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The simplest way to eliminate redundant data is to identify identical les or email messages and store only one instance of the data object and build pointers to it from the other instances where the duplicate data has been removed. One could argue that this type of redundant data elimination can be accomplished through disk-based synthetic backups. It is also valid to argue that the reduction in data through this method is minimal because the redundancy reduction is limited to identical les. A more advanced method tries to remove redundant chunks of data which we will call segments for the rest of this discussion. This approach attempts to eliminate the duplicate data throughout the le system by segmenting the les into multiple equal segments of a certain size determined by the application or the user. Each of the segments is then given a special identi er using a hashing algorithm. These identi ers are stored in a database. When subsequent backups occur, the process of segmentation and identi cation is repeated. However, now a comparison is conducted between the new identi ers and the existing ones. Because the identi ers are unique, whenever a match is found, an assumption is made that a similar segment exists and therefore a pointer is build to the segment and an entry is generated in the database. In this manner not only is redundant data eliminated from the backup of the client that is being backed up but it is also eliminated from the backups of all the clients in that domain. So there is only one instance of that segment stored for all the clients in that data protection domain. Another signi cant bene t occurs during the backup of a

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The Integrated Fuel Processor (IFP) This was developed by Ballard Power [40], and is a multifunctional reactor including the evaporation of a methanol/water mixture, autothermal methanol reforming and preferential oxidation (PrOx) for CO removal The device consists of a stack of identical, structured plates which divide its volume in two compartments with microstructured rectangular channels These plates are made from aluminum and copper, thus ensuring high thermal conductivity for a uniform temperature over the entire reactor volume A schematic picture of a single plate is shown in Fig 125 Liquid methanol/water mixture enters the first compartment and evaporates when heated by the exothermic PrOx reaction, which takes place on the other side of the plate The reactants are mixed with air and enter the porous section of the plates where the reforming reaction takes place as the reaction gases cross the plates.

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In the second chamber, secondary air is added and the reaction products pass over a PrOx-catalyst while exchanging heat with the first chamber The temperature of the reactor is adjusted to 280 C Proof-of-concept experiments with the IFP gave an extremely 3 high productivity of 25 mN H2/lit/h 75kWLHV,H2/lit A special powder-metallurgical fabrication method allows for producing impermeable and porous areas on the plate as required for the flow distribution, embossing the surface structure and impregnating with reforming catalyst (Cu/ZnO) in one step The plates are piled to a stack and joined by sintering However, the IFP-design is not suitable for high-temperature applications such as gasoline or methane processors Furthermore, the above-mentioned autothermal reforming processes are charged with the inherent shortcomings of the simultaneous mode with regard to product dilution and pressure limitations Therefore, the focus is set on high- temperature steam reforming.

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The potential of catalytic plate reactors with narrow channels regarding controllability, productivity and efficiency has been demonstrated in detailed theoretical studies by Zanfir and Gavriilidis [43] One crucial task in implementing the concept is the development of fabrication techniques for catalytic activation of the plates and for assembling a stack The solution of choice would be to coat the plates before joining them to a stack However, the conditions required by the common joint methods soldering or diffusion bonding would damage the catalyst, whilst the alternative of laser welding is too expensive Therefore, although coating the completely assembled reactor is often employed as the only viable solution, this is extremely difficult to control [44] and is a clear restriction of the adequacy of micro-fabricated reactors for specific applications Moreover, the suggestion of the smaller the better is not.

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The abstract CostFunction class for computing rst derivatives is:

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