| Assessment Year | 2020 |
|---|---|
| Principal Product | Whiskey |
| NAICS | 312140: Distilleries |
| SIC | 2085: Distilled and Blended Liquors |
| Sales Range | $50 M to 100M |
| # of Employees | 65 |
| Plant Area |
40,000
ft2
|
| Annual Production | 24,000
Tgal
|
| Production Hrs. Annual | 8,400
hrs
|
| Location (State) | Kentucky |
Facility Energy Cost and Usage
| Source | Yearly Cost | Usage | Unit Cost | ||
|---|---|---|---|---|---|
| Electricity Usage | $314,884 | 10,347,600 |
kWh
|
$0.030 | |
| Electricity Demand | $563,834 | 26,560 |
kW-mo/yr
|
$21.23 | |
| Electricity Fees | $2,650 | - |
|
- | |
| Natural Gas | $1,703,176 | 553,353 |
MMBtu
|
$3.08 | |
| Waste Disposal Costs | |||||
| Water Usage | $648,128 | 217,612 |
Tgal
|
$2.98 | |
| Water Disposal | $4,305,000 | 956,667 |
Tgal
|
$4.50 | |
| TOTAL YEARLY COSTS | $7,537,672 | ||||
| RECOMMENDED SAVINGS* | $939,576 |
See individual recommendations below
*Non-energy impacts included in savings.
|
|||
| IMPLEMENTED SAVINGS* | $645,962 | ||||
Recommendations
| # | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Electricity Demand Savings | Electricity Fees Savings | Natural Gas Savings | Water Usage Savings | Water Disposal Savings |
|---|---|---|---|---|---|---|---|---|---|---|
| 01 | 2.4222: Install adequate dryers on air lines to eliminate blowdown | $6,031 | $21,360 |
$2,974
99,120
kWh
|
$3,057
-
kW-mo/yr
|
- | - | - | - | |
| 02 | 2.4231: Reduce the pressure of compressed air to the minimum required | $9,779 | - |
$4,854
161,805
kWh
|
$4,925
-
kW-mo/yr
|
- | - | - | - | |
| 03 | 2.4236: Eliminate leaks in inert gas and compressed air lines/ valves | $3,067 | $2,630 |
$3,067
102,228
kWh
|
- | - | - | - | - | |
| 04 | 2.2121: Increase amount of condensate returned | $360,000 | $250,000 | - | - | - | - |
$144,000
-
Tgal
|
$216,000
-
Tgal
|
|
| 05 | 2.2511: Insulate bare equipment | $52,668 | $24,890 | - | - | - |
$52,668
-
MMBtu
|
- | - | |
| 06 | 2.2442: Preheat combustion air with waste heat | $71,487 | $150,900 | - | - | - |
$71,487
-
MMBtu
|
- | - | |
| 07 | 2.1233: Analyze flue gas for proper air/fuel ratio | $102,672 | $4,000 | - | - | - |
$102,672
-
MMBtu
|
- | - | |
| 08 | 3.1181: Eliminate a by-product | $293,614 | $53,800 |
$554
(-18,480)
kWh
|
$560
-
kW-mo/yr
|
- | - |
$117,000
-
Tgal
|
$175,500
-
Tgal
|
|
| 09 | 2.3212: Optimize plant power factor | $40,258 | $23,660 | - | - | $40,258 | - | - | - | |
| TOTAL RECOMMENDED | $939,576 | $531,240 |
$11,449
344,673
kWh
|
$8,542
-
kW-mo/yr
|
$40,258 |
$226,827
-
MMBtu
|
$261,000
-
Tgal
|
$391,500
-
Tgal
|
||
| TOTAL IMPLEMENTED | $645,962 | $477,440 |
$10,895
363,153
kWh
|
$7,982
-
kW-mo/yr
|
$40,258 |
$226,827
-
MMBtu
|
$144,000
-
Tgal
|
$216,000
-
Tgal
|
||
| Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Electricity Fees Savings | Natural Gas Savings | Water Usage Savings | Water Disposal Savings | |||
*Savings and costs are best estimates based on the center's site visit, associated engineering analysis, and typical capital and labor costs