Page 326 - Improving Machinery Reliability
P. 326

Life Cycle Cost Studies   295

                                             Table 5-1 1
                    Non-annualized Acquisition and Sustaining Costs for Solo ANSI Pump

                       ANSI Pump:
                    CoslE,emenl   Year   Year   Year   Year   Year   Year   Year   Year   Year   Year   Year
                               0    1    2    3    4    5    6    7    8    8    10
                Aquisdion Cos&
                Picgram Managemenl   0
                Engineering Design   0
                Engineernng Data   0
                Spare pans B Lagisbu   0
                Faulilies 8 ConsVucLon   0
                lnieal Training   0
                Technical Data   0
                Capital Equlpmenl   0
                Suseining Costs
                DOwmenlaliOn Coas     0
                Disposal Costs                                                   3000
                          TOM    0    0    0    0    0    0    0    0    0    0   3000

                 Alternative #2: Add redundant ANSI pump. Use the following details from plant
                 experience.
                   This case results in pumps installed in parallel but operated as a standby redundant
                 system as the redundant components are not energized but are literally standing by
                 waiting to be used when failure of  the operating system is detected. Of course, the
                 detectiodswitching  device is very important for calculating overall system reliabili-
                 ty, and for this case the reliability is assumed to be  100%. Also for simplicity, the
                 reliability of the system is calculated as if the redundant pumps are operating in par-
                 allel. Furthermore, experience in most chemical plants and refineries shows impend-
                 ing failure is usually detected and redundant systems are usually started in a timely
                 manner to avoid lost production from the failing device; therefore, assume no loss of
                 production by use of redundant pumps.
                   Capital costs for the redundant ANSI pumps are $8,000 plus $3,000 for checkhso-
                 lation valves, plus $2,500 for construction and installation along with US$l,OOO for
                 program  management,  US$1,500 for engineering  design,  and US$l,OOO for docu-
                 mentation.  Likewise,  the plant  maintenance  organization  will  incur US$l,OOO for
                 engineering documentation costs to put the equipment into the paperwork system.
                   Lost gross margin occurs at US$4,000/hour when the process is down for repairs,
                   Annual power cost for running the pump is US$165/year per horsepower. Remem-
                 ber. either the old pump runs or the new pump (not both at the same time). The plant
                 incurs  1.6 power outages each year for an average downtime of  0.5 hours, and this
                 cost is charged into plant overhead rather than to individual pieces of equipment.


                   Annual power costs are (US$165/hp-year) * (100 hp) = US$16,500
                   Assume no lost production  time by  use of  the redundant pumps.  Keep all other
                 costs as described for the single ANSI pump and depreciate the assets over the ten
                 year project life.
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