Assessment Year | 1996 |
---|---|
Principal Product | Dried Fruits |
NAICS |
n/a
|
SIC | 2034: Dried and Dehydrated Fruits, Vegetables, and Soup Mixes |
Sales Range | $50 M to 100M |
# of Employees | 250 |
Plant Area |
100,000
ft2
|
Annual Production | 25,000
ton
|
Production Hrs. Annual | 4,160
hrs
|
Location (State) | California |
Facility Energy Cost and Usage
Source | Yearly Cost | Usage | Unit Cost | |
---|---|---|---|---|
Electricity Usage | $156,311 | 2,384,525 |
kWh
|
$0.066 |
Electricity Demand | $106,186 | 8,325 |
kW-mo/yr
|
$12.76 |
Natural Gas | $126,721 | 21,329 |
MMBtu
|
$5.94 |
TOTAL YEARLY COSTS | - | |||
RECOMMENDED SAVINGS* | $294,251 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
IMPLEMENTED SAVINGS* | $48,649 |
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 |
---|---|---|---|---|---|---|---|---|---|
01 | 2.1243: Use heat from boiler blowdown to preheat boiler feed water | $7,415 | $8,500 | - | - |
$7,415
-
MMBtu
|
- | - | |
02 | 2.7142: Utilize higher efficiency lamps and/or ballasts | $6,960 | $20,930 |
$3,914
59,789
kWh
|
$3,046
-
kW-mo/yr
|
- | - | - | |
03 | 2.1311: Replace electrically-operated equipment with fossil fuel equipment | $5,794 | $9,792 |
$3,273
49,824
kWh
|
$3,674
-
kW-mo/yr
|
$(-1,153.0)
-
MMBtu
|
- | - | |
04 | 2.4239: Eliminate or reduce compressed air usage | $3,011 | $4,970 |
$1,418
22,860
kWh
|
$1,593
-
kW-mo/yr
|
- | - | - | |
05 | 2.4133: Use most efficient type of electric motors | $2,069 | $1,792 |
$1,125
17,292
kWh
|
$944
-
kW-mo/yr
|
- | - | - | |
06 | 2.6218: Turn off equipment when not in use | $1,248 | $2,120 |
$1,220
18,464
kWh
|
$28
-
kW-mo/yr
|
- | - | - | |
07 | 2.2122: Install / repair insulation on condensate lines | $663 | $1,089 | - | - |
$663
-
MMBtu
|
- | - | |
08 | 2.2135: Repair and eliminate steam leaks | $558 | $375 | - | - |
$558
-
MMBtu
|
- | - | |
09 | 2.4236: Eliminate leaks in inert gas and compressed air lines/ valves | $1,017 | $120 |
$651
9,672
kWh
|
$366
-
kW-mo/yr
|
- | - | - | |
10 | 2.4239: Eliminate or reduce compressed air usage | $932 | $500 |
$597
9,086
kWh
|
$335
-
kW-mo/yr
|
- | - | - | |
11 | 3.4131: Minimize contamination of water before treatment | $171,634 | $672,500 | - | - | - |
$171,634
-
Tgal
|
- | |
12 | 3.3131: Use evaporation to concentrate material | $65,621 | $78,072 | - | - | - |
$65,621
-
Tgal
|
- | |
13 | 3.5314: Use in-process recycling whenever possible | $12,812 | $250 | - | - | - | - |
$12,812
-
lb
|
|
14 | 3.4113: Treat and reuse rinse waters | $14,517 | $3,115 | - | - | - |
$14,517
-
Tgal
|
- | |
TOTAL RECOMMENDED | $294,251 | $804,125 |
$12,198
186,987
kWh
|
$9,986
-
kW-mo/yr
|
$7,483
-
MMBtu
|
$251,772
-
Tgal
|
$12,812
-
lb
|
||
TOTAL IMPLEMENTED | $48,649 | $44,553 |
$11,601
177,901
kWh
|
$9,651
-
kW-mo/yr
|
$68
-
MMBtu
|
$14,517
-
Tgal
|
$12,812
-
lb
|
||
Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Water Disposal Savings | Solid Waste (non-haz) Savings |
*Savings and costs are best estimates based on the center's site visit, associated engineering analysis, and typical capital and labor costs