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, you are developing a product for a particular company, then it is easier to involve them If, however, you are developing a product for the open market, it is unlikely that you will be able to co-opt a user to your design team Box 91 explains how Microsoft involves users in its developments..

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frequency fc = c /2 , using a data rate Rb = 1/Tb and a chip rate Rc = 1/Tc . The kth user (k = 1, 2, . . . , Ku ) is assigned a unique code sequence {ak,j } of chip elements (+1, 1), so that its code waveform is given by

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This result is only due to the different degeneracies of the rotational levels for the two molecular models The simple rotational energy expression only applies to nondegenerate vibrational levels If the rigid rotor model for the degenerate states is relaxed, Coriolis interaction will give rotatiorid fine structure clusters caused by term splitting The CH4 spectrum, presented in Fig 43-1 1, may serve as an example A closer look at the PQR structure of the y fundamental at 3020 cm I reveals the line clusters Magnification of some of the P branch lines, such as P(7), discloses five components of similar intensity The primary splittings, as mentioned above, occur in the upper J'-levels, each of which contains J' - 1 components High resolution laser spectroscopy can even resolve 10 transitions, the additional of which arise from splittings in the ground state due to centrifugal effects.

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organics were sent back to the liquid vessel via an overflow During the experiments liquid samples were taken from the liquid inlet to the reactor and from the reactor outlet Samples were analyzed using gas chromatography (GC) and a Karl Fischer coulombmeter (KF) to determine concentrations and water contents Herein, the conversion measured at the reactor inlet for a certain time point is referred to as reactor inlet conversion The difference in conversion between the reactor inlet and outlet samples at the same time point will be called per (single) pass conversion For reactive stripping experiments, ca 13 L of liquid was used containing cumene as solvent, tetradecane as internal standard, and ca 12 mol% each of hexanoic acid and octanol-1 For the experiments with elevated acid concentrations, these values were 20 mol% and 11 mol%, respectively All experiments were carried out at 160 C and 5 bar absolute pressure.

The total BEA catalyst amount in the reactor ranged from 91 to 103 g for the different monolith sets The mass balances for the experiments were in the range of 99 % to 101 % The water balances for the reported experiments were in the range of 97 % to 101 %, thus giving sufficient confidence in the results of GC- and KF-analyses Flooding of the column was never observed For the experiments with increased water content or suppressed water removal, a 5 cm-long piece of coated monolith was mounted in a 500-mL autoclave All liquid concentrations, operation conditions and catalyst hold-up were the same as in the pilot-scale plant To maintain a gradient-less operation, a turbine-type stirrer recirculated the liquid very rapidly through the monolith channels During the experiments, liquid samples were taken from the reactor and analyzed as described above.

For the activity test, stirred glass flasks (50 mL) were run under atmospheric pressure and reflux conditions The solvent (cumene) boils at 160 C, and the vapor enters the cooler above the glass flask, from where the condensates flow back Treatment of the samples, all liquid concentrations and catalyst hold-up were similar to those in the pilot-scale plant and in the autoclave..

Internal and external integration 2001-2005

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