| Assessment Year | 2008 |
|---|---|
| Principal Product | Brake Components |
| NAICS | 327910: Abrasive Product Manufacturing |
| SIC | 3291: Abrasive Products |
| Sales Range | $10 M to 50M |
| # of Employees | 130 |
| Plant Area |
100,000
ft2
|
| Annual Production | 100,000,000
pieces
|
| Production Hrs. Annual | 6,600
hrs
|
| Location (State) | Indiana |
Facility Energy Cost and Usage
| Source | Yearly Cost | Usage | Unit Cost | |
|---|---|---|---|---|
| Electricity Usage | $538,702 | 7,475,900 |
kWh
|
$0.072 |
| Natural Gas | $549,243 | 68,813 |
MMBtu
|
$7.98 |
| TOTAL YEARLY COSTS | - | |||
| RECOMMENDED SAVINGS* | $1,454,462 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
| IMPLEMENTED SAVINGS* | $189,799 | |||
Recommendations
| # | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Solid Waste (non-haz) Savings | Administrative Changes Savings | Primary Raw Material Savings | Ancillary Material Cost Savings | Water Consumption Savings |
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 01 | 4.131: Modify process to reduce material use/cost | $621,360 | $28,800 | - | - | - |
$3,600
-
lb
|
$380,160 | $237,600 | - | - | |
| 02 | 2.2191: Substitute hot process fluids for steam | $468,137 | $140,000 | - | - |
$468,137
-
MMBtu
|
- | - | - | - | - | |
| 03 | 3.8132: Use less toxic and volatile solvent substitutes | $86,400 | $85,000 | - | - | - | - | $86,400 | - | - | - | |
| 04 | 2.2223: Enhance sensitivity of temperature control and cutoff | $70,469 | $40,000 | - | - |
$70,469
-
MMBtu
|
- | - | - | - | - | |
| 05 | 3.4114: Replace city water with recycled water via cooling tower | $45,421 | $74,873 | - | - | - | - | - | - | - |
$45,421
-
Tgal
|
|
| 06 | 2.2124: Install de-aerator in place of condensate tank | $35,664 | $50,000 | - | - |
$28,568
-
MMBtu
|
- | - | - | $6,000 |
$1,096
-
Tgal
|
|
| 07 | 2.4131: Size electric motors for peak operating efficiency | $35,347 | $15,000 |
$29,733
561,000
kWh
|
$5,614
-
kW-mo/yr
|
- | - | - | - | - | - | |
| 08 | 2.4236: Eliminate leaks in inert gas and compressed air lines/ valves | $33,252 | $1,000 |
$26,585
501,600
kWh
|
$6,667
-
kW-mo/yr
|
- | - | - | - | - | - | |
| 09 | 2.2136: Install / repair insulation on steam lines | $18,821 | $1,900 | - | - |
$18,821
-
MMBtu
|
- | - | - | - | - | |
| 10 | 2.7142: Utilize higher efficiency lamps and/or ballasts | $15,188 | $28,755 |
$11,799
222,631
kWh
|
$2,959
-
kW-mo/yr
|
- | - | $430 | - | - | - | |
| 11 | 2.2163: Use minimum steam operating pressure | $7,900 | - | - | - |
$7,900
-
MMBtu
|
- | - | - | - | - | |
| 12 | 2.4234: Cool compressor air intake with heat exchanger | $8,318 | $19,000 | - | - | - | - | - | - | - |
$8,318
-
Tgal
|
|
| 13 | 2.6221: Use most efficient equipment at it's maximum capacity and less efficient equipment only when necessary | $4,240 | - |
$4,240
80,000
kWh
|
- | - | - | - | - | - | - | |
| 14 | 2.7142: Utilize higher efficiency lamps and/or ballasts | $2,509 | $3,815 |
$2,144
40,445
kWh
|
$365
-
kW-mo/yr
|
- | - | - | - | - | - | |
| 15 | 4.131: Modify process to reduce material use/cost | $1,436 | - | - | - |
$1,436
-
MMBtu
|
- | - | - | - | - | |
| TOTAL RECOMMENDED | $1,454,462 | $488,143 |
$74,501
1,405,676
kWh
|
$15,605
-
kW-mo/yr
|
$595,331
-
MMBtu
|
$3,600
-
lb
|
$466,990 | $237,600 | $6,000 |
$54,835
-
Tgal
|
||
| TOTAL IMPLEMENTED | $189,799 | $128,815 |
$62,702
1,183,045
kWh
|
$12,646
-
kW-mo/yr
|
$99,037
-
MMBtu
|
- | - | - | $6,000 |
$9,414
-
Tgal
|
||
| Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Solid Waste (non-haz) Savings | Administrative Changes Savings | Primary Raw Material 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