When Good Isn’t Enough: Advancing Firetube Boiler...

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When Good Isn’t Enough: Advancing Firetube Boiler Design

Presented by Steve Connor August, 2014

Presenter
Presentation Notes
Note: This presentation includes a full script under separate cover…

What We are Covering Today

2

Summary Focus areas for design change

The final results The design solutions

Brief on boiler evolution

Market drivers demanding

change

Advancing Firetube

Boiler Design

Boiler Evolution

3

• Egyptian boilers 5 – 6 BC • Hero’s Engine; 1st Century

BC

Hero’s Engine

Burner

Boiler

Steam drum

Egyptian Boilers

SOME OF THE FIRST

DISCOVERED BOILERS

Boiler Evolution

• Bronze cast Hot Water boiler

• 80 AD

4

HOT WATER BOILER FOUND

IN EUROPE

Boiler Evolution

5

Steam Locomotives

NOTE:

These firetube boilers could weigh up to

200,000lbs and reach speeds of 100mph

Boiler Evolution

6

Steam Locomotive Cut-A-Way

Furnace

Convection

Steam dome

Tube sheet

NOTE:

These boilers were an integral part in leading the way in the industrial revolution starting in

the 1860’s.

Boiler Evolution

7

Titanic Titanic Boiler Room

NOTE:

The Titanic was powered by 29 boilers that contained 159

furnaces which were fired with 825 tons of coal per day.

Boiler Evolution

• Shaft Horsepower based on 100 DF feedwater to reach 70 psi saturated

• 2,546 BTU/HR • Boiler horsepower: 33,475

BTU/HR • 2,546/33475 = 8% FTSE

8

NOTE:

At this time, boiler efficiency was not nearly as important as

the motive power.

Boiler Evolution

9

1946 1957 and Beyond

A STANDARD FOR FIRETUBE

CONSTRUCTION WAS CREATED

Market Drivers

• Energy Conservation • Footprint (square footage

and weight) • Emissions

10

What is driving the market today?

Focus Areas

• Reduce number of passes and tube count

• Improved radiant and convective heat transfer

• Enhance heat transfer coefficient & Reynolds number

• Lower furnace heat release rates

• Enhanced combustion & control

• CFD modeling • Structural analysis

11

Where should we focus our attention?

Improving Radiant & Convective Heat Transfer

• Lower heat release • Less weight • Smaller footprint • Longer life

12

Radiant

Convective

125,000 BTU/Ft3

BENEFITS FROM THE AREAS OF FOCUS

Reducing Weight and Footprint

13

• 30% less weight • 15% less floor space

Larger furnace Improve convection heat transfer

2 pass

NOTE:

These are attractive features to architects designing new boiler

rooms when faced with budget restraints.

Radiant Heat Transfer

14

• Large Delta T • High velocity • Turbulence • Excellent heat exchange • 60% of the heat energy absorbed

Furnace

NOTE:

The furnace transfers the greatest amount of heat than anywhere else in the boiler.

Convective Heat Transfer

Typical Boiler Tube

Extended Tube Surface

16

Boundary layer

Fins Dimples Spiraled

INCREASED INERTIA FORCES

= INCREASED HEAT

TRANSFER

Increasing Efficiency While Reducing Footprint

17

1st pass

2nd pass

Gas exit

Focus Areas

• Reduce number of passes and tube count

• Improved radiant and convective heat transfer

• Enhance heat transfer coefficient & Reynolds number

• Lower furnace heat release rates

• Enhanced combustion & control

18

How do we address market needs with regards to Efficiency and Emissions?

Low Emission & High Efficiency Burner

19

High Efficiency Low NOx Burner

Matching Burner to Furnace

20

20% firing rate 40% firing rate

• Time • Temperature • Turbulence

FACTORS TO CONSIDER

Combustion Control

21

Gun Burner- Single Point Positioning

FGR

Air Fuel

Drive motor Jackshaft

Combustion Control

22

Parallel Positioning System

Controlling Excess Air

23

15% excess air

Stoichiometric

Controlling Excess Air

24

RULE OF THUMB

For every 2% increase in O2, you lose 1% in efficiency

Controlling Excess Air

Excessive Time at Mid to Low Fire

Optimum range

Energy loss

25

Controlling the Excess Air

26

VFD Modulating Burner

Controlling Excess Air

27

Engineering, Designing & Testing for Constant 3%O2

Emission Reduction

28

Flue Gas Recirculation

Integral burner Gun burner

FGR

Emission Reduction

29

Fuel Air

Designing Boilers in the 21st Century

30

Is boiler R&D like it was in the past?

Computation Fluid Dynamics & Finite Element Analysis

31

CFD Modeling

FEA Proving

Structural Verification

32

Structural Analysis & Evaluation

33

Plain Furnace Corrugated Furnace

Corrugated furnace reduces plate thickness, but adds corrugating cost.

Metal Stresses

34

Tensile Strength

Metal Deformation

Tube Sheets

Tubes & Ligaments

Furnace

The Prototypes are Constructed

35

NOTE:

The prototypes take a fraction of the time to create now than in the past thanks to advances

in computer technology

The End Result

36

• 150, 200 & 250# Steam • 30# & 125# HW • 100 – 2200 HP • Natural gas & #2 oil or

combination • <60&30 PPM NOx 100-1200 HP

10:1 turndown with 3% O2 • <9 PPM NOx 100–1200 HP

(integral), 1300–2200 HP (Gun) • <5 PPM 500 – 680 HP (integral) • Parallel positioning standard • Nominal Efficiency 82.5% 100 –

2200 HP

CBEX Elite

CBEX Elite Features

Main Feature Set

• 150, 200 & 250# Steam • 30# & 125# HW • 100 – 1200 HP • Natural gas & #2 oil or

combination • <9 PPM NOx available • Parallel positioning

available 100-800 HP standard 900 – 1200 HP

• Turndown: 4:1 – 10:1 • O2: 3.5 (Mid-HF) – 8% (LF) • Efficiency: 81%

37

CBEX Premium

CBEX Premium Features

The Design Outcome

38

C-B Elite “Life Cycle Leader”

C-B Premium “The Value Choice”

. 15% Less Floor Space

. 20 – 30% Less Weight

Burner and Furnace Matching

39

Maximizing Radiant Heat Absorbtion

40

60%

Extended Tube Surfaces

41

2nd pass

Spiraled Tubes

Flue gas outlet

Maximize Combustion Control

42

Single Point Parallel Positioning

Market Drivers

• Energy Conservation • Footprint • Emissions • Maintained price/value

relationship • Increased boiler life

43

Summary • Firetube boilers have been evolving for years based on

customer needs. • The heating surface and gas passes can be reduced if

provisions are made for increasing radiant and convective heat transfer coefficients & Reynolds numbers.

• Extended surfaces in the tubes breakup the laminar flow, increasing heat transfer

• Reducing thermal NOx is a time/temperature relationship • Imperative the burner and the furnace be matched to

optimize results. • A 2% increase in O2 = 1% loss in efficiency • Most burners lose efficiency at mid to low fire • When selecting a boiler, check the efficiencies at all firing

rates. • Single point positioning is fine if burner doesn’t modulate

much.

44

Contact Us

45

David Brick Sales Engineer dbrick@cleaverbrooks.com 414-577-2736 cleaverbrooks.com