Write an energy audit report for PECO based on our March 11, 2008 visit. One savings recommendation, printed out, is due Wednesday April 16, 2008 in class. The complete report is due at our final exam on Monday April 28, 2008 at 4:30 pm. The report will be graded on accuracy, completeness, conciseness and clarity.
The report should have the following sections.
Cover Page
Table of Contents
Executive Summary (a paragraph or two which includes the following information)
“On March 11, 2008 our team visited your facility…”
Current annual electricity and fuel use
Current annual electricity and fuel cost, and total cost
Current annual CO2 emissions
Number of energy saving recommendations
Total cost savings and CO2 emission savings identified
Fraction of total cost savings identified to total energy cost
Fraction of total CO2 emission savings identified to total CO2 emissions
Summary of Recommendations
Table and one-paragraph description of each recommendation. A sample table
and description are shown below. The table is in EEM_Project.xls)

AR 1: Insulate Pipes, Tanks and Pump in
Steam System
Much of the steam delivery and condensate return system has little to no insulation. This uninsulated equipment loses heat during the year, therefore increasing the load on the boiler and creating more natural gas consumption. Furthermore, insulating these surfaces would create a safer plant environment. We recommend insulating all steam delivery and condensate return system equipment. We estimate this would save about $31,350 per year with a 3-month simple payback.
Electricity Use Analysis
Rate Schedule
Graph of monthly electricity use and demand
Table of monthly electricity use, demand and cost with annual totals
Lean Energy Analysis of electricity use versus outdoor air temperature with interpretation
Propane Use Analysis
Table of propane refill amounts and cost with annual totals
Exemplary Practices
Savings Recommendations
Write savings recommendations for:
Replace 400 W MH lights with 6-lamp T8 HBF lights
Replace Smooth V-belts with Notched V-belts
Install VFD on Chilled Water Pump
Fix Compressed Air Leaks
Install Ducts and Compress Outside Air
Purchase 25-hp Air Compressor
Turn Off Paint Booth Ventilation Fan When Not in Use
Install Control to Turn Off Hydraulic Motors When Not in Use
Install Photosensor to Regulate Compressed Air Blowoff
An example savings recommendation is included below. Each recommendation should start on a new page and include atleast one picture. Write completely and concisely. ‘Completely’ means that the origins of all numbers and all calculations used in the report are documented. Carry units in all calculations. ‘Concisely’ means that that each word in the report is essential to promote understanding. Eliminate redundancy and seek to convey your ideas with the minimum number of words.
Compressed air tool and leaking fitting
50-hp air compressor Compressed air intake
Paint booth Paint booth exhaust duct
Conveyor with continuous compressed air blowoff
Victorious energy assessment team
|
|
Annual Savings |
Project Cost |
Simple Payback |
||
|
Resource |
CO2 (tonnes) |
Dollars |
|||
|
Natural Gas |
4,145
mmBtu |
225 |
$31,350 |
$8,290 |
3 months |
Analysis
Much of the steam delivery and condensate return system has little to no insulation.
This uninsulated
equipment loses heat during the year, therefore increasing the load on the
boiler and creating more natural gas consumption. Furthermore, insulating these surfaces would
create a safer plant environment.
Recommendation
We recommend insulating all steam delivery and condensate return system equipment.
Estimated
Savings
Calculations are based on standard 2-inch thick fiberglass insulation with white jacketing and thermal conductivity of about 0.15 Btu/(hr-ft2-oF). The average plant temperature is estimated to be 70 F and the boiler is operated 7,200 hours per year.
The simulations indicate a total energy savings from insulating the steam delivery and condensate return system equipment to be about:
(446,777 Btu/hr + 39,518 Btu/hr + 42,258 Btu/hr + 6 x 9,442 Btu/hr) x 1 mmBtu / 1,000,000 Btu = 0.59 mmBtu/hr
0.59 mmBtu/hr x 7,200 hr/yr = 4,248 mmBtu/yr
4,248 mmBtu/yr x $7.38 /mmBtu = $31,350 /yr
The total reduction in plant CO2 emissions would be about:
4,248 mmBtu/year x 117 lb-CO2/mmBtu / (2,205 lbs/tonne) ≈ 225 tonnes-CO2 /year
Estimated Implementation Cost
Based on data from RSMeans Mechanical Costs Data 2002, both pipe and tank insulation costs about $10 per square foot including installation. Thus, the implementation cost would be about:
829 ft2 x $10 /ft2 = $8,290
Estimated Simple
Payback
$8,290 / $31,350 /yr
x 12 months/yr = 3 months