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CEP: Meeting Preview - AIChE 2007 Spring National Meeting Preliminary Program Book

Meeting Preview
March
2007
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Features

Scaling Fixed-Bed Catalyzed Processes

The new parameter introduced here will yield more meaningful results when a fixed-bed reactor is scaled up for process development or scaled down for plant support.

Modular Mini-Plants: A New Paradigm

Modular design principles are well known, but have found only niche applications in the Chemical industry. This article outlines an innovative methodology, whereby plant and process design may be conducted in parallel using components with pre-determined specifications and capacities, and...

Streamlining the Validation Process

Today, validation is no longer an afterthought for the design and construction of a new or renovated process or facility. It is, in fact, recognized as an integral part of the total project. Fully integrated services are now available to ensure a reduced validation cost and timely completion...

The G-Value for Agitator Design: Time to Retire It?

This commonly used number does not correctly address the influence of viscosity, and has no relationship to performance parameters such as fluid velocity and blend time. This article recommends actual measures of agitator performance that should be used instead.

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