Assessment Year | 1998 |
---|---|
Principal Product | Internal combustion engine bearings |
NAICS |
n/a
|
SIC | 3714: Motor Vehicle Parts and Accessories |
Sales Range | $50 M to 100M |
# of Employees | 615 |
Plant Area |
266,000
ft2
|
Annual Production | 100,000,000
pieces
|
Production Hrs. Annual | 8,400
hrs
|
Location (State) | Virginia |
Facility Energy Cost and Usage
Source | Yearly Cost | Usage | Unit Cost | |
---|---|---|---|---|
Electricity Usage | $588,250 | 28,555,100 |
kWh
|
$0.021 |
Electricity Demand | $519,065 | 37,296 |
kW-mo/yr
|
$13.92 |
Electricity Fees | $424,019 | - |
|
- |
Natural Gas | $323,547 | 61,916 |
MMBtu
|
$5.23 |
TOTAL YEARLY COSTS | - | |||
RECOMMENDED SAVINGS* | $1,513,070 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
IMPLEMENTED SAVINGS* | $424,900 |
Recommendations
# | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Water Disposal Savings | Solid Waste (non-haz) Savings | Personnel Changes Savings | Primary Raw Material Savings | Primary Product Savings | By-product Production Savings |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
01 | 3.1242: Allow drainage before withdrawing object | $408,630 | $24,685 | - | - | - |
$239,950
-
Tgal
|
$46,250
-
lb
|
- | $122,430 | - | - | |
02 | 3.4112: Recovery metals from rinse water(evap., ion exchange, ro, electrolysis, electrodialysis) and reuse rinse water | $277,345 | $644,800 | - | - | - |
$275,890
-
Tgal
|
$61,455
-
lb
|
$(-60,000.0) | - | - | - | |
03 | 3.1244: Reduce solution drag-out to prevent solution loss | $237,600 | $153,485 | - | - | - |
$119,975
-
Tgal
|
$23,125
-
lb
|
$(-28,000.0) | $122,500 | - | - | |
04 | 3.5248: Separate and recycle scrap metal to foundry or for sale | $221,455 | $70,000 | - | - |
$(-34,140.0)
-
MMBtu
|
- | - | $(-422,220.0) | - | - | $677,815 | |
05 | 4.721: Initiate a program to acquire iso certification | $198,225 | $250,000 | - | - | - | - | - | - | - | $198,225 | - | |
06 | 3.1175: Use a different or recycled raw material | $51,945 | $200,000 | - | - | - |
$101,945
-
Tgal
|
- | $(-50,000.0) | - | - | - | |
07 | 3.4132: Use deionized water in upstream rinse tanks | $48,650 | $120,000 | - | - | - | - |
$68,150
-
lb
|
$(-19,500.0) | - | - | - | |
08 | 3.4113: Treat and reuse rinse waters | $28,105 | $69,200 | - | - | - |
$28,105
-
Tgal
|
- | - | - | - | - | |
09 | 2.6232: Install set-back timers | $15,755 | $1,555 |
$15,755
395,662
kWh
|
- | - | - | - | - | - | - | - | |
10 | 3.4154: Eliminate leaks in water lines and valves | $9,390 | $8,000 | - | - | - |
$9,390
-
Tgal
|
- | - | - | - | - | |
11 | 2.4236: Eliminate leaks in inert gas and compressed air lines/ valves | $6,880 | $5,000 |
$6,680
317,995
kWh
|
$200
-
kW-mo/yr
|
- | - | - | - | - | - | - | |
12 | 2.4221: Install compressor air intakes in coolest locations | $6,310 | $1,120 |
$6,060
288,687
kWh
|
$250
-
kW-mo/yr
|
- | - | - | - | - | - | - | |
13 | 2.2441: Preheat boiler makeup water with waste process heat | $2,780 | $14,300 | - | - |
$2,780
-
MMBtu
|
- | - | - | - | - | - | |
TOTAL RECOMMENDED | $1,513,070 | $1,562,145 |
$28,495
1,002,344
kWh
|
$450
-
kW-mo/yr
|
$(-31,360.0)
-
MMBtu
|
$775,255
-
Tgal
|
$198,980
-
lb
|
$(-579,720.0) | $244,930 | $198,225 | $677,815 | ||
TOTAL IMPLEMENTED | $424,900 | $37,685 |
$6,680
317,995
kWh
|
$200
-
kW-mo/yr
|
- |
$249,340
-
Tgal
|
$46,250
-
lb
|
- | $122,430 | - | - | ||
Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Water Disposal Savings | Solid Waste (non-haz) Savings | Personnel Changes Savings | Primary Raw Material Savings | Primary Product Savings | By-product Production Savings |
*Savings and costs are best estimates based on the center's site visit, associated engineering analysis, and typical capital and labor costs