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Completed Projects
 Cable Life Study
Relay does not provide enough protection for the
transformer and cause terminal cables to overload
Cable’s life drops to 2.7 years from 40 years because of
overloading
Safety tip: TRACK card and be aware of hazards
Solutions: Shift devices to other line
Keep temperature traced till find long-term solution
Learnings from work:
Situational safety awareness
Team collaborations reinforced
Interpersonal and communication skills
Real-world experience with transformer and
breaker testing
One-line Diagrams for power transmission
and substations
SKMTools (Arc Flash)
AutoCAD
Thermodynamics (Energy)
On-going Project:
Develop visual risk ID of inspected substations
onTopographical map
CHP operation schedule and economic
analysis
Plant energy flow and cost model update
Identify and label overhead transmission lines
More research on cable overloading
Substation Score
UPP Substation 8.43776
North Main Switchyard 8.41877
Smelter Substation 8.40989
Copperton Substation 8.36902
Magna/PacifiCorp 8.31334
Refinery Substation 8.07266
6190 Switchyard 6.87315
Arthur Switchrack 5.39835
No.2 Substation 4.94158
South Main Substation 6.67596
About Me
 Master Student in Electrical Engineering at Case
Western Reserve University , Cleveland Ohio
 Graduate in May 2016
 Interested in Energy Optimization, Control
Systems and Automation
Utility Air
Ambient Air
Drain Water
Natural Gas
(from Questar)
Pulsing Timer Pulsing Timer
Air Filter
Evaprorative
Cooler
Gas Turbine & Generator Diverter Valve
Gas
Compressor
Oil Cooler
ATM
Combustion
Air Blower
Boiler
Steam
Feed Water
ATM
Condensate
Blowdown
Power
Gas Compressor
Silencer
Ambient Air
Duct
Burner
Feed Water
Xuan Wang—Electrical Engineer Intern
Energy System Optimization
Supervisor: DavidVan Hees
Optimization of Combined Heat
and Power (CHP) Operation
 Substation Inspections
Inspected Arthur Switchrack, No.2 Substation, and South
Main Substation, scheduled for Arthur Substation
Visual inspections on transformers, breakers, and control
buildings
SafetyTip: TRACK every inspection
Watch for warnings and signage
Keep accompanied
Wear PPE
Step 1
Compare the operational cost of CHP
with old Boilers
When generating the same amount of steam,
the CHP costs half as much as running the old
boiler
Break-even point:
When natural gas price is $ 13.4/mmBTU, Boiler
and CHP will have same operation cost.
Step 3
Create an energy flow model that
determines the energy input and output
of the Combined Heat and Process
system
PI data:
 Natural gas flow rate in SCFM and
temperature in °F
 Water flow rate in GPM and temperature in °
F
 Steam flow rate in LB/H, pressure in PSIG and
temperature in °F
Properties:
 Heat values of natural gas
 Water quality and properties
 Power generation
Work out the economic value of
running CHP and determine its
operational schedule
Step 2
Find out the most cost efficient way to
operate the CHP
Under the condition of fixed electricity and nat-
ural gas price , we can operate CHP for our en-
tire steam or power demand
Red — 44KV Transmission Lines
Purple — RMP Transmission Lines
Yellow — Lower Voltage Transmission Lines
Assumptions
 CHP and Boiler generation (power and
steam) meet plant demands
 Steam is a saturated
 Electricity import costs and natural gas price
are at $46/MWH and 2.18/mmBTU
Combine Heat Power Process Flow Diagram
CHP Generation
CHP & Boiler Steam Generation
Team members:
Hana Baesmat, BlakeWilde,
PerWenstad, Luke Kooyman,
Becca Novy

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Xuan's Poster Board

  • 1. Completed Projects  Cable Life Study Relay does not provide enough protection for the transformer and cause terminal cables to overload Cable’s life drops to 2.7 years from 40 years because of overloading Safety tip: TRACK card and be aware of hazards Solutions: Shift devices to other line Keep temperature traced till find long-term solution Learnings from work: Situational safety awareness Team collaborations reinforced Interpersonal and communication skills Real-world experience with transformer and breaker testing One-line Diagrams for power transmission and substations SKMTools (Arc Flash) AutoCAD Thermodynamics (Energy) On-going Project: Develop visual risk ID of inspected substations onTopographical map CHP operation schedule and economic analysis Plant energy flow and cost model update Identify and label overhead transmission lines More research on cable overloading Substation Score UPP Substation 8.43776 North Main Switchyard 8.41877 Smelter Substation 8.40989 Copperton Substation 8.36902 Magna/PacifiCorp 8.31334 Refinery Substation 8.07266 6190 Switchyard 6.87315 Arthur Switchrack 5.39835 No.2 Substation 4.94158 South Main Substation 6.67596 About Me  Master Student in Electrical Engineering at Case Western Reserve University , Cleveland Ohio  Graduate in May 2016  Interested in Energy Optimization, Control Systems and Automation Utility Air Ambient Air Drain Water Natural Gas (from Questar) Pulsing Timer Pulsing Timer Air Filter Evaprorative Cooler Gas Turbine & Generator Diverter Valve Gas Compressor Oil Cooler ATM Combustion Air Blower Boiler Steam Feed Water ATM Condensate Blowdown Power Gas Compressor Silencer Ambient Air Duct Burner Feed Water Xuan Wang—Electrical Engineer Intern Energy System Optimization Supervisor: DavidVan Hees Optimization of Combined Heat and Power (CHP) Operation  Substation Inspections Inspected Arthur Switchrack, No.2 Substation, and South Main Substation, scheduled for Arthur Substation Visual inspections on transformers, breakers, and control buildings SafetyTip: TRACK every inspection Watch for warnings and signage Keep accompanied Wear PPE Step 1 Compare the operational cost of CHP with old Boilers When generating the same amount of steam, the CHP costs half as much as running the old boiler Break-even point: When natural gas price is $ 13.4/mmBTU, Boiler and CHP will have same operation cost. Step 3 Create an energy flow model that determines the energy input and output of the Combined Heat and Process system PI data:  Natural gas flow rate in SCFM and temperature in °F  Water flow rate in GPM and temperature in ° F  Steam flow rate in LB/H, pressure in PSIG and temperature in °F Properties:  Heat values of natural gas  Water quality and properties  Power generation Work out the economic value of running CHP and determine its operational schedule Step 2 Find out the most cost efficient way to operate the CHP Under the condition of fixed electricity and nat- ural gas price , we can operate CHP for our en- tire steam or power demand Red — 44KV Transmission Lines Purple — RMP Transmission Lines Yellow — Lower Voltage Transmission Lines Assumptions  CHP and Boiler generation (power and steam) meet plant demands  Steam is a saturated  Electricity import costs and natural gas price are at $46/MWH and 2.18/mmBTU Combine Heat Power Process Flow Diagram CHP Generation CHP & Boiler Steam Generation Team members: Hana Baesmat, BlakeWilde, PerWenstad, Luke Kooyman, Becca Novy