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Compressed Air Walter Bright MAE406 – Energy Conservation in Industry [email protected] 10/29/2013

Compressed Air

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Compressed Air. Walter Bright MAE406 – Energy Conservation in Industry [email protected] 10/29/2013. C.A. Basics. C.A. Basics. Why Compressed Air?. Compressed air is simply a medium to transmit power, similar to electricity or steam to transmit heat - PowerPoint PPT Presentation

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Page 1: Compressed Air

Compressed Air

Walter BrightMAE406 – Energy Conservation in Industry

[email protected]/29/2013

Page 2: Compressed Air

C.A. BASICS

Page 3: Compressed Air

C.A. Basics• Compressed air is simply a medium to transmit

power, similar to electricity or steam to transmit heat

• Often referred to as the ‘fourth utility’ • Compressed air can be used for a multitude of

applications– Simple: Pumping up tires and blow-off nozzles– More Complex: Instrumentation, Vacuum generation,

Pneumatic tools, cylinders and valves• Ex: flow controllers, pumps, impact wrenches, nail guns, etc

– End-use equipment is cheap, lightweight, compact & powerful

– Explosive environments– Easy to control (solenoid valves, pressure

proportional to force)

Why Compressed Air?

Page 4: Compressed Air

C.A. Basics Basic Compressor

Specialized Bicycles/Popular Mechanics

Page 5: Compressed Air

C.A. Basics

$$$Typically the most expensive utility at a plantRule of Thumb: It takes 7 units of compressor

horsepower to provide one horsepower of useful work!Why is compressed air so expensive???

Ex: Cost of operating a 10hp motor for 1 year (8,760hrs) 10hp Electric Motor 10hp Pneumatic Motor

Why NOT Compressed Air?

$5,388

$32,818

Page 6: Compressed Air

C.A. Basics• Surely if it’s the most expensive utility at a

plant it’s being continuously managed…• Example:

– Foundry Sand Transport System– 350 hp of compressor power– Energy consumption reduced by 36%– $16,300 in annual savings– 1.3 year simple payback

• Substantial opportunity throughout industry to reduce compressed air usage and cost

• Plant personnel often think compressed air is free

Why Manage Compressed Air?

Compressed Air Challenge, www.compressedairchallenge.org

Page 7: Compressed Air

C.A. Basics Compression Thermodynamics

MOTOR

100 kW of electrical

energy input

COMP

Greg Harrell, Energy Management Services (EMS)

Page 8: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 9: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

# kW of loss??

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 10: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

98-99% Efficient

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 11: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

98-99% Efficient

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 12: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

98-99% Efficient

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 13: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

98-99% Efficient*

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 14: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

# kW of thermal energy loss??

98-99% Efficient*

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 15: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

90 kW of thermal energy loss

98-99% Efficient*

COMP

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 16: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

90 kW of thermal energy loss

98-99% Efficient*

COMP C.A.MTR

#kW of shaft

energy from comp. air motor??

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 17: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

90 kW of thermal energy loss

98-99% Efficient*

COMP C.A.MTR

10 to 20 kW of shaft

energy from comp. air motor

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 18: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

90 kW of thermal energy loss

98-99% Efficient*

COMP C.A.MTR

10 to 20 kW of shaft

energy from comp. air motor

What about the 1st Law of Thermo??

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 19: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

90 kW of thermal energy loss

98-99% Efficient*

COMP C.A.MTR

10 to 20 kW of shaft

energy from comp. air motor

The 1st Law of Thermo is not

violated because the air discharged is

very cold

Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 20: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

90 kW of thermal energy loss

98-99% Efficient*

COMP C.A.MTR

10 to 20 kW of shaft

energy from comp. air motor

The 1st Law of Thermo is not

violated because the air discharged is

very cold

COMPRESSION EFF:10-20%Greg Harrell, EMS

C.A. Basics Compression Thermodynamics

Page 21: Compressed Air

MOTOR

100 kW of electrical

energy input

5-8 kW of thermal energy

loss

We want high-pressure air from the compressor…

What we get is high-pressure,

high-temperature air

90 kW of thermal energy loss

98-99% Efficient*

COMP C.A.MTR

10 to 20 kW of shaft

energy from comp. air motor

The 1st Law of Thermo is not

violated because the air discharged is

very cold

COMPRESSION EFF:10-20%Greg Harrell, EMS

C.A. Basics Compression ThermodynamicsPROVE IT

Page 22: Compressed Air

THE C.A. SYSTEM

Page 23: Compressed Air

The C.A. System Typical System

Compressed Air Challenge

Supply Side Demand

Side

Page 24: Compressed Air

The C.A. System Supply Side

Types of Compressors

Compressed Air Challenge

Page 25: Compressed Air

The C.A. System• Analogy: Car IC

Engine• How it works:• Oil and Oil-free• Single-acting and

double-acting• Single or multi-

stage, depending on pressure/size

• Typically smaller units (less than 30hp*)

Supply SideReciprocating

Compressed Air Challenge (pg. 129)

Page 26: Compressed Air

The C.A. System

• Originally THE compressor technology

• Many vintage reciprocating compressors operating today, some in excess of 1,000 hp

• THE most efficient compressor technology (double-acting)

• Not used much today in industry

• 22-24 kW/100 cfm (single-acting), 15-16 kW/100 cfm (double-acting)

Supply SideReciprocating

Belliss and Morcom

Page 27: Compressed Air

The C.A. System

• Analogy: Car turbocharger

• How it works:– Impeller spinning at

10,000+ rpm• Typically larger units

(300 hp to >4,500 hp)• All Oil Free• Multi-stage, typically 2-

4 depending on size/pressure

• Centrifugal Compressor Animation

Supply SideCentrifugal

Page 28: Compressed Air

The C.A. System

• Low vibration, don’t need a heavy concrete pad like reciprocating

• Still very efficient

• Favored by industry today for large applications

• Operating range limited• 16-20 kW/100 cfm

Supply SideCentrifugal

Page 29: Compressed Air

The C.A. System Supply Side

Rotary Screw• Analogy: Car supercharger• How it works:

– Two screws meshed together which squeeze air

• Typically medium sized units (20 hp to 300 hp) but can be as large as 600 hp

• Oil and Oil Free• Typically single stage, some

larger units 2 stage

Page 30: Compressed Air

The C.A. System Supply Side

Rotary Screw

Ingersoll Rand

• By far, most common industrial air compressor today

• Low first cost, good efficiency, large operating range

• Variety of control techniques and manufacturers

• 17-22 kW/100 cfm (single stage)

Page 31: Compressed Air

The C.A. System

Supply SideRotary Screw (Lubricant-

Injected)

Credit: Ponna Pneumatic

Compressed Air/Oil MixtureOil (Lubricant)“Oil-Free” Compressed Air(2-3 ppm)

Page 32: Compressed Air

The C.A. System Supply SideDryers

Compressed Air Challenge

• Air dryers condense water out of compressed air• Air at 80°F and 50% = 60°F dewpoint and 0.01092 lbw/lba

• Compressed to 100 psig and 185°F, how much water in air?– Same! 0.01092 lbw/lba Squeeze water into space 8 times smaller (114.7/14.7=7.8)

• What is new dewpoint?– 125°F (Rule of Thumb: Double pressure, increase dewpoint by 20°F

• What happens if we send that air into a industrial plant that is 80°F ambient?– Rain inside compressed air pipes

Page 33: Compressed Air

The C.A. System

• Refrigerated dryers utilize a refrigerant circuit to condense moisture from the air stream

• Typical leaving dewpoint of 40°F• Cycling, non-cycling and head-unloading designs• 0.80 kW/100 cfm

Supply SideRefrigerated Dryers

Page 34: Compressed Air

The C.A. System

• Desiccant dryers use a desiccant to dry the air (via adsorption)

• Typical leaving dewpoint of -40°F to -100°F, depending on desiccant type

• Heatless, heat-assisted and blower-heat assisted designs• 2-3 kW/100 cfm

Supply SideDesiccant

Regenerative Dryers

Page 35: Compressed Air

The C.A. System• Storage (Air Receivers, piping, etc)• Pressure/Flow Controllers• After-coolers• Air/Lubricant Separators• Filters

– Particulate: Removes dirt/debris– Coalescing: Removes vapors (typically oil/lubricant

vapors)– Adsorption: Additional hydrocarbons and other

impurities• Traps and Drains

– Level operated– Timer operated– Zero-air loss

Supply SideAdditional

Components

Page 36: Compressed Air

The C.A. System• In a typical compressed air system,

how much air is used “appropriately” by production?

Demand SideUsage Breakdown

Compressed Air Challenge

• Leaks: Compressed air which leaks from distribution• Inappropriate Uses: Anything that compressed air is

used for which could be replaced via a more efficient process

• Increased Demand from Excessive System Pressure: Better known as artificial demand

Page 37: Compressed Air

The C.A. System• Pneumatic tools, cylinders, valves• Automation equipment• Instrumentation Air• Baghouses• Blow-off (special cases)• Motors/Pumps (where appropriate)• Etc.

Demand SideEnd-Users (Normal

Production)

Page 38: Compressed Air

The C.A. System

• Higher the system pressure, higher the leak rate– <2 cfm leak: can’t feel, can’t hear– 3-4 cfm leak: can feel, can’t hear– >5 cfm leak: can feel, can hear

• Leaks do more than waste energy– Shortens life of supply equipment because of increased

runtime– Buy/add new compressor capacity that is not needed

• Leak Table for a ‘perfect’ orifice (values are cfm)

Demand SideLeaks

Compressed Air Challenge

1/64” 1/32” 1/16” 1/8” 1/4” 3/8”70 psig 0.300 1.20 4.79 19.2 76.7 17380 psig 0.335 1.34 5.36 21.4 85.7 193

90 psig 0.370 1.48 5.92 23.8 94.8 213 100 psig 0.406 1.62 6.49 26.0 104 234

125 psig 0.494 1.98 7.90 31.6 126 284

Page 39: Compressed Air

The C.A. System

• An inappropriate use is anything that compressed air is currently used for, but has a more efficient alternative

Demand SideInappropriate Uses

DOE Tip Sheets

Potentially Inappropriate Uses

Suggested Alternatives/Actions

Clean-up, Drying, Process Cooling Low-pressure blowers, electric fans, brooms, nozzles

Sparging Low-pressure blowers and mixers

Aspirating, Atomizing Low-pressure blowers

Padding Low to medium-pressure blowers

Vacuum generator Dedicated vacuum pump or central vacuum system

Personnel cooling Electric fans

Open-tube, compressed air-operated vortex coolers without thermostats

Air-to-air heat exchanger or air conditioner, add thermostats to vortex cooler

Air motor-driven mixer Electric motor-driven mixer

Air-operated diaphragm pumps Proper regulator and speed control; electric pump

Idle equipment Put an air-stop valve at the compressed air inlet

Abandoned equipment Disconnect air supply to equipment

Page 40: Compressed Air

The C.A. System• If the pressure of the system is too

high, uncontrolled uses consume more air– For example, a system that is at 100 psig

has a leak load of 100 cfm. If the pressure is decreased, the leak rate is also decreased.

– An unregulated air cylinder• Reducing the pressure not only saves

energy because the compressor doesn’t have to work as hard, it also reduces the amount of air it has to generate

Demand SideArtificial Demand

Page 41: Compressed Air

The C.A. System• Compressed air systems are dynamic,

meaning that a spot check is not sufficient to determine how well it is operating

• Determining how a compressor is operating requires logging equipment

Measurements and Baselining

Page 42: Compressed Air

C.A. CONTROL STRATEGIES

Page 43: Compressed Air

C.A. Control Strategies• The simplest and most efficient control method• Turn compressor on and low pressure setpoint and

turn off at high pressure setpoint• Only practical for small motors

On/Off Control

Page 44: Compressed Air

C.A. Control Strategies• Compressor operates in a pressure dead-

band, similar to on/off• At upper band, instead of shutting off,

compressor “unloads”• Bleed off air/oil separator (~40 seconds)

– Only bleed down to ~40 psi– Why does it take 40 second to bleed sump?

• Wait for pressure to reach lower setpoint• Compress air/oil separator back to

operating pressure (~6 seconds)• Resume operation

Load/Unload Control

Page 45: Compressed Air

C.A. Control Strategies Lubricant-Injected Rotary Screw

Load/Unload Control

Credit: Ponna Pneumatic

Compressed Air/Oil MixtureOil (Lubricant)“Oil-Free” Compressed Air(2-3 ppm)

LoadedUnloadingUnloaded

Page 46: Compressed Air

C.A. Control Strategies Lubricant-Injected Rotary Screw

Load/Unload Control

Credit: Ponna Pneumatic

Compressed Air/Oil MixtureOil (Lubricant)“Oil-Free” Compressed Air(2-3 ppm)

LoadedLoadingUnloaded

Page 47: Compressed Air

C.A. Control Strategies• Storage plays a huge role in

load/unload power consumption

Lubricant-Injected Rotary ScrewLoad/Unload Control

Page 48: Compressed Air

C.A. Control Strategies Load/Unload Control

Compressed Air Challenge

Capacity of

TRIM

compressor!

Page 49: Compressed Air

C.A. Control Strategies• A low and high pressure limit as with

load/unload• Inlet valve modulates flow rate into

compressor– System pressure increases, inlet valve

closes– System pressure decreases, inlet valve

opens– No blowdown valve, sump always

pressurized• Pressure drop across inlet valve

– inlet pressure at screws decreases– increases pressure ratio, increases work

• Results in competition between savings and costs

Modulating Control

Page 50: Compressed Air

C.A. Control Strategies Modulating Control

Compressed Air Challenge

Page 51: Compressed Air

C.A. Control Strategies• Add variable speed drive to motor• Speed is proportional to capacity

– So at 80% speed, you produce roughly 80% of the rated capacity

• Less efficient than other types at 100% capacity– VFD drive consumes some power– Screws on constant speed machines can be

designed for a single speed. Screws on variable speed machines must pick a design point, typically about 80% of full speed.

Variable Speed Control

Compressed Air Challenge

Page 52: Compressed Air

C.A. Control Strategies Variable Speed Control

Compressed Air Challenge

Page 53: Compressed Air

C.A. ENERGY SAVINGS

55

Page 54: Compressed Air

C.A. Energy Savings• Compressed air leaks can be between 5

and 30% of system energy usage– Typically 20-30% for ‘unmanaged’ systems– Poorly maintained plants can be even more!

• Savings depend on type of compressor and control type, but applicable for all compressed air systems

Fix Compressed Air Leaks

Page 55: Compressed Air

C.A. Energy Savings• At $0.10/kWh, 8,760 hrs/yr• For a variable speed compressor:

Fix Compressed Air Leaks

Leak Volumetric Power Loss Demand Energy CostDiameter,

DFlow Rate,

VfL Reduction,

DRSavings Savings

(in) (cfm) (hp) (kW) (kWh/yr) ($/yr) 1/32 1.0 0.22 0.16 727 $72 1/16 4.0 0.88 0.66 2,908 $291 1/8 16.1 3.53 2.63 11,634 $1,163 1/4 64.6 14.11 10.53 46,535 $4,654• For a modulating compressor:Leak Volumetric Power Loss Demand Energy Cost

Diameter, D

Flow Rate, Vf

L Reduction, DR

Savings Savings

(in) (cfm) (hp) (kW) (kWh/yr) ($/yr) 1/32 1.0 0.22 0.048 218 $22 1/16 4.0 0.88 0.198 872 $87 1/8 16.1 3.53 0.789 3,490 $349 1/4 64.6 14.11 3.16 13,961 $1,396 • Ex: Reduce air leaks by 160 cfm, save $3,458/yr

Page 56: Compressed Air

C.A. Energy Savings• Pressure typically set at whatever compressor is

rated • Plant rarely needs that high of a pressure• Pressure should be set based on highest pressure

need– If the highest pressure need is 65 psig for a process line,

then the compressor should be set at a pressure to provide that 65 psig

– <100 psi is a typical header pressure• Rule of Thumb: 1% for every 2 psi reduction• Recall discussion about artificial demand• Example: Can we decrease pressure with system “as-

is?”– No, already below critical pressure at high demand!– Then modify the system

Reduce Compressor Pressure

Page 57: Compressed Air

C.A. Energy Savings• Screw compressors can switch from modulating to

load/unload very easily*– *Many compressors can do it at the flip of a switch, not

all– Storage is important (next slide)

• Difficult to retrofit from single speed to variable speed– Typically have to buy new compressor, even more pricy

• Interlink multiple compressors with network controls– Typically only useful for many compressor systems– Not as helpful in our example

• Overlapping control bands– With pressure fixed, control bands can be separated

Change Control Type/Setpoint

Page 58: Compressed Air

C.A. Energy Savings• Only for load/unload• Adding storage allows for compressor to run

unloaded for longer periods of time, resulting in lower overall energy usage

• Storage is expensive– $20,000 or more for 7,000 gal of storage

• What does 7,000 gallons look like?• What does 20,000 gallons look like?

• Add 4,000 gal of storage to system– Switch to Load/Unload– Lower control bands to appropriate points (18 psi

improvement)– Savings of $22,226/yr (this includes load/unload savings,

pressure reduction savings and overlapping control band savings)

Add Storage

Page 59: Compressed Air

C.A. Energy Savings• Cooling the air at the compressor inlet

reduces energy consumption• Doesn’t work for flooded-oil screw

compressors• Works well for reciprocating,

centrifugal and oil-free rotary screw compressors

Cool Compressor Inlet

Page 60: Compressed Air

C.A. Energy Savings• Baghouse pulse causes severe pressure

drops in system• 6 cubic foot pulse for 0.25 seconds every 1

minute• Instantaneous Flow:

– (6 ft3)/(.25 sec)x(60 sec/min) = 1,440 cfm• Average Flow

– (6 ft3)/(2 minutes)=6 cfm• Add secondary storage• Savings are hard to figure, likely from

productivity increase

High Volume, Intermittent Needs

Page 61: Compressed Air

C.A. Energy Savings• Air Knifes can be replaced with low

pressure blowers• Think about an industrial-strength hair

blower without the heat• High flow, low pressure

Low Pressure Blowers

Page 62: Compressed Air

C.A. Energy Savings• Use the 80-85% of energy wasted as

heat– If air cooled, use to heat areas during

winter– If water cooled, might be able to utilize

for boiler makeup water or other sources• Piping can get very expensive

• Low-grade heat, makes it difficult to capture

Utilize Compressor Waste Heat

Page 63: Compressed Air

C.A. Energy Savings• Facility not operating, still need

compressed air• Typically a result of a “dry” sprinkler

system• Compressed air pressurizes and fills

pipes, if a sprinkler head bursts the compressed air escapes and the water follows behind

• Typically need <5 hp to keep system pressurized

• Many companies run one compressor off-shift to pressurize system

• Savings for our example are $14,400/yr!

Off-Hours Compressed Air Use

Page 64: Compressed Air

C.A. Energy Savings• Savings are intertwined; cannot add savings

from other slides all together because effects are cumulative

• Summary– Eliminate Compressed Air Leaks– Reduce Pressure and Fix Control Bands– Add storage and switch to Load/Unload– Add low pressure blower for air knifes– Add new 5 hp compressor for sprinkler system

• Total savings: $66,331 or 65%!• Implementation cost likely below $30,000• Doesn’t include Productivity Increase!

Total Savings from Example

Page 65: Compressed Air

QUESTIONS???

67