Chemical Processing - May 2008 - (Page 39) MAKING IT WORK << Hot cutover boosts control system migration Keeping critical unit running provides significant economic and implementation benefits By Eric Schnipke, Ineos Nitriles Component failures oCCuring in a 1980s–1990s-era distributed control system (DCS) at Ineos Nitriles’ Lima, Ohio, complex were jeopardizing production of acrylonitrile and its marketable acetonitrile and cyanide byproducts early in 2005. Shutdowns of the plant’s two continuous acrylonitrile reactors are intolerable. Production has been running at 98% reliability for several years; lost sales can’t be made up. Most hardware failures in the Bailey Network 90/Infi 90 DCS were in the DEC Alpha-based, OSI Conductor VMS consoles that had replaced original Bailey MCS consoles. DEC parts are out of production; used parts are difficult to locate. We also were seeing occasional failures in DCS controller input/output (I/O). In addition, an associated programmable logic controller (PLC) running the Lima site’s deep-well injection system was suffering spurious failures of unknown origin that tended to be in attention-getting critical logic and EPA-required recordkeeping. Opinion was divided on whether the failures were random or symptomatic of equipment age and possible failure acceleration. We initiated an analysis to find out but results were inconclusive. The next scheduled turnaround for the acrylonitrile unit isn’t until 2010, so management had to grapple with whether the plant could wait four years for an automation upgrade or replacement. The decision was that it couldn’t. Upgrade or replace? We evaluated three potential solutions: R 1. efurbish the VMS console computers, replace the lower CRT monitors with LCDs (the top CRTs already had been swapped out as a stopgap), and hope for the best from the controller hardware until 2010. This option posed two major downsides: the cost and questionable quality of refurbished computers to gain only a three-to-four-year reprieve; and, of course, potential controller and I/O unreliability. 2. eplace the old console computers with new HMI R hardware and software from the same company. The downsides: the difficulty in reconfiguring from Conductor VMS to Windows; time-consuming graphics conversion because no automated utilities were availwww.chemicalprocessing.com able; doubt about whether the consoles could be replaced without shutting down acrylonitrile production; and, again, questionable controller and I/O reliability. 3. nstall a new DCS, plus perhaps a new PLC, as soon I as possible, with cutover of the acrylonitrile operation accomplished hot. The major downside here was a possible cutover-induced process trip. None of these options involved changing field devices or altering control strategies. We found that the last alternative was the only practical choice. First, the cost of configuring and switching from existing consoles to new workstations was lower than that for retaining the old HMIs. The new DCS also offered the best avenue for hot cutover of both consoles and reactors — one reason is that it incorporates advanced digital automation, so we could avoid the need for add-on technology and the attendant chance of mistakes. Last, Ineos has had excellent experience with this automation equipment at other sites, including an adjacent catalysts plant. However, management was very concerned about a hot cutover; no one at Ineos to our knowledge had ever retrofitted controls for such a large and important process while it ran. Management also questioned whether enough real estate existed in electrical equipment rooms for both new and old control cabinets to run simultaneously and thereby allow a hot cutover. We won over management by developing a two-phase, six-month plan. This involved replacing the HMIs first, then the controllers, and finally the I/O. The plan The first phase employed Emerson’s DeltaV Connect Solution for Bailey Systems, a transition package that replaces the existing HMIs and provides modern functions, while retaining the original system’s controllers, I/O and field May 2008 • 39 http://www.chemicalprocessing.com
Table of Contents Feed for the Digital Edition of Chemical Processing - May 2008 From the Editor ChemicalProcessing.com Field Notes In Process Energy Saver Compliance Advisor WirelessHART signals a change at plants Avoid costly fabrication mistakes Watch out with variable speed pumping Hot cutover boosts control system migration Plant InSites Process Puzzler Equipment & Services Product Spotlight/Classifieds Ad Index End Point Chemical Processing - May 2008 Chemical Processing - May 2008 - (Page Cover1) Chemical Processing - May 2008 - (Page Cover2) Chemical Processing - May 2008 - (Page 3) Chemical Processing - May 2008 - (Page 4) Chemical Processing - May 2008 - (Page 5) Chemical Processing - May 2008 - (Page 6) Chemical Processing - May 2008 - (Page 7) Chemical Processing - May 2008 - (Page 8) Chemical Processing - May 2008 - From the Editor (Page 9) Chemical Processing - May 2008 - From the Editor (Page 10) Chemical Processing - May 2008 - ChemicalProcessing.com (Page 11) Chemical Processing - May 2008 - ChemicalProcessing.com (Page 12) Chemical Processing - May 2008 - Field Notes (Page 13) Chemical Processing - May 2008 - In Process (Page 14) Chemical Processing - May 2008 - In Process (Page 15) Chemical Processing - May 2008 - Energy Saver (Page 16) Chemical Processing - May 2008 - Compliance Advisor (Page 17) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 18) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 19) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 20) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 21) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 22) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 23) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 24) Chemical Processing - May 2008 - WirelessHART signals a change at plants (Page 25) Chemical Processing - May 2008 - Avoid costly fabrication mistakes (Page 26) Chemical Processing - May 2008 - Avoid costly fabrication mistakes (Page 27) Chemical Processing - May 2008 - Avoid costly fabrication mistakes (Page 28) Chemical Processing - May 2008 - Avoid costly fabrication mistakes (Page 29) Chemical Processing - May 2008 - Avoid costly fabrication mistakes (Page 30) Chemical Processing - May 2008 - Avoid costly fabrication mistakes (Page 31) Chemical Processing - May 2008 - Avoid costly fabrication mistakes (Page 32) Chemical Processing - May 2008 - Watch out with variable speed pumping (Page 33) Chemical Processing - May 2008 - Watch out with variable speed pumping (Page 34) Chemical Processing - May 2008 - Watch out with variable speed pumping (Page 35) Chemical Processing - May 2008 - Watch out with variable speed pumping (Page 36) Chemical Processing - May 2008 - Watch out with variable speed pumping (Page 37) Chemical Processing - May 2008 - Watch out with variable speed pumping (Page 38) Chemical Processing - May 2008 - Hot cutover boosts control system migration (Page 39) Chemical Processing - May 2008 - Hot cutover boosts control system migration (Page 40) Chemical Processing - May 2008 - Hot cutover boosts control system migration (Page 41) Chemical Processing - May 2008 - Hot cutover boosts control system migration (Page 42) Chemical Processing - May 2008 - Process Puzzler (Page 43) Chemical Processing - May 2008 - Plant InSites (Page 44) Chemical Processing - May 2008 - Equipment & Services (Page 45) Chemical Processing - May 2008 - Product Spotlight/Classifieds (Page 46) Chemical Processing - May 2008 - Product Spotlight/Classifieds (Page 47) Chemical Processing - May 2008 - Product Spotlight/Classifieds (Page 48) Chemical Processing - May 2008 - Ad Index (Page 49) Chemical Processing - May 2008 - End Point (Page 50) Chemical Processing - May 2008 - End Point (Page Cover3) Chemical Processing - May 2008 - End Point (Page Cover4)
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