Synchronous and Sequential Strategies in the Process Design of Cascade Equipment
✍ Scribed by Prof. Ir. Dr. S. Jan Groot Wassink; Ir. Imre G. Rácz
- Publisher
- John Wiley and Sons
- Year
- 1976
- Tongue
- German
- Weight
- 379 KB
- Volume
- 48
- Category
- Article
- ISSN
- 0009-286X
No coin nor oath required. For personal study only.
✦ Synopsis
Abstract
Cascade or multistage equipment is characterized by the repetition of similar equipment elements in series. Process design, resulting into the main geometric and kinematic dimensions of the equipment, makes use of different strategies. These strategies, based on a process description, the (equality‐ and inequality) constraints and the number of degrees of freedom of the mathematical system, which describes the process, can be divided in synchronous‐ and sequential procedures. In a synchronous strategy no a priori requirements are made as to the distribution of a given process variable over the stages, so that the equipment dimensions are obtained simultaneously. In contrast to this a sequential strategy makes use of a priori statements resulting into stage‐to‐stage calculations and a decreasing number of degrees of freedom. The general theory presented with detailed information on process description, constraints and degrees of freedom, has been applied to the process design of a multi‐stage centrifugal compressor.
📜 SIMILAR VOLUMES
## Abstract ChemInform is a weekly Abstracting Service, delivering concise information at a glance that was extracted from about 200 leading journals. To access a ChemInform Abstract, please click on HTML or PDF.
This paper presents strategies for an automated control of distortion at the operational level of a production process chain, as well as first steps towards a combined implementation in heat-treatment processes. In order to minimise the loss of production due to quality defects, the first quality co
## Abstract In the SFB570, several sub‐processes of the standard process chain for manufacturing bearing rings have been modified in order to compensate distortion. This paper presents control strategies that enable a precise deployment of the compensation potential, on a local (sub‐process) level