Chemical Processing - March 2008 - (Page 22) >> High capacity tray Figure 1. Column internals that offer better performance such as this MD tray remain in high demand. Source: UOP. icalProcessing.com/articles/2007/177.html, www.Chemical Processing.com/industrynews/2008/002.html, and www. ChemicalProcessing.com/industrynews/2007/026.html.) Improvements in internals UOP is seeing continuing strong demand for its high performance distillation trays, notes Sturtevant, particularly for its high capacity MD ones (Figure 1). They typically are used for large liquid loads, especially when the volumetric ratio between vapor and liquid rates is low — common conditions in medium- to high-pressure services. Because MD trays can be used at close spacings, they can reduce both the height and diameter of a new column compared to one fitted with conventional multipass trays, says the company, thus significantly cutting vessel shell costs. The closer spacing means that retrofitted towers can contain far more trays, increasing product purity and recovery while reducing reflux ratio and therefore energy consumption. “The point here is that we are able to get more out of existing columns and make new columns smaller to achieve the same throughput,” Sturtevant says. It’s a similar story with Koch-Glitsch, Wichita, Kan., another major player in mass transfer. Like UOP, the company has a long tradition of manufacturing trays and in pioneering specialty high capacity designs. For instance, Superfrac trays, which are the culmination of 10 years of development work, are designed to produce the maximum capacity and maximum vapor/liquid contact efficiency achievable with crossflow distillation trays. They trays have provided the highest combined capacity and efficiency of any crossflow tray tested so far at Fractionation Research Inc. (FRI), Bartlesville, Okla., boasts Koch-Glitsch. (For insights from FRI about installing column internals, see www.Chemical Processing.com/articles/2007/030.html.) 22 • March 2008 When designing Superfrac trays, the company targeted three major areas to give them enhanced performance over conventional trays. First, a variety of valve styles and technologies are available to enhance the vapor/liquid contacting that takes place on a tray deck. Second, the downcomer is precisely sized and shaped to maximize the active area available for vapor/liquid contact. Finally, inlet area improvements provide more capacity and better froth initiation/bubbling activity on the tray — increasing vapor contact efficiency. Together, these enhancements eliminate the vapor and liquid maldistribution and stagnant zones that can occur on conventional trays, claims the company. They promote uniform flow distribution at the tray inlet and the perimeter areas, a great benefit to the tray’s hydraulic performance and contact efficiency. Sulzer Chemtech, Winterthur, Switzerland, another major player in the mass transfer field, offers a variety of trays, including high performance chordal downcomer, multi-downcomer and ultra-system-limit trays. In addition, it’s the authorized supplier of Shell’s high-end trays and other equipment. Many distillation columns rely on structured or random packings. And, here too, developments are pushing up performance. For instance, Koch-Glitsch has just introduced the Intalox Ultra random packings (Figure 2). These boast industry-leading strength-to-weight ratios, efficiencies and capacities, according to the company. This translates to reduced column diameter or height in new columns. On a revamp, the new packings offer a range of benefits, including more capacity at current purity, less energy consumption per unit of product, higher purity at current product rates, and lower pressure drop. In early February, Sulzer Chemtech signed an agreement with Kuehni, Allschwil, Switzerland, to work together on packed liquid/liquid extraction columns. Sulzer is providing the structured packing know-how and Kuehni the stirred exraction column knowledge so that customers can develop optimized designs for their extractors. Besides hardware, most major vendors of mass transfer hardware offer services to optimize the operation of columns; demand for such help is strong. Better and safer operation Optimizing distillation assets involves more than the mass transfer hardware. Enhanced column control can play an essential role. Major automation vendors such as Emerson, Yokogawa and Invensys are developing new technologies and alliances designed to improve distillation efficiency. For instance, in early January Emerson Process Management, Austin, Texas, announced the acquisition of The Automation Group (TAG), Houston. The deal will help Emerson expand its technical and management services for the design, engineering and implementation of automation systems, especially for distillation-based processes. Yokogawa, Tokyo, which will supply an integrated www.chemicalprocessing.com http://www.chemicalProcessing.com/articles/2007/177.html http://www.chemicalProcessing.com/industrynews/2008/002.html http://www.ChemicalProcessing.com/industrynews/2007/026.html http://www.chemicalProcessing.com/industrynews/2008/002.html http://www.ChemicalProcessing.com/industrynews/2007/026.html http://www.chemicalProcessing.com/articles/2007/030.html http://www.chemicalProcessing.com/articles/2007/030.html http://www.chemicalprocessing.com
Table of Contents Feed for the Digital Edition of Chemical Processing - March 2008 Chemical Processing - March 2008 Contents From the Editor ChemicalProcessing.com Field Notes In Process Energy Saver Compliance Advisor Distillation is Bubbling Feel Secure About Vulnerability Assessments The Door Opens For Membranes Achieve Effective Heat Exchanger Control Epoxy Maker Finds the Right Glue for Its Business Process Puzzler Plant InSites Equipment & Services Product Spotlight/Classifieds Ad Index End Point Chemical Processing - March 2008 Chemical Processing - March 2008 - Chemical Processing - March 2008 (Page Cover1) Chemical Processing - March 2008 - Chemical Processing - March 2008 (Page Cover2) Chemical Processing - March 2008 - Chemical Processing - March 2008 (Page 3) Chemical Processing - March 2008 - Chemical Processing - March 2008 (Page 4) Chemical Processing - March 2008 - Contents (Page 5) Chemical Processing - March 2008 - Contents (Page 6) Chemical Processing - March 2008 - From the Editor (Page 7) Chemical Processing - March 2008 - From the Editor (Page 8) Chemical Processing - March 2008 - ChemicalProcessing.com (Page 9) Chemical Processing - March 2008 - ChemicalProcessing.com (Page 10) Chemical Processing - March 2008 - Field Notes (Page 11) Chemical Processing - March 2008 - Field Notes (Page 12) Chemical Processing - March 2008 - In Process (Page 13) Chemical Processing - March 2008 - In Process (Page 14) Chemical Processing - March 2008 - In Process (Page 15) Chemical Processing - March 2008 - In Process (Page 16) Chemical Processing - March 2008 - Energy Saver (Page 17) Chemical Processing - March 2008 - Energy Saver (Page 18) Chemical Processing - March 2008 - Compliance Advisor (Page 19) Chemical Processing - March 2008 - Distillation is Bubbling (Page 20) Chemical Processing - March 2008 - Distillation is Bubbling (Page 21) Chemical Processing - March 2008 - Distillation is Bubbling (Page 22) Chemical Processing - March 2008 - Distillation is Bubbling (Page 23) Chemical Processing - March 2008 - Distillation is Bubbling (Page 24) Chemical Processing - March 2008 - Distillation is Bubbling (Page 25) Chemical Processing - March 2008 - Feel Secure About Vulnerability Assessments (Page 26) Chemical Processing - March 2008 - Feel Secure About Vulnerability Assessments (Page 27) Chemical Processing - March 2008 - Feel Secure About Vulnerability Assessments (Page 28) Chemical Processing - March 2008 - The Door Opens For Membranes (Page 29) Chemical Processing - March 2008 - The Door Opens For Membranes (Page 30) Chemical Processing - March 2008 - The Door Opens For Membranes (Page 31) Chemical Processing - March 2008 - The Door Opens For Membranes (Page 32) Chemical Processing - March 2008 - The Door Opens For Membranes (Page 33) Chemical Processing - March 2008 - Achieve Effective Heat Exchanger Control (Page 34) Chemical Processing - March 2008 - Achieve Effective Heat Exchanger Control (Page 35) Chemical Processing - March 2008 - Achieve Effective Heat Exchanger Control (Page 36) Chemical Processing - March 2008 - Achieve Effective Heat Exchanger Control (Page 37) Chemical Processing - March 2008 - Achieve Effective Heat Exchanger Control (Page 38) Chemical Processing - March 2008 - Epoxy Maker Finds the Right Glue for Its Business (Page 39) Chemical Processing - March 2008 - Epoxy Maker Finds the Right Glue for Its Business (Page 40) Chemical Processing - March 2008 - Process Puzzler (Page 41) Chemical Processing - March 2008 - Process Puzzler (Page 42) Chemical Processing - March 2008 - Plant InSites (Page 43) Chemical Processing - March 2008 - Equipment & Services (Page 44) Chemical Processing - March 2008 - Equipment & Services (Page 45) Chemical Processing - March 2008 - Product Spotlight/Classifieds (Page 46) Chemical Processing - March 2008 - Product Spotlight/Classifieds (Page 47) Chemical Processing - March 2008 - Product Spotlight/Classifieds (Page 48) Chemical Processing - March 2008 - Ad Index (Page 49) Chemical Processing - March 2008 - End Point (Page 50) Chemical Processing - March 2008 - End Point (Page Cover4) Chemical Processing - March 2008 - End Point (Page Cover4)
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