water to water heat recovery

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Water to Water Heat Recovery Concepts and Applications Christian Rudio Product Manager Johnson Controls, Inc

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Presentation by Christian Rudio, STC water cooled product manager, Johnson Controls, at the May 11, 2010 Illinois Chapter ASHRAE seminar.

TRANSCRIPT

Page 1: Water to Water Heat Recovery

Water to Water Heat Recovery

Concepts and Applications

Christian Rudio

Product Manager

Johnson Controls, Inc

Page 2: Water to Water Heat Recovery

Trends and Topics

Industry Trends

� Energy Costs

� Green building movement

� Globalization – impact of Europe, Canada

� Manufacturer support and new products

Topics

� Fundamentals� Fundamentals

� Basic economics – the case for heat pumps

� Heat pump water distribution systems

� Heat pump arrangements

� Application examples

� Other heat recovery

� Questions

2

Page 3: Water to Water Heat Recovery

Basic Refrigeration Cycle

Fluid refrigerant absorbs heat from a load and rejects it to a sink

4 basic parts: compressor, condenser, expansion device, evaporator

1 to 2: Compress cold low-pressure gas to hot high-pressure gas

2 to 3: Reject heat to the sink, refrigerant condenses to hot liquid

3 to 4: Lower refrigerant temperature by rapidly lowering pressure

4 to 1: Evaporate refrigerant to absorb heat from the load

Hot liquid

Heat is rejected

3

Compressor

Condenser

Evaporator

ExpansionValve

Cold liquid

Hot liquid

Hot high-pressure gas

Cold low-pressure gas

Heat is absorbed

Work in

14

3

2

Page 4: Water to Water Heat Recovery

What is a heat pump?

Definition: A heating device that moves heat from low to high temperature.

Reversing type: Reversing systems change refrigerant flow direction with a reversing valve.

Each heat exchanger can act as an evaporator or a condenser depending on refrigerant flow

direction.

Non-reversing type: Evaporator and condenser do not change roles.

Hot liquid

Heat is produced

2

4

Compressor

Condenser

Evaporator

ExpansionValve

Cold liquid

Hot liquid

Hot high-pressure gas

Cold low-pressure gas

Heat is absorbed

Work in

14

3

2

Page 5: Water to Water Heat Recovery

When is a chiller not a chiller?

When machine is making hot water, it’s a heat pump, cold water is by-product.

When machine is making cold water, it’s a chiller, hot water is by-product.

Control condenser water temp or evaporator water temp – not both simultaneously.

Hot liquid

Heat is rejected

Hot liquid

Heat is produced

Chiller Heat Pump

5

Compressor

Condenser

Evaporator

ExpansionValve

Cold liquid

Hot liquid

Hot high-pressure gas

Cold low-pressure gas

Heat is absorbed

Work in

14

3

2

Compressor

Condenser

Evaporator

ExpansionValve

Cold liquid

Hot liquid

Hot high-pressure gas

Cold low-pressure gas

Heat is absorbed

Work in

14

3

2

Page 6: Water to Water Heat Recovery

Heat Pump vs. Energy Recovery

A heat pump’s purpose is to heat.

Energy recovery occurs when we extract waste heat from a chiller’s condenser and use it.

Control point is still chilled water set point.

Chiller with energy recovery

Condenser

Hot liquid

Hot high-

Some heat is rejected

2

Some heat is diverted and used

6

Compressor

Condenser

Evaporator

ExpansionValve

Cold liquid

Hot high-pressure gas

Cold low-pressure gas

Heat is absorbed

Work in

14

3

Page 7: Water to Water Heat Recovery

Other energy recovery methods

Desuperheater

• Heat exchanger in compressor discharge line

• 5-15% heat recovery

• Highest

Double Bundle Condenser

• Condenser circuit with “4-pipe” configuration –separate loop for heat

Water to Water Heat Pump

• Unit operating as heating device

• 100% recovery of cooling load plus work input

7

Water to Water Heat Pumps offer the most heat recovery, low first cost, direct control of

water temperature and most comply with ASHRAE 90.1 efficiency standards when operating

as a chiller

• Highest temperatures possible

• No direct control of water temp

heat

• 10-20% heat recovery

• No direct control of water temperature

work input

• Direct control of water temperature

Page 8: Water to Water Heat Recovery

The COP Advantage

Coefficient of Performance

� For a heat pump, COP = (Heat output) / (Work input)

� For electric resistive heaters, COP = 1. Heat output is equal to electrical power input.

� For fuel burning heaters with heat exchangers (like boilers), COP < 1.

� For heat pumps, COP > 1, often 2 < COP < 6.

How can heat pumps “produce” more heat than the input power?

Because heat pumps move heat from one place to another. The largest part of the

heating effect comes from heat that is pumped; not created, produced, or converted

8

from fuel.

Heating COP is calculated as:

in other words, Heating COP = (Heating effect) / (Work input)

How can heat pumps be more efficient than the chiller they’re based on?

Chiller COP is calculated as:

Therefore chiller COP will be slightly lower than heat pump COP for the same machine.

(∆Q = heat removed from cooling load and ∆W is work input to compressors)

Page 9: Water to Water Heat Recovery

The COP Advantage

Simultaneous Heating and Cooling

Combined COP

When machine is providing useful heating and cooling, combined COP is:

Because

9

Substitute for

Yields

Compared to

The benefit of combined heating and cooling is more than double the cooling COP for the same given conditions.

Page 10: Water to Water Heat Recovery

Specific Savings Example

COP – The economic lever

Quick cost analysis based on 165 ton positive displacement heat pump:

Heating Temperature 110 F � 125 F, 390 gpm

Evaporator water from 54 F � 44 F

(Illinois 2008 utility rates)

Boiler Heat Pump

10

Boiler Heat Pump

COP 0.85 3.55

Energy/Fuel Cost $11.49/MMBTU $0.0854/kWh

Heat Produced 2.68 MMBH 2.68 MMBH

Hours Run 4000 4000

Annual Heat Cost $ 144,614 $ 75,254

Annual Savings $ 69,360

Page 11: Water to Water Heat Recovery

Water Distribution Systems

Dedicated Heat Pump

Condenser water loop is dedicated to useful

heating.

– Best when the heating load is consistently

higher than heating capacity of the unit

Change-over Systems

Condenser water loop can reject heat to a cooling

tower (chiller mode), or divert it to provide useful

heating (heat pump mode).

– Additional Heat Sink allows chiller operation

when heating load is lower than unit capacity

Heat

Heat Sink

11

Dedicated System

Cooling Load

Heat Load

Hot waterWarm water

Cold water Cool water

Change-over System

Heat Load

Hot waterWarm water

Cold water Cool waterCooling

Load

Page 12: Water to Water Heat Recovery

Dedicated Heating Loop Example

Condenser water loop is dedicated to useful heating.

– Best when the heating load is consistently higher

than heating capacity of the unit

Heat Load

Hot waterWarm waterHigher evap temps

120 F108 F

HeatExchanger

Domestic coldwater 50 F

Preheated domesticwater 80 F

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Heat Sink

Dedicated System

Hot water

Cool water

Warm water

Cold water

Higher evap temps improve unit efficiency

(reduce lift)

Example

CHWR tocentral plant

54 F

54 F48F

54 F

53 F

Page 13: Water to Water Heat Recovery

Heat Pump Arrangements

Single Unit or Multiple Parallel Units

One unit or a team of parallel units make hot water.

– Advantages: Relatively simple piping and controls. Higher flow capacity.

– Disadvantages: Can only control hot or cold side. Limited temperature difference.

Heat Load

Hot waterWarm water

Heat

Load

Warm waterHot water

13

Heat Sink

Cold water ControlledCool water Heat

Sink

Controlled Cold water

Cool waterSingle Unit

Multiple Units in Parallel

Page 14: Water to Water Heat Recovery

Heat Pump Arrangements

Series Counterflow Units

Two chillers with series flow through the condensers and evaporators

– Advantages: Larger temperature differences are possible. Can control cooling with

one machine and heating with the other.

– Disadvantages: More complicated. Controls are critical. Flow must be the same

through both machines (machines similar or identical size).

100 F

Heat Load

130 F(controlled)115 F

14

Cooling Load

40 F(controlled)

60 F50 F

Two Units - Series Counter-flow Arrangement

Page 15: Water to Water Heat Recovery

Applications: Hot Water Preheat

Hospitals/Universities/Schools/Laboratories/Offices

– Buildings with fairly constant heating and cooling load profiles that require simultaneous

heating and cooling.

– Boiler feed water and/or domestic hot water is preheated to reduce fuel consumption.

Heating Plant Return Water

15

Central Plant Chilled Water Return

Central Chiller Plant

Central Heating PlantHeating Plant Return Water

Heat Pump

Page 16: Water to Water Heat Recovery

Heat Pump Arrangements

Cascade Chillers

– Advantages: Large temperature difference between heating and cooling loads. Can

control high and low temperature sides simultaneously.

– Disadvantages: More complicated. Condenser water treatment is critical. Controls

are critical. Geographically or seasonally limited (cooling tower temperatures).

Heat

Load120 F110 F

Small Heat Pump

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Cooling Load

36 F 46 F

60 F to cooling tower

50 F from cooling tower

60 F50 F

Large Chiller(s)

Small Heat Pump

Cascade Arrangement

Page 17: Water to Water Heat Recovery

Applications: Perimeter Reheat

Hospitals/Universities/Laboratories

– Buildings with fairly constant heating and cooling load profiles that require simultaneous

heating and cooling.

– VAV or perimeter heating loop primary heat source is heat pump; boiler used to

supplement as necessary for heating demand

– Previous economic example a good representation of Perimeter Reheat (50% run hours)

Supplemental

Boiler

17

Central Plant Chilled Water Return

Central Chiller Plant

Heating Loop Return

Heat Pump

VAV or Perimeter

Heat Loop

Page 18: Water to Water Heat Recovery

Applications: Hotel

Hotel Domestic Hot Water, or Laundry Water, or Pool Water Heating

– Typically need cooling in the building core, even in the winter; hot water is always in

demand.

– Use a cascade system to preheat domestic water.

Cooling Tower

Water

Heaters

Domestic Cold Water

Domestic Hot Water

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Large Chiller(s)Small Heat Pump

Heaters

Heat

Exchanger

Page 19: Water to Water Heat Recovery

Application Economics: Hotel

Hotel Domestic Hot Water, or Laundry Water, or Pool Water Heating

– Hotel in Wyoming where cooling tower water temperatures are useful for 1750 hours per

year (20%).

– Representative of a cascade system, where run hours are limited

– Same 165 ton heat pump as previous example

Boiler Heat Pump

COP 0.85 3.55

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COP 0.85 3.55

Energy/Fuel Cost $8.58/MMBTU $0.0667/kWh

Heat Produced 2.68 MMBH 2.68 MMBH

Hours Run 1750 1750

Annual Heat Cost $ 47,236 $ 25,715

Annual Savings $ 21,521

Page 20: Water to Water Heat Recovery

Application Example: Process/Manufacturing

Process/Manufacturing

– Process applications often have continuous and simultaneous heating and cooling needs.

– A series counter-flow arrangement allows for larger temperature differences and good

control on both hot and cold sides.

Heat Load

20

Mixing TankProcess Water Return Process Water Supply

Page 21: Water to Water Heat Recovery

Application Economics: Process/Manufacturing

Process/Manufacturing

– Brewery in IL runs continuously and can use heat pumps for 8000 hours per year

Boiler Heat Pump

COP 0.85 3.55

Energy/Fuel Cost $11.49/MMBTU $0.0854/kWh

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Energy/Fuel Cost $11.49/MMBTU $0.0854/kWh

Heat Produced 2.68 MMBH 2.68 MMBH

Hours Run 8000 8000

Annual Heat Cost $ 289,229 $ 150,509

Annual Savings $ 138,720

Page 22: Water to Water Heat Recovery

Application Consideration

Water temperature

Hotter water, less efficiency

� Operating cost vs. first cost (kW’s vs. coil rows)

� Higher temperatures a good fit for:

� Boiler pre-heat

� Retrofit projects (difficult to change air side coils)

� Up to 160F available commercially

� Equipment may not meet ASHRAE 90.1 chiller requirements

� Lower temperatures a good fit for:

� Perimeter reheat – coils can be sized for temperature

� New construction – additional coil row a small incremental cost

� Up to 140F – wide selection of equipment available, meets chiller efficiency requirements

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Page 23: Water to Water Heat Recovery

Application Consideration

Water temperature

Operating Cost Comparison

� 200 ton chiller with 20º F temperature difference across condenser

� Case #1: 120º to 140º F , heating-only COP 3.16, 3308 MBH heating, 193 tons cooling

� Case #2: 110º to 130º F, heating-only COP 3.70, 3308 MBH heating, 205 tons cooling

� Evaporator condition 54º to 44º F

� Illinois utility rates, 4000 run hours Case #1 Case #2

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Case #1 Case #2

Boiler Heat Pump Heat Pump

COP 0.85 3.55 3.55

Energy/Fuel Cost $11.49/MMBTU $0.0854/kWh $0.0854/kWh

Heat Produced 3.3 MMBH 3.3 MMBH 3.3 MMBH

Hours Run 4000 4000 4000

Annual Heat Cost $ 178,869 $ 104,871 $ 89,499

Annual Savings $ 73,997 $ 89,369

$15,000 Annual Savings for lower HWT – and more cooling capacity

Page 24: Water to Water Heat Recovery

Design Considerations

� Profile heating and cooling load profiles for properly designed system

� Buffer tanks can be critical between cascade and series systems, to add thermal mass

during quick temperature changes

� Control schemes must be carefully considered to avoid hunting

� When preheating domestic hot water, double heat exchanger must be used

� Water quality must be controlled as higher temperatures can accelerate fouling

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� Ground source should give careful consideration for water quality in evaporator

� Ground source typically leverage only heating or cooling COP, not combined

� Manufacturers can provide guidelines for equipment – temperature, flow limits – and

application advice