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n Username and Password The administrative login and password that you will use to administer CPG. n Email Address The administrator s (your) e-mail address. n MySQL Host The server name that CGP will connect to for the database. In this case, you want to use localhost. n MySQL Database Name The name of the database that you created in Step 2. (In the example, I used cpg.) n MySQL Username and Password The username and password that you created in Step 2 for accessing the database. (In the example, I used cpg and mypassword, respectively.) n MySQL table prefix The prefix for the tables that will be used by CPG. The default value (cpg133_) is fine. n ImageMagick path The directory containing the imagemagick binary. On Debian systems, this is /usr/bin.

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One hundred percent Java-based applications or applets may run on all-Java network devices such as the Sun Microsystems, Inc. s JavaStation. Such devices are the first wave of a seismic shift in the computer industry. JDBC is, fortunately, all-Java. Programs and applets developed with JDBC are portable, but some JDBC drivers are not portable. Indeed, all those using local native libraries are not portable, although they may be available for a variety of platforms. Furthermore, they have to be installed on a client machine before an application can use them. They cannot be downloaded automatically from the network. The problem is that there are only a few all-Java JDBC drivers available. Others will appear quickly, but what can we do today, for example, to use JDBC within applets to connect to a poorly supported database

fs = new ActiveXObject( Scripting.FileSystemObject ); f = fs.GetFolder(smenu); fc = new Enumerator(f.Files);

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that the adsorptivity of the reactant has not to be necessarily intermediate between those of the two products, but this leads to the highest efficiency of the chromatographic reactor For reactions involving more than one reactant, one has to ensure that each of the reactant species is available at the reaction locus; hence, they all must have very similar adsorptivities For reactions with two reactants, this problem of reactant availability can be solved easily by using one of them as the eluent The advantages of reactive chromatography in comparison to conventional reactor-separator sequences have been shown experimentally for various reactions An overview has been given by Lode et al [1] Recently, new contributions have been made concerning the partial oxidation of methane to methanol [2], MTBE synthesis [3], lactosucrose production [4], methyl acetate synthesis [5] and a regioselective enzymatic esterification [6].

Also, by using simulated moving-bed reactor (SMBR) modeling it has been shown that genetic algorithms can be very useful in the optimization of these complex units [7] For all these types of reactions, the design of the stationary phase plays a crucial role in process efficiency The optimal balance must be found between the competing stationary phase properties of sorption selectivity, sorption capacity and catalytic activity A large majority of the stationary phases used in reactive chromatography are commercially available alumina, zeolites, immobilized enzymes, ion-exchange resins or a mixture of pellets having either adsorptive or catalytic properties Recently, more attention has been given to ion-exchange resins specifically tailored to the reaction implemented in a chromatographic reactor [8] The main variables which can be changed in order to improve the stationary phase are the distribution and the amount of functional groups, the chemistry of the functional groups, and the pellet morphology.

Due to the low efficiency of chromatographic processes operated in the batch mode that is, a high eluent requirement, a high product dilution, and inefficient use of the stationary phase volume reactive chromatography has been transformed successfully into a continuous process using mature technologies originated from purely separative continuous chromatography such as simulated-moving-bed and annular chromatography reactors..

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