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2. While holding down the mouse button, move the cursor to the Pets table. Notice that Access displays a field-select icon (small rectangular box with lines inside of it) as you hold and drag the Customer Number field from the Customer table. 3. Drag-and-drop the field-select icon to the Customer Number field of the Pets table. Access displays the Edit Relationships dialog box as seen in Figure 6-6. 4. Click the Create button to create the relationship. Access closes the dialog box and places a join line between the Customer and Pets table.

After the execution of the preceding statements, the variable txt3 contains: What a very nice day

package com.wiley; import import import import import javax.servlet.http.HttpServletRequest; org.apache.struts.action.ActionForm; org.apache.struts.action.ActionMapping; org.apache.struts.action.ActionErrors; org.apache.struts.action.ActionError;

When you type the dot after Colors, IntelliSense can show you a list of all possible named colors that you can use.

**** IN WITNESS WHEREOF, each of Customer and Vendor has caused this Agreement to be signed and delivered by its duly authorized representative. [CUSTOMER] By: __________________________________ Name: Title:

As you would expect, user-centered development involves finding out a lot about the users and their tasks, and using this information to inform design. In 7 we introduced some data-gathering techniques which can be used to collect this information, including naturalistic observation. Studying people in their "natural" surroundings as they go about their work can provide insights that other data-gathering techniques cannot, and so interaction designers are keen to use this approach where appropriate. One particular method that has been used successfully for naturalistic observation in the social sciences is ethnography. It has also been used with some success in product development but there have been some difficulties knowing how to interpret and present the data gathered this way so that it can be translated into practical design. Another aspect of user-centered development is user involvement in the development process. There are different degrees of involvement, one of which is through evaluation studies, as discussed in s 10 through 14. Another is for users to contribute actively to the design itself-to become co-designers. As Gillian Crampton Smith said in the interview at the end of 6, users are not designers, but the payoffs for allowing users to contribute to the design themselves are quite high in terms of user acceptance of the product. So techniques have been developed that engage users actively and productively in design.

Taylor-flow or bubble train-flow regimes are characterized by gas bubbles, which are separated from the channel wall by a very thin liquid film, and from each other by a liquid slug At flow rates of industrial interest, this regime is achieved with typical organic fluids or water in monolith channels smaller than 2 mm Typical geometric surface areas are between 1200 and 4000 m2 m 3 Due to the thin liquid films between the bubbles and the wall on the one hand, and a strong internal recirculation of the liquid slug and exchange between the slugs and the films during the moving of the slugs and bubbles along the channel on the other hand, mass transfer in this regime is extraordinarily high and is accompanied with a low pressure drop.

Gas and liquid are fed co-currently into the reactor by a spray nozzle for the liquid and free gas suction, or together through a special set of static mixers to form a foamy layer on top of the monoliths The low pressure drop permits having, if necessary, a high recirculation rate of gas as well as liquid Figure 87 shows a set-up using monoliths in Taylor-flow regime where the heat of reaction is removed by an external heat exchanger Meanwhile, Akzo Nobel runs a commercial process applying the Taylor-flow regime, namely the hydrogenation of anthraquinone In monolithic catalyst carriers with wider channels, the liquid forms a film on the channel walls, whereas in the core of the channel a continuous gas phase exists As shown by Lebens [10], countercurrent gas liquid operation is now possible, and shows certain advantages over the countercurrent trickle bed operation.

Summary

1 2

Typical channel diameters are 3 5 mm, and the geometric surface areas are between 550 and 1000 m2 m 3 Below the flooding point, almost no hydrodynamic interaction between the gas and liquid can be observed; for example, the RTD is the same for both co-current and countercurrent operation Apart from some surface waves, the film flow is completely laminar..