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UI Steam Plant Boiler Analysis MICHAEL CLARK BRIAN KISLING COLIN SOWARDS VINCE SCHWARTZ
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UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Dec 22, 2015

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Page 1: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

UI Steam Plant Boiler AnalysisMICHAEL CLARK BRIAN KISLING

COLIN SOWARDS VINCE SCHWARTZ

Page 2: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Goals•Synthesize given information

•Simplify the problem into reasonable terms/ideas

•Apply reasonable assumptions

•Keep records of all calculations

•Find Overall Heat Transfer Coefficient

•Find Heat Rate

•Assess possible performance improving options

Page 3: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Our Initial Model

T_in = 266 F x_in = 0P = 164.7 psiam_dot = 40800 lbm/hr

T_out = 365.9 Fx_out = 1

= 39,200,000 Btu/hr

Page 4: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Assumptions•Model the water/steam as pure (negate impurities)

•Flue Gas modeled as Air

•Steady State

•Boiler modeled as an adiabatic heat exchanger

•All pipes are equal diameter and have equal amounts of fouling on them

•Crossflow

Page 5: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Finding the Initial Q-ValueUse EES to calculate enthalpies

eq. 11.7a

= 39.2 MMBtu

Page 6: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Finding the T_inf-Valueeq. 11.6a

Setting the q’s equal to each other, and solving for the mass flow rate of the flue gas, the flue gas temperature can be backed out using the EES function call.

Page 7: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Analysis of the Pipes in the Boiler•1764 pipes• D_outside = 1.5 in• D_inside = 1.25 in• Mild steel

•Cross flow

•7 pipes per side

•Thermal Circuit

T_inf h_inf

Page 8: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Find the Convective Heat Transfer Coeff. (Outside & Inside)

Assume a constant pipe surface temperature

Find Necessary Pi-groups◦ Reynolds◦ Nusselt◦ Prandtl

eq. 7.53

(Laminar Flow) eq. 8.55

Page 9: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Thermal Circuit

Page 10: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Final AssessmentInitial boiler efficiency was thought to be around 76-78%

Our calculations put the boiler at a 77.8% efficiency

Overall Heat Transfer Coefficient;◦ U = 5.009 [Btu/hr-ft^2-R]

Rate of Heat Transfer◦ Q = 50.36 [MMBtu/hr]

Page 11: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Recommendations Replace the whole thing?

◦ NOPE◦ Too expensive◦ Would only improve the efficiency a minimal amount

Average commercial boilers tend to hover around 70% - 85% efficiency◦ Expensive boiler component additions would only

minimally increase overall efficiency

B.E.T Tube Cleaners◦ Increase boiler efficiency from 6% - 20%◦ Uses hourly compressed air/steam jets to clean pipes

Credit: fuelefficiencyllc.com

Page 12: UI Steam Plant Boiler Analysis MICHAEL CLARKBRIAN KISLING COLIN SOWARDSVINCE SCHWARTZ.

Questions/Comments/Critiques/Compliments•No questions

•No comments

•ABSOLUTELY no critiques• We’re all friends here, right?

•Just compliments