the shaking process. The continuous shaking process causes sufficient mass transfer and thorough mixing of the reaction partners or fluids while the reaction is not limited or restricted by the mass transfer conditions.