Page 177 - Boiler plant and distribution system optimization manual
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162                                                 Boiler Plant and Distribution System Optimization Manual


                     All steam used by the system must pass         heating make up water to system operating tem-
                through steam traps, so the whole system is sub-    perature. One point often overlooked is that boil-
                ject to this loss if atmospheric vents are  used.   er inefficiencies are doubled in this case, because
                Closed pressurized condensate recovery systems      the steam in these leaks must be generated twice
                are  used  in  well-designed  plants  to  avoid  this   to use it once.
                problem. If the pure hot water is not brought back
                to the plant by the condensate recovery system,     Internal Steam Leaks
                then the expense of new water, its chemical treat-       Internal steam leaks are hard to detect, they
                ment and heating it back to operating tempera-      are inside the piping system, and common sense
                ture will just add to avoidable plant expenses.     indicates there are such leaks. Steam traps are in-
                                                                    stalled with bypass valves which are often opened
                Advantages/Disadvantages                            in the event there is a problem with the trap like
                     If you are not getting the condensate back     plugging. The bypass valves are often opened on
                from your steam system you are incurring about      start up or when water hammer becomes a prob-
                a 17% loss from that fact alone.                    lem in the system to drain water from the system.
                                                                    Steam driven equipment such as turbines and
                      ——————————————————
                                Rule of Thumb                       pumps have drains and  warmup  systems  and
                           Every 11 deg F [6 deg C] that            these can be left open too. The fact is steam can be
                             must be added to boiler                slipping  through  the  system  without  doing  any
                         feedwater costs 1% in efficiency.          work
                      ——————————————————


                                                                    8.   OPTIMIzE DEAEREATOR VENT RATE
                6.   REPAIR CONDENSATE RECEIVERS,                        (Figure 10.58)
                     PUMPS AND PIPING

                     Water seems to be such a common and cheap      9.   INSULATE THE FEEDWATER SYSTEM
                commodity and it is not assigned its real value to
                steam system management.                                 The water in the feedwater system is at the
                                                                    boiling point which could be 212F or higher de-
                     When conditions are not observable or
                                                                    pending on the pressure in the system. The deare-
                     known, the assumption is often made
                                                                    ator  and  reserve  feedwater  tank  are  typical  of
                     that they are negligible .
                                                                    such systems. The large surface represents a large
                                                                    loss of heat if not insulated. (Figure 10.59)
                     In steam systems, most of the losses are
                     not observable. Unfortunately they are
                     quite large and far from negligible .
                                                                    10.  USE HIGH-PRESSURE CONDENSATE TO
                                                                         MAKE LOW-PRESSURE STEAM
                7.   REPAIR STEAM LEAKS                                  The high pressure condensate recovery sys-
                                                                    tem can be a source for low pressure steam use in
                External Steam Leaks                                the plant or for other uses.
                     External steam leaks are usually visible and
                the length of the plume can be measured by eye.
                     For example, if there are 4 visible steam      11.  PRESSURE REDUCING VALVES
                leaks, two 6-foot plumes and two 8-foot plumes,
                this would work out to nearly $100,000 a year loss   Potential Savings
                plus the cost of water, chemicals and fuel wasted        Moderate
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