| Assessment Year | 1994 |
|---|---|
| Principal Product | Ashaplt |
| NAICS |
n/a
|
| SIC | 2911: Petroleum Refining |
| Sales Range | $50 M to 100M |
| # of Employees | 42 |
| Plant Area |
10,000
ft2
|
| Annual Production | 4,800,000
bbl
|
| Production Hrs. Annual | 7,224
hrs
|
| Location (State) | Georgia |
Facility Energy Cost and Usage
| Source | Yearly Cost | Usage | Unit Cost | |
|---|---|---|---|---|
| Electricity Usage | $302,920 | 5,939,918 |
kWh
|
$0.051 |
| Natural Gas | $1,807,067 | 614,501 |
MMBtu
|
$2.94 |
| LPG | $280,135 | 113,112 |
MMBtu
|
$2.48 |
| TOTAL YEARLY COSTS | - | |||
| RECOMMENDED SAVINGS* | $119,525 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
| IMPLEMENTED SAVINGS* | $28,220 | |||
Recommendations
| # | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Natural Gas Savings |
|---|---|---|---|---|---|---|
| 01 | 2.4133: Use most efficient type of electric motors | $4,820 | $20,170 |
$4,820
94,666
kWh
|
- | |
| 02 | 2.2135: Repair and eliminate steam leaks | $5,240 | $800 | - |
$5,240
-
MMBtu
|
|
| 03 | 2.2437: Recover waste heat from equipment | $77,700 | $212,000 | - |
$77,700
-
MMBtu
|
|
| 04 | 2.2121: Increase amount of condensate returned | $18,160 | $13,550 | - |
$18,160
-
MMBtu
|
|
| 05 | 2.2511: Insulate bare equipment | $3,090 | $2,665 | - |
$3,090
-
MMBtu
|
|
| 06 | 2.2124: Install de-aerator in place of condensate tank | $8,610 | $13,750 | - |
$8,610
-
MMBtu
|
|
| 07 | 2.1243: Use heat from boiler blowdown to preheat boiler feed water | $1,905 | $4,800 | - |
$1,905
-
MMBtu
|
|
| TOTAL RECOMMENDED | $119,525 | $267,735 |
$4,820
94,666
kWh
|
$114,705
-
MMBtu
|
||
| TOTAL IMPLEMENTED | $28,220 | $34,520 |
$4,820
94,666
kWh
|
$23,400
-
MMBtu
|
||
| Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Natural Gas Savings | |||
*Savings and costs are best estimates based on the center's site visit, associated engineering analysis, and typical capital and labor costs