| Assessment Year | 2003 |
|---|---|
| Principal Product | Distilled water and medical supplies |
| NAICS | 325412: Pharmaceutical Preparation Manufacturing |
| SIC | 2834: Pharmaceutical Preparations |
| Sales Range | greater than $500 M |
| # of Employees | 1,000 |
| Plant Area |
800,000
ft2
|
| Annual Production | 38,000,000
pieces
|
| Production Hrs. Annual | 8,760
hrs
|
| Location (State) | Mississippi |
Facility Energy Cost and Usage
| Source | Yearly Cost | Usage | Unit Cost | |
|---|---|---|---|---|
| Electricity Usage | $1,812,720 | 52,756,704 |
kWh
|
$0.034 |
| Electricity Demand | $547,171 | 93,793 |
kW-mo/yr
|
$5.83 |
| Electricity Fees | $224,168 | - |
|
- |
| Natural Gas | $1,088,181 | 261,556 |
MMBtu
|
$4.16 |
| TOTAL YEARLY COSTS | - | |||
| RECOMMENDED SAVINGS* | $1,564,891 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
| IMPLEMENTED SAVINGS* | $43,745 | |||
Recommendations
| # | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Electricity Demand Savings | Electricity Fees Savings | Natural Gas Savings |
|---|---|---|---|---|---|---|---|---|
| 01 | 2.3416: Use combined cycle gas turbine generator sets with waste heat boilers connected to turbine exhaust | $936,645 | $8,400,000 | n/a |
$1,812,720
52,756,704
kWh
|
$547,171
-
kW-mo/yr
|
$224,168 |
$(-1,647,414.0)
-
MMBtu
|
| 02 | 2.2414: Use waste heat from hot flue gases to preheat | $351,990 | $119,086 | n/a | - | - | - |
$351,990
-
MMBtu
|
| 03 | 2.2111: Install steam trap | $76,374 | $12,262 | - | - | - |
$76,374
-
MMBtu
|
|
| 04 | 2.4146: Use adjustable frequency drive or multiple speed motors on existing system | $68,515 | $153,750 |
$52,908
1,539,800
kWh
|
$5,397
-
kW-mo/yr
|
$10,210 | - | |
| 05 | 2.2152: Maintain steam jets used for vacuum system | $37,053 | $70,000 | n/a | - | - | - |
$37,053
-
MMBtu
|
| 06 | 2.4146: Use adjustable frequency drive or multiple speed motors on existing system | $31,243 | $26,302 |
$26,407
768,537
kWh
|
- | $4,836 | - | |
| 07 | 2.2614: Use cooling tower or economizer to replace chiller cooling | $26,018 | $50,000 | n/a |
$21,990
640,000
kWh
|
- | $4,028 | - |
| 08 | 2.3132: Recharge batteries on during off-peak demand periods | $12,652 | - | - |
$11,539
-
kW-mo/yr
|
$1,113 | - | |
| 09 | 2.1311: Replace electrically-operated equipment with fossil fuel equipment | $8,477 | $1,560 |
$3,955
115,096
kWh
|
$3,464
-
kW-mo/yr
|
$1,058 | - | |
| 10 | 2.4236: Eliminate leaks in inert gas and compressed air lines/ valves | $7,641 | $181 |
$6,457
187,929
kWh
|
- | $1,184 | - | |
| 11 | 2.4239: Eliminate or reduce compressed air usage | $4,861 | $7,596 |
$4,109
119,573
kWh
|
- | $752 | - | |
| 12 | 2.2511: Insulate bare equipment | $3,422 | $301 |
$2,893
84,185
kWh
|
- | $529 | - | |
| TOTAL RECOMMENDED | $1,564,891 | $8,841,038 |
$1,931,439
56,211,824
kWh
|
$567,571
-
kW-mo/yr
|
$247,878 |
$(-1,181,997.0)
-
MMBtu
|
||
| TOTAL IMPLEMENTED | $43,745 | $34,079 |
$36,973
1,076,039
kWh
|
- | $6,772 | - | ||
| Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Electricity Fees 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