17
matching recommendations| ID | # | Year | Description | Yearly Savings |
Implementation
Imp Cost |
Status |
|---|---|---|---|---|---|---|
| MS0305 #03 Y:2006 | 03 | 2006 | Eliminate leaks in inert gas and compressed air lines/ valves | $1,851 | $244 | |
| MS0305 #02 Y:2006 | 02 | 2006 | Utilize higher efficiency lamps and/or ballasts | $3,385 | $16,886 | |
| MS0305 #01 Y:2006 | 01 | 2006 | Use waste heat to produce steam to drive a steam turbine-generator | $48,733 | $70,000 | |
| MS0183 #06 Y:2001 | 06 | 2001 | Eliminate leaks in water lines and valves | $1,296 | $50 | |
| MS0183 #05 Y:2001 | 05 | 2001 | Convert from batch operation to continuous processing | $1,957 | $432 | |
| MS0183 #04 Y:2001 | 04 | 2001 | Utilize higher efficiency lamps and/or ballasts | $711 | $2,074 | |
| MS0183 #03 Y:2001 | 03 | 2001 | Install occupancy sensors | $142 | $230 | |
| MS0183 #02 Y:2001 | 02 | 2001 | Eliminate leaks in inert gas and compressed air lines/ valves | $1,000 | $190 | |
| MS0183 #01 Y:2001 | 01 | 2001 | Optimize plant power factor | $7,236 | $8,235 | |
| MS0095 #08 Y:1997 | 08 | 1997 | Distill contaminated solvents for reuse | $142,935 | $162,000 | |
| MS0095 #07 Y:1997 | 07 | 1997 | Replace city water with recycled water via cooling tower | $45,259 | $8,955 | |
| MS0095 #06 Y:1997 | 06 | 1997 | Change procedures / equipment / operating conditions | $41,338 | $19,152 | |
| MS0095 #05 Y:1997 | 05 | 1997 | Insulate bare equipment | $2,730 | $6,255 | |
| MS0095 #04 Y:1997 | 04 | 1997 | Disconnect ballasts | $1,814 | $1,602 | |
| MS0095 #03 Y:1997 | 03 | 1997 | Utilize higher efficiency lamps and/or ballasts | $20,715 | $38,711 | |
| MS0095 #02 Y:1997 | 02 | 1997 | Recover waste heat from equipment | $8,674 | $14,571 | |
| MS0095 #01 Y:1997 | 01 | 1997 | Optimize plant power factor | $26,582 | $9,750 |