| Assessment Year | 1998 |
|---|---|
| Principal Product | Ductile Iron Castings |
| NAICS |
n/a
|
| SIC | 3321: Gray and Ductile Iron Foundries |
| Sales Range | $50 M to 100M |
| # of Employees | 650 |
| Plant Area |
500,000
ft2
|
| Annual Production | 100,000
ton
|
| Production Hrs. Annual | 6,000
hrs
|
| Location (State) | Georgia |
Facility Energy Cost and Usage
| Source | Yearly Cost | Usage | Unit Cost | |
|---|---|---|---|---|
| Electricity Usage | $4,887,289 | 159,171,163 |
kWh
|
$0.031 |
| 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 YEARLY COSTS | - | |||
| RECOMMENDED SAVINGS* | $272,267 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
| IMPLEMENTED SAVINGS* | - | |||
Recommendations
| # | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Natural Gas Savings | LPG Savings | Water Disposal Savings | Administrative Changes Savings | Ancillary Material Cost Savings |
|---|---|---|---|---|---|---|---|---|---|---|
| 01 | 2.3415: Use a fossil fuel engine to cogenerate electricity or motive power; and utilize heat | $66,000 | $80,750 | - | - | - | - | $66,000 | - | |
| 02 | 2.4224: Upgrade controls on compressors | $44,660 | $40,000 |
$44,660
1,786,635
kWh
|
- | - | - | - | - | |
| 03 | 2.8113: Purchase gas directly from a contract gas supplier | $33,270 | - | - | - | - | - | $33,270 | - | |
| 04 | 2.2414: Use waste heat from hot flue gases to preheat | $13,572 | $12,000 |
$3,491
139,508
kWh
|
$10,081
-
MMBtu
|
- | - | - | - | |
| 05 | 2.2414: Use waste heat from hot flue gases to preheat | $37,500 | $28,000 | - |
$37,500
-
MMBtu
|
- | - | - | - | |
| 06 | 2.1332: Convert combustion equipment to burn natural gas | $36,165 | $36,600 | - |
$(-35,150.0)
-
MMBtu
|
$71,315
-
MMBtu
|
- | - | - | |
| 07 | 3.4155: Meter waste water | $32,250 | $7,000 | - | - | - | - | $32,250 | - | |
| 08 | 3.4141: Replace the chlorination stage with an oxygen or ozone stage | $8,850 | $36,000 | - | - | - |
$3,000
-
Tgal
|
- | $5,850 | |
| TOTAL RECOMMENDED | $272,267 | $240,350 |
$48,151
1,926,143
kWh
|
$12,431
-
MMBtu
|
$71,315
-
MMBtu
|
$3,000
-
Tgal
|
$131,520 | $5,850 | ||
| TOTAL IMPLEMENTED | - | - | - | - | - | - | - | - | ||
| Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Natural Gas Savings | LPG Savings | Water Disposal Savings | Administrative Changes Savings | Ancillary Material Cost Savings | |||
*Savings and costs are best estimates based on the center's site visit, associated engineering analysis, and typical capital and labor costs