Assessment Year | 2017 |
---|---|
Principal Product | Iso-E, Geraniol, Pine Oil |
NAICS | 325199: All Other Basic Organic Chemical Manufacturing |
SIC | 2869: Industrial Organic Chemicals, Not Elsewhere Classified |
Sales Range | $50 M to 100M |
# of Employees | 89 |
Plant Area |
1,100,000
ft2
|
Annual Production | 22,274
ton
|
Production Hrs. Annual | 8,736
hrs
|
Location (State) | Florida |
Facility Energy Cost and Usage
Source | Yearly Cost | Usage | Unit Cost | ||
---|---|---|---|---|---|
Electricity Usage | $1,161,881 | 21,324,017 |
kWh
|
$0.054 | |
Electricity Demand | $237,928 | 34,810 |
kW-mo/yr
|
$6.84 | |
Electricity Fees | $179,996 | - |
|
- | |
Natural Gas | $2,228,418 | 456,062 |
MMBtu
|
$4.89 | |
Waste Disposal Costs | |||||
Water Usage | $19,081 | 4,990 |
Tgal
|
$3.82 | |
Water Disposal | $703,265 | 59,983 |
Tgal
|
$11.72 | |
TOTAL YEARLY COSTS | $4,530,569 | ||||
RECOMMENDED SAVINGS* | $953,722 |
See individual recommendations below
*Non-energy impacts included in savings.
|
|||
IMPLEMENTED SAVINGS* | $527,397 |
Recommendations
# | Description | Yearly Savings* | Imp'd Cost* | Status | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Water Usage Savings | Personnel Changes Savings | Administrative Changes Savings | By-product Production Savings |
---|---|---|---|---|---|---|---|---|---|---|---|
01 | 2.3416: Use combined cycle gas turbine generator sets with waste heat boilers connected to turbine exhaust | $401,159 | $2,500,000 |
$1,182,600
21,900,000
kWh
|
- |
$(-474,841.0)
-
MMBtu
|
- | - | $(-306,600.0) | - | |
02 | 2.2522: Isolate hot or cold equipment | $124,880 | $17,000 |
$124,880
2,312,640
kWh
|
- | - | - | - | - | - | |
03 | 2.3212: Optimize plant power factor | $38,189 | $13,000 |
$38,189
707,200
kWh
|
- | - | - | - | - | - | |
04 | 2.3131: Reschedule plant operations or reduce load to avoid peaks | $23,030 | $40,000 |
$23,030
426,480
kWh
|
- | - | - | - | - | - | |
05 | 2.2112: Use correct size steam traps | $27,893 | $340 | - | - |
$27,893
-
MMBtu
|
- | - | - | - | |
06 | 2.6231: Utilize controls to operate equipment only when needed | $10,845 | $2,750 |
$10,845
200,809
kWh
|
- | - | - | - | - | - | |
07 | 2.2623: Minimize condenser cooling water temperature | $26,348 | $725 |
$26,348
487,582
kWh
|
- | - | - | - | - | - | |
08 | 2.7243: Improve air circulation with destratification fans / other methods | $9,636 | $6,225 |
$4,324
80,066
kWh
|
$749
-
kW-mo/yr
|
- | - | $4,563 | - | - | |
09 | 2.2121: Increase amount of condensate returned | $4,891 | - | - | - |
$3,068
-
MMBtu
|
$1,823
-
Tgal
|
- | - | - | |
10 | 2.4225: Install common header on compressors | $3,951 | $11,185 |
$3,951
73,164
kWh
|
- | - | - | - | - | - | |
11 | 2.4234: Cool compressor air intake with heat exchanger | $2,136 | $1,562 |
$2,136
39,560
kWh
|
- | - | - | - | - | - | |
12 | 3.3128: Utilize other methods to remove contaminants | $280,764 | $300,000 | - | - | - | - | - | - | $280,764 | |
TOTAL RECOMMENDED | $953,722 | $2,892,787 |
$1,416,303
26,227,501
kWh
|
$749
-
kW-mo/yr
|
$(-443,880.0)
-
MMBtu
|
$1,823
-
Tgal
|
$4,563 | $(-306,600.0) | $280,764 | ||
TOTAL IMPLEMENTED | $527,397 | $351,225 |
$208,537
3,861,461
kWh
|
$749
-
kW-mo/yr
|
$30,961
-
MMBtu
|
$1,823
-
Tgal
|
$4,563 | - | $280,764 | ||
Yearly Savings* | Imp'd Cost* | Electricity Usage Savings | Electricity Demand Savings | Natural Gas Savings | Water Usage Savings | Personnel Changes Savings | Administrative Changes 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