| Assessment Year | 2007 |
|---|---|
| Principal Product | sorbitol and maltitol |
| NAICS | 311930: Flavoring Syrup and Concentrate Manufacturing |
| SIC | 2869: Industrial Organic Chemicals, Not Elsewhere Classified |
| Sales Range | $50 M to 100M |
| # of Employees | 41 |
| Plant Area |
93,500
ft2
|
| Annual Production | 70,000
ton
|
| Production Hrs. Annual | 8,736
hrs
|
| Location (State) | Illinois |
Facility Energy Cost and Usage
| Source | Yearly Cost | Usage | Unit Cost | |
|---|---|---|---|---|
| Electricity Usage | $1,395,650 | 24,443,365 |
kWh
|
$0.057 |
| Electricity Demand | $191,513 | 40,798 |
kW-mo/yr
|
$4.69 |
| Natural Gas | $2,603,188 | 282,677 |
MMBtu
|
$9.21 |
| TOTAL YEARLY COSTS | - | |||
| RECOMMENDED SAVINGS* | $899,372 |
See individual recommendations below
*Non-energy impacts included in savings.
|
||
| IMPLEMENTED SAVINGS* | $87,197 | |||
Recommendations
| # | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Water Disposal Savings | Ancillary Material Cost Savings |
|---|---|---|---|---|---|---|---|---|---|
| 01 | 2.2437: Recover waste heat from equipment | $202,850 | $475,200 |
$22,123
388,110
kWh
|
$2,459
-
kW-mo/yr
|
$178,268
-
MMBtu
|
- | - | |
| 02 | 2.2437: Recover waste heat from equipment | $305,019 | $900,000 | - | - |
$293,046
-
MMBtu
|
$11,973
-
Tgal
|
- | |
| 03 | 2.3321: Use steam pressure reduction to generate power | $227,690 | $372,000 |
$227,690
3,994,560
kWh
|
- | - | - | - | |
| 04 | 2.2163: Use minimum steam operating pressure | $611 | - | - | - |
$494
-
MMBtu
|
$117
-
Tgal
|
- | |
| 05 | 2.8114: Change rate schedules or other changes in utility service | $36,000 | - |
$36,000
-
kWh
|
- | - | - | - | |
| 06 | 2.2614: Use cooling tower or economizer to replace chiller cooling | $21,910 | $4,260 |
$19,943
349,867
kWh
|
$1,967
-
kW-mo/yr
|
- | - | - | |
| 07 | 2.1233: Analyze flue gas for proper air/fuel ratio | $25,485 | $4,800 | - | - |
$25,485
-
MMBtu
|
- | - | |
| 08 | 2.4224: Upgrade controls on compressors | $12,731 | $18,755 |
$11,453
200,928
kWh
|
$1,278
-
kW-mo/yr
|
- | - | - | |
| 09 | 2.5111: Convert from indirect to direct fired systems | $52,577 | $43,780 | - | - |
$38,726
-
MMBtu
|
$13,851
-
Tgal
|
- | |
| 10 | 2.4323: Use optimum size and capacity equipment | $5,975 | $14,767 |
$5,975
104,832
kWh
|
- | - | - | - | |
| 11 | 2.4133: Use most efficient type of electric motors | $6,961 | $16,278 |
$6,073
106,587
kWh
|
$888
-
kW-mo/yr
|
- | - | - | |
| 12 | 2.6127: Maintain air filters by cleaning or replacement | $1,563 | - |
$2,667
46,803
kWh
|
$296
-
kW-mo/yr
|
- | - | $(-1,400.0) | |
| TOTAL RECOMMENDED | $899,372 | $1,849,840 |
$331,924
5,191,687
kWh
|
$6,888
-
kW-mo/yr
|
$536,019
-
MMBtu
|
$25,941
-
Tgal
|
$(-1,400.0) | ||
| TOTAL IMPLEMENTED | $87,197 | $64,858 |
$8,740
153,390
kWh
|
$1,184
-
kW-mo/yr
|
$64,705
-
MMBtu
|
$13,968
-
Tgal
|
$(-1,400.0) | ||
| Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Water Disposal Savings | Ancillary Material Cost Savings | |||
*Savings and costs are best estimates based on the center's site visit, associated engineering analysis, and typical capital and labor costs