Implementation Grant Funding Opportunity Open
IMPORTANT: The grant program operates on a rolling basis and applications may be submitted at any time, with quarterly reviews.
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Implementation Grant Funding Opportunity Open
Qualifying* small and medium-sized US manufacturers, that received IAC or Combined Heat and Power Technical Assistance Partnership assessments between 2018 and 2024, can now apply for grants for implementation of assessment recommendations up 50% of qualifying* project costs with a maximum of $300,000 per manufacturer.
IMPORTANT: The grant program now operates on a rolling basis and applications may be submitted at any time through the year, with quarterly reviews.
*See Full Grant Solicitation for full qualification and selection details.
20,022
matching recommendations| ARC | 2.2 | Thermal Systems |
|---|
| Row Colors Legend |
|---|
| no implementation information |
| Implemented |
| NOT Implemented |
| ID | # | Year | Products | Savings | Cost | Status |
|---|---|---|---|---|---|---|
| UD0851 # 12 Y:2012 | 12 | 2012 | USE WASTE HEAT FROM HOT FLUE GASES TO PREHEAT | $27,723 | $31,000 | Not Implemented |
| LE0334 # 03 Y:2012 | 03 | 2012 | RECOVER WASTE HEAT FROM EQUIPMENT | $44,014 | $12,000 | Not Implemented |
| OR0579 # 06 Y:2012 | 06 | 2012 | RECOVER HEAT FROM EXHAUSTED STEAM, HOT AIR OR HOT WATER | $8,805 | $18,596 | Not Implemented |
| DL0082 # 02 Y:2012 | 02 | 2012 | USE "HEAT WHEEL" OR OTHER HEAT EXCHANGER TO CROSS-EXCHANGE BUILDING EXHAUST AIR WITH MAKE-UP AIR | $18,536 | $46,000 | Not Implemented |
| IA0476 # 05 Y:2012 | 05 | 2012 | RE-USE OR RECYCLE HOT OR COLD PROCESS EXHAUST AIR | $1,225 | $979 | Not Implemented |
| MA0689 # 04 Y:2012 | 04 | 2012 | USE OPTIMUM TEMPERATURE | $13,757 | $8,000 | Implemented |
| MA0689 # 06 Y:2012 | 06 | 2012 | RECOVER WASTE HEAT FROM EQUIPMENT | $7,905 | $12,000 | Not Implemented |
| MA0689 # 09 Y:2012 | 09 | 2012 | USE OPTIMUM TEMPERATURE | $5,818 | $900 | Implemented |
| MA0689 # 15 Y:2012 | 15 | 2012 | INSULATE BARE EQUIPMENT | $1,579 | $2,300 | Implemented |
| TT0090 # 01 Y:2012 | 01 | 2012 | RECOVER WASTE HEAT FROM EQUIPMENT | $4,085 | $0 | Not Implemented |
| TT0090 # 04 Y:2012 | 04 | 2012 | USE COOLING TOWER OR ECONOMIZER TO REPLACE CHILLER COOLING | $2,764 | $2,000 | Implemented |
| TT0090 # 06 Y:2012 | 06 | 2012 | USE WASTE HEAT FROM HOT FLUE GASES TO PREHEAT | $29,200 | $35,000 | Not Implemented |
| SF0411 # 07 Y:2012 | 07 | 2012 | USE MULTIPLE-EFFECT EVAPORATORS | $14,245 | $17,433 | Not Implemented |
| SF0411 # 08 Y:2012 | 08 | 2012 | RECOVER WASTE HEAT FROM EQUIPMENT | $2,723 | $3,965 | Not Implemented |
| SF0411 # 09 Y:2012 | 09 | 2012 | USE WASTE HEAT FROM HOT FLUE GASES TO PREHEAT | $4,671 | $11,216 | Not Implemented |
| SF0411 # 11 Y:2012 | 11 | 2012 | REPLACE EXISTING CHILLER WITH HIGH EFFICIENCY MODEL | $1,227 | $3,774 | Not Implemented |
| TT0086 # 01 Y:2012 | 01 | 2012 | USE OPTIMUM THICKNESS INSULATION | $920 | $950 | Implemented |
| TT0086 # 02 Y:2012 | 02 | 2012 | CHILL WATER TO THE HIGHEST TEMPERATURE POSSIBLE | $1,061 | $0 | Implemented |
| NC0442 # 02 Y:2012 | 02 | 2012 | USE WASTE HEAT FROM HOT FLUE GASES TO PREHEAT | $44,787 | $200,000 | Not Implemented |
| NC0442 # 03 Y:2012 | 03 | 2012 | FLASH CONDENSATE TO PRODUCE LOWER PRESSURE STEAM | $4,788 | $20,000 | Not Implemented |
| OK0822 # 08 Y:2012 | 08 | 2012 | SHUT OFF COOLING IF COLD OUTSIDE AIR WILL COOL PROCESS | $16,463 | $26,358 | Implemented |
| LE0333 # 05 Y:2012 | 05 | 2012 | RECOVER WASTE HEAT FROM EQUIPMENT | $1,865 | $1,000 | Not Implemented |
| MA0690 # 01 Y:2012 | 01 | 2012 | INSULATE BARE EQUIPMENT | $3,246 | $1,750 | Implemented |
| MA0690 # 02 Y:2012 | 02 | 2012 | USE COOLING TOWER OR ECONOMIZER TO REPLACE CHILLER COOLING | $1,986 | $7,500 | Not Implemented |
| MA0690 # 04 Y:2012 | 04 | 2012 | MODERATE COOLING TOWER OUTLET TEMPERATURE | $1,582 | $4,075 | Not Implemented |