26
matching recommendations| ID | # | Year | Description | Yearly Savings |
Implementation
Imp Cost |
Status |
|---|---|---|---|---|---|---|
| OR0832 #04 Y:2026 | 04 | 2026 | Burn fossil fuel to produce steam to drive a steam turbine-generator and use steam exhaust for heat | $31,560 | $243,649 |
n/a
|
| OR0832 #03 Y:2026 | 03 | 2026 | Burn fossil fuel to produce steam to drive a steam turbine-generator and use steam exhaust for heat | $23,710 | $48,334 |
n/a
|
| OR0832 #02 Y:2026 | 02 | 2026 | Reduce the pressure of compressed air to the minimum required | $3,071 | $10,190 |
n/a
|
| OR0832 #01 Y:2026 | 01 | 2026 | Eliminate/reduce an operation | $32,217 | $26,036 |
n/a
|
| UF0549 #04 Y:2019 | 04 | 2019 | Develop standard procedures to improve internal yields | $492,292 | $1,875,550 | |
| UF0549 #03 Y:2019 | 03 | 2019 | Utilize higher efficiency lamps and/or ballasts | $6,001 | $2,904 | |
| UF0549 #02 Y:2019 | 02 | 2019 | Use most efficient type of electric motors | $73,018 | $68,138 | |
| UF0549 #01 Y:2019 | 01 | 2019 | Use a fossil fuel engine to cogenerate electricity or motive power; and utilize heat | $737,260 | $2,600,000 | |
| TT0211 #07 Y:2018 | 07 | 2018 | Use adjustable frequency drive or multiple speed motors on existing system | $13,109 | $3,750 | |
| TT0211 #06 Y:2018 | 06 | 2018 | Use most efficient equipment at it's maximum capacity and less efficient equipment only when necessary | $25,620 | $100 | |
| TT0211 #05 Y:2018 | 05 | 2018 | Use optimum temperature | $67,812 | $300,000 | |
| TT0211 #04 Y:2018 | 04 | 2018 | Replace existing chiller with high efficiency model | $73,737 | $75,000 | |
| TT0211 #03 Y:2018 | 03 | 2018 | Use adjustable frequency drive or multiple speed motors on existing system | $89,245 | $600,000 | |
| TT0211 #02 Y:2018 | 02 | 2018 | Use optimum size and capacity equipment | $96,921 | $15,000 | |
| TT0211 #01 Y:2018 | 01 | 2018 | Flash condensate to produce lower pressure steam | $115,103 | $150,000 | |
| OR0579 #07 Y:2012 | 07 | 2012 | Use photocell controls | $17,340 | $46,680 | |
| OR0579 #06 Y:2012 | 06 | 2012 | Recover heat from exhausted steam, hot air or hot water | $8,805 | $18,596 | |
| OR0579 #05 Y:2012 | 05 | 2012 | Replace electrically-operated equipment with fossil fuel equipment | $7,281 | $12,000 | |
| OR0579 #04 Y:2012 | 04 | 2012 | Use / purchase optimum sized compressor | $2,300 | $8,200 | |
| OR0579 #03 Y:2012 | 03 | 2012 | Substitute compressed air cooling with water or air cooling | $23,346 | $55,000 |