Chemical Processing - April 2008 - (Page 31) >> Test rig Figure 2. High shear in-line test rig at Cranfield includes transducers for torque and differential pressure. Source: British Hydromechanics Research Group. attention to the subject — namely the University of Maryland, College Park, Md., with its High Shear Mixing Research Program, and the British Hydromechanics Research Group at Cranfield University, Cranfield, U.K. (Figure 2). Because this research has been carried out by consortia that includes equipment manufacturers, much of the data remain within their control. Again, results from these studies are being utilized to streamline development processes and as an aid to scale-up but little of the research has found its way into the public domain. To some extent this is understandable because the market for high shear mixing equipment is relatively small and highly competitive. The ability to accurately scale-up when specifying mixing equipment for a given application is one of the suppliers’ competitive advantages; the application of new techniques in combination with many years of research and development is a vital part of this advantage. Scale-up calculations Where scale-up is concerned, different manufacturers cite certain criteria as the basis for calculations but, as we’ve noted, the complexity of devices such as rotor/stator mixers makes it more realistic to combine a number of these factors. With the benefit of practical experience, the right combination can give an accurate scale-up recommendation. Traditionally geometric similarity and tank turnover/throughput formed the basis for many calculations. In light of recent research, additional parameters generally considered to provide reliable results include energy dissipation (that is, power per unit volume or power draw), rotor tip speed and shear frequency (residence time, also linked to open area or mixer geometry). Energy dissipation. In a situation where vessel and mixer geometry are similar across a range of sizes, energy dissipation is considered to be constant and, therefore, a useful tool in scale-up calculations. Power has to be monitored while mixing to determine the effects of the fluid’s physical properties on power draw. The most reliable way of doing this is to incorporate a torque transducer onto the mixer’s shaft to www.chemicalprocessing.com Readco Kurimoto and Melfi Technologies have combined to make processing a whole lot easier. With Readco’s continuous processing mixers and touch screen control produced by Melfi Technologies, life just became a lot less puzzling. Now you can process anything and change parameters with the touch of a button. This combined technology gives so many advantages over traditional batch mixing: • • • • • • • • • Reduced Cycle Time Combined Processes Reduced Clean-up and Waste Less Labor Batch to Batch Consistency Ease of use No Operator Error Reduced Costs Touch Screen Control Process anything with touch screen control. Actual Screen Shot Call us today to learn more. www.melfitechnologies.com 905-760-9080 800-395-4959 www.readco.com Visit Us at Booth #4405 at the PTXi Show and See A Live Demonstration! http://www.melfitechnologies.com http://www.readco.com http://www.chemicalprocessing.com
Table of Contents Feed for the Digital Edition of Chemical Processing - April 2008 Chemical Processing - April 2008 Contents From the Editor ChemicalProcessing.com Field Notes In Process Energy Saver Compliance Advisor Is It a Tragedy or Comedy for Engineers? Better Understanding Boosts Mixer Scale-up Don't Err With Air Compressors Control Performance Supervision Enhances Revamp Process Puzzler Plant InSites Equipment & Services Product Spotlight/Classifieds Ad Index End Point Chemical Processing - April 2008 Chemical Processing - April 2008 - Chemical Processing - April 2008 (Page Cover1) Chemical Processing - April 2008 - Chemical Processing - April 2008 (Page Cover2) Chemical Processing - April 2008 - Chemical Processing - April 2008 (Page 3) Chemical Processing - April 2008 - Chemical Processing - April 2008 (Page 4) Chemical Processing - April 2008 - Contents (Page 5) Chemical Processing - April 2008 - Contents (Page 6) Chemical Processing - April 2008 - From the Editor (Page 7) Chemical Processing - April 2008 - From the Editor (Page 8) Chemical Processing - April 2008 - ChemicalProcessing.com (Page 9) Chemical Processing - April 2008 - ChemicalProcessing.com (Page 10) Chemical Processing - April 2008 - Field Notes (Page 11) Chemical Processing - April 2008 - Field Notes (Page 12) Chemical Processing - April 2008 - In Process (Page 13) Chemical Processing - April 2008 - In Process (Page 14) Chemical Processing - April 2008 - In Process (Page 15) Chemical Processing - April 2008 - In Process (Page 16) Chemical Processing - April 2008 - Energy Saver (Page 17) Chemical Processing - April 2008 - Energy Saver (Page 18) Chemical Processing - April 2008 - Compliance Advisor (Page 19) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 20) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 21) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 22) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 23) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 24) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 25) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 26) Chemical Processing - April 2008 - Is It a Tragedy or Comedy for Engineers? (Page 27) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 28) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 29) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 30) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 31) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 32) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 33) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 34) Chemical Processing - April 2008 - Better Understanding Boosts Mixer Scale-up (Page 35) Chemical Processing - April 2008 - Don't Err With Air Compressors (Page 36) Chemical Processing - April 2008 - Don't Err With Air Compressors (Page 37) Chemical Processing - April 2008 - Don't Err With Air Compressors (Page 38) Chemical Processing - April 2008 - Don't Err With Air Compressors (Page 39) Chemical Processing - April 2008 - Don't Err With Air Compressors (Page 40) Chemical Processing - April 2008 - Control Performance Supervision Enhances Revamp (Page 41) Chemical Processing - April 2008 - Control Performance Supervision Enhances Revamp (Page 42) Chemical Processing - April 2008 - Control Performance Supervision Enhances Revamp (Page 43) Chemical Processing - April 2008 - Control Performance Supervision Enhances Revamp (Page 44) Chemical Processing - April 2008 - Process Puzzler (Page 45) Chemical Processing - April 2008 - Process Puzzler (Page 46) Chemical Processing - April 2008 - Process Puzzler (Page 47) Chemical Processing - April 2008 - Plant InSites (Page 48) Chemical Processing - April 2008 - Equipment & Services (Page 49) Chemical Processing - April 2008 - Equipment & Services (Page 50) Chemical Processing - April 2008 - Equipment & Services (Page 51) Chemical Processing - April 2008 - Product Spotlight/Classifieds (Page 52) Chemical Processing - April 2008 - Product Spotlight/Classifieds (Page 53) Chemical Processing - April 2008 - Product Spotlight/Classifieds (Page 54) Chemical Processing - April 2008 - Product Spotlight/Classifieds (Page 55) Chemical Processing - April 2008 - Product Spotlight/Classifieds (Page 56) Chemical Processing - April 2008 - Ad Index (Page 57) Chemical Processing - April 2008 - End Point (Page 58) Chemical Processing - April 2008 - End Point (Page Cover3) Chemical Processing - April 2008 - End Point (Page Cover4)
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