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.
Learn More
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.
| IAC Center | Georgia Institute of Technology |
|---|---|
| Assessment Year | 1998 |
| Principal Product | Ductile Iron Castings |
| NAICS | n/a |
| SIC | 3321 - Gray And Ductile Iron Foundries |
| Sales | $50,000,000-$100,000,000 |
| # of Employees | 650 |
| Plant Area (Sq.Ft.) | 500,000 |
| Annual Production | 100,000 Tons |
| Production Hrs. Annual | 6,000 |
| Location (State) | GA |
| Source | Yearly Cost | Usage | Unit | Unit Cost |
|---|---|---|---|---|
| Electricity Usage | $4,887,289 | 159,171,163 | kWh | $0.03 |
| Natural Gas | $469,886 | 127,418 | MMBtu | $3.69 |
| LPG | $123,971 | 18,566 | MMBtu | $6.68 |
| Fuel Oil #2 | $20,342 | 3,752 | MMBtu | $5.42 |
| TOTAL ENERGY COSTS | $5,555,340 | |||
| RECOMMENDED SAVINGS* | $272,267 | *Non-energy impacts included in savings. See recommendations below |
||
| IMPLEMENTED SAVINGS* | - | |||
| #|Description |
Savings Cost |
Status | Electricity Usage | Natural Gas | LPG | Water Disposal | Administrative Changes | Ancillary Material Cost | Electricity Usage | Natural Gas | LPG | Water Disposal | Administrative Changes | Ancillary Material Cost | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| $ | kWh | $ | MMBtu | $ | MMBtu | $ | Tgal | $ | $ | $ | $ | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 01: 2.3415 USE A FOSSIL FUEL ENGINE TO COGENERATE ELECTRICITY OR MOTIVE POWER; AND UTILIZE HEAT |
Savings: $66,000 Cost: $80,750 |
- | - | - | - | - | - | - | - | $66,000 | - | - | - |
- - kWh |
- - MMBtu |
- - MMBtu |
- - Tgal |
$66,000 - $ |
- - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 02: 2.4224 UPGRADE CONTROLS ON COMPRESSORS |
Savings: $44,660 Cost: $40,000 |
$44,660 | 1,786,635 | - | - | - | - | - | - | - | - | - | - |
$44,660 1,786,635 kWh |
- - MMBtu |
- - MMBtu |
- - Tgal |
- - $ |
- - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 03: 2.8113 PURCHASE GAS DIRECTLY FROM A CONTRACT GAS SUPPLIER |
Savings: $33,270 Cost: - |
- | - | - | - | - | - | - | - | $33,270 | - | - | - |
- - kWh |
- - MMBtu |
- - MMBtu |
- - Tgal |
$33,270 - $ |
- - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 04: 2.2414 USE WASTE HEAT FROM HOT FLUE GASES TO PREHEAT |
Savings: $13,572 Cost: $12,000 |
$3,491 | 139,508 | $10,081 | 2,808 | - | - | - | - | - | - | - | - |
$3,491 139,508 kWh |
$10,081 2,808 MMBtu |
- - MMBtu |
- - Tgal |
- - $ |
- - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 05: 2.2414 USE WASTE HEAT FROM HOT FLUE GASES TO PREHEAT |
Savings: $37,500 Cost: $28,000 |
- | - | $37,500 | 10,460 | - | - | - | - | - | - | - | - |
- - kWh |
$37,500 10,460 MMBtu |
- - MMBtu |
- - Tgal |
- - $ |
- - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 06: 2.1332 CONVERT COMBUSTION EQUIPMENT TO BURN NATURAL GAS |
Savings: $36,165 Cost: $36,600 |
- | - | $(-35,150) | (-9,792) | $71,315 | 9,792 | - | - | - | - | - | - |
- - kWh |
$(-35,150) (-9,792) MMBtu |
$71,315 9,792 MMBtu |
- - Tgal |
- - $ |
- - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 07: 3.4155 METER WASTE WATER |
Savings: $32,250 Cost: $7,000 |
- | - | - | - | - | - | - | - | $32,250 | - | - | - |
- - kWh |
- - MMBtu |
- - MMBtu |
- - Tgal |
$32,250 - $ |
- - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| 08: 3.4141 REPLACE THE CHLORINATION STAGE WITH AN OXYGEN OR OZONE STAGE |
Savings: $8,850 Cost: $36,000 |
- | - | - | - | - | - | $3,000 | 3,132,000 | - | - | $5,850 | - |
- - kWh |
- - MMBtu |
- - MMBtu |
$3,000 3,132,000 Tgal |
- - $ |
$5,850 - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| TOTAL RECOMMENDED |
Savings: $272,267 Cost: $240,350 |
$48,151 | 1,926,143 | $12,431 | 3,476 | $71,315 | 9,792 | $3,000 | 3,132,000 | $131,520 | - | $5,850 | - | $48,151 1,926,143 kWh |
$12,431 3,476 MMBtu |
$71,315 9,792 MMBtu |
$3,000 3,132,000 Tgal |
$131,520 - $ |
$5,850 - $ |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| TOTAL IMPLEMENTED |
Savings: - Cost: - |
- | - | - | - | - | - | - | - | - | - | - | - | - - kWh |
- - MMBtu |
- - MMBtu |
- - Tgal |
- - $ |
- - $ |
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|
Savings Cost |
$ | kWh | $ | MMBtu | $ | MMBtu | $ | Tgal | $ | $ | $ | $ | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| Electricity Usage | Natural Gas | LPG | Water Disposal | Administrative Changes | Ancillary Material Cost | Electricity Usage | Natural Gas | LPG | Water Disposal | Administrative Changes | Ancillary Material Cost | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||