Assessment Year | 1997 |
---|---|
Principal Product | Copper-Clad Laminates |
NAICS |
n/a
|
SIC | 3083: Laminated Plastics Plate, Sheet, and Profile Shapes |
Sales Range | $100 M to 500M |
# of Employees | 475 |
Plant Area |
243,000
ft2
|
Annual Production | 72,500
thousand feet
|
Production Hrs. Annual | 8,400
hrs
|
Location (State) | South Carolina |
Facility Energy Cost and Usage
Source | Yearly Cost | Usage | Unit Cost | |
---|---|---|---|---|
Electricity Usage | $594,010 | 25,830,598 |
kWh
|
$0.023 |
Electricity Demand | $367,000 | 40,330 |
kW-mo/yr
|
$9.10 |
Electricity Fees | $19,175 | - |
|
- |
Natural Gas | $1,616,015 | 468,867 |
MMBtu
|
$3.45 |
LPG | $48,660 | 6,808 |
MMBtu
|
$7.15 |
Fuel Oil #2 | $128,548 | 13,157 |
MMBtu
|
$9.77 |
TOTAL YEARLY COSTS | - | |||
RECOMMENDED SAVINGS* | $351,856 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
IMPLEMENTED SAVINGS* | - |
Recommendations
# | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Electricity Demand Savings | Electricity Fees Savings | Natural Gas Savings | Water Disposal Savings | Personnel Changes Savings | Ancillary Material Cost Savings | Water Consumption Savings |
---|---|---|---|---|---|---|---|---|---|---|---|---|
01 | 2.3112: Store heated/ cooled water for use during peak demand periods | $86,500 | $120,000 | n/a | - |
$51,200
-
kW-mo/yr
|
$35,300 | - | - | - | - | - |
02 | 2.3412: Use waste heat to produce steam to drive a steam turbine-generator | $186,200 | $245,000 | n/a |
$193,330
5,019,050
kWh
|
$35,670
-
kW-mo/yr
|
- |
$(-12,800.0)
-
MMBtu
|
- | $(-30,000.0) | - | - |
03 | 2.7142: Utilize higher efficiency lamps and/or ballasts | $11,903 | $37,960 | n/a |
$7,852
341,442
kWh
|
$4,051
-
kW-mo/yr
|
- | - | - | - | - | - |
04 | 2.2437: Recover waste heat from equipment | $4,263 | $5,550 | n/a |
$540
19,050
kWh
|
- | - |
$3,723
-
MMBtu
|
- | - | - | - |
05 | 3.4151: Minimize water usage | $2,924 | - | n/a | - | - | - |
$2,203
-
MMBtu
|
$452
-
Tgal
|
- | - |
$269
-
Tgal
|
06 | 3.4141: Replace the chlorination stage with an oxygen or ozone stage | $23,066 | $72,100 | n/a |
$6,609
133,060
kWh
|
- | - | - |
$4,592
-
Tgal
|
- | $9,130 |
$2,735
-
Tgal
|
07 | 4.652: Replace existing equipment with more suitable substitutes | $37,000 | - | n/a | - | - | - | - | - | - | $37,000 | - |
TOTAL RECOMMENDED | $351,856 | $480,610 |
$208,331
5,512,602
kWh
|
$90,921
-
kW-mo/yr
|
$35,300 |
$(-6,874.0)
-
MMBtu
|
$5,044
-
Tgal
|
$(-30,000.0) | $46,130 |
$3,004
-
Tgal
|
||
TOTAL IMPLEMENTED | - | - | - | - | - | - | - | - | - | - | ||
Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Electricity Fees Savings | Natural Gas Savings | Water Disposal Savings | Personnel Changes Savings | Ancillary Material Cost Savings | Water Consumption Savings |
*Savings and costs are best estimates based on the center's site visit, associated engineering analysis, and typical capital and labor costs