Process coating module

Figure4.108 Coating module (processing from left to right 1, unwinding 2, coating 3, drying compartment with temperature sensor 4, additional driven roller pair 5, up-winding) and continuous etched foil (length 72 m, width 150 mm, thickness 300 pm, structure dimensions breadth x height x length = 300 x 200 x 10000 pm and 500 x 300 x 5000 pm) [109].

As with ah thin-film PV technologies, the projected manufacturing costs of a-Si H ahoy PV modules fah rapidly with annual manufacturing volume, ie, MWp /yr. The primary driver of this volume cost reduction is the volume—cost relationship of commercially available thin-film processing equipment. Thin-film coating machines often have capacities equivalent to 3—5 yr, so that manufacturing economies of scale are more fully realized at the... 

Extracellular ligands (hormones, neurotrophins, carrier protein, adhesion molecules, small molecules, etc.) will bind to specific transmembrane receptors. This binding of specific ligand induces the concentration of the receptor in coated pits and internalization via clathrin-coated vesicles. One of the best studied and characterized examples of RME is the internalization of cholesterol by mammalian cells [69]. In the nervous system, there are a plethora of different membrane receptors that bind extracellular molecules, including neurotrophins, hormones and other cell modulators, being the best studied examples. This type of clathrin-mediated endocytosis is an amazingly efficient process, capable of concentrating... 

Research effort at Albany International Research Co. has developed unit processes necessary for pilot scale production of several species of reverse osmosis hollow fiber composite membranes. These processes include spin-dope preparation, a proprietary apparatus for dry-jet wet-spinning of microporous polysul-fone hollow fibers, coating of these fibers with a variety of permselective materials, bundle winding using multifilament yarns and module assembly. Modules of the membrane identified as Quantro II are in field trial against brackish and seawater feeds. Brackish water rejections of 94+% at a flux of 5-7 gfd at 400 psi have been measured. Seawater rejections of 99+% at 1-2 gfd at 1000 psi have been measured. Membrane use requires sealing of some portion of the fiber bundle for installation in a pressure shell. Much effort has been devoted to identification of potting materials which exhibit satisfactory adhesion to the fiber while... 

Air from the compressor is split into two streams primary air is premixed with the fuel and then fed to the catalyst, which is operated under O2 defect conditions secondary air is used first as a catalyst cooling stream and then mixed with the partially converted stream from the catalyst in a downstream homogeneous section where ignition of gas-phase combustion occurs and complete fuel burnout is readily achieved. The control of the catalyst temperature below 1000 Cis achieved by means of O2 starvation to the catalyst surface, which leads to the release of reaction heat controlled by the mass transfer rate of O2 in the fuel-rich stream and of backside cooling of the catalyst with secondary air. To handle both processes, a catalyst/heat exchanger module has been developed, which consists of a bundle of small tubes externally coated with an active catalyst layer, with cooling air and fuel-rich stream flowing in the tube and in the shell side, respectively [24]. 

The whole process consists of a sequence of consecutive steps which allows separation into production modules. Some of them already exist and will just need slight modifications. Others have to be developed. At the very beginning, one makes use of the newly developed reel-to-reel etching technology for micro structured stainless-steel foils similar to the process described in [166], The structured foils are then coated with catalyst, structured again with a laser tool and finally folded by sheet metal forming to a reactor monolith. The readily mass-produced reactors will be sealed by laser welding. 

For the period of the foil shaping, the coating knife must be positioned on a section of the foil which is not structured. This prevents the slurry from delivering an undefined coat thickness and helps to seal the jet exit This is one of the reasons for the existence of the laser structuring module as this foil section will be thinned by the laser after the coating step to create a predefined joint for the subsequent folding process. 

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