Danfoss Application Handbook - Automatic Controls for Industrial Refrigeration Systems Mode d'emploi

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Application Handbook

Industrial Refrigeration

Ammonia and CO

2

applications

MAKING MODERN LIVING POSSIBLE

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

Contents Page

Foreword.......................................................................................................... 3

1. Introduction .................................................................................................... 4

2. Compressor Controls ............................................................................................ 6

2.1 Compressor Capacity Control .............................................................................. 6

2.2 Discharge Temperature - Control with Liquid Injection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 10

2.3 Crankcase Pressure Control ...............................................................................13

2.4 Reverse Flow Control .....................................................................................14

2.5 Summary.................................................................................................15

2.6 Reference Documents ....................................................................................16

3. Condenser Controls ............................................................................................17

3.1 Air Cooled Condensers....................................................................................17

3.2 Evaporative Condensers ..................................................................................22

3.3 Water Cooled Condensers.................................................................................25

3.4 Summary.................................................................................................27

3.5 Reference Documents ....................................................................................27

4. Liquid Level Control ............................................................................................28

4.1 High Pressure Liquid Level Control System (HP LLRS).......................................................28

4.2 Low Pressure Liquid Level Control System (LP LLRS)........................................................32

4.3 Summary.................................................................................................36

4.4 Reference Documents ....................................................................................36

5. Evaporator Controls . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 37

5.1 Direct Expansion Control..................................................................................37

5.2 Pumped Liquid Circulation Control ........................................................................42

5.3 Hot Gas Defrost for DX Air Coolers.........................................................................45

5.4 Hot Gas Defrost for Pumped Liquid Circulation Air Coolers .................................................51

5.5 Multi Temperature Changeover ...........................................................................54

5.6 Media Temperature Control ...............................................................................55

5.7 Summary.................................................................................................57

5.8 Reference Documents ....................................................................................58

6. Oil Systems ....................................................................................................59

6.1 Oil cooling ...............................................................................................59

6.2 Oil Dierential Pressure Control ...........................................................................63

6.3 Oil Recovery System ......................................................................................66

6.4 Summary.................................................................................................68

6.5 Reference Documents ....................................................................................69

7. Safety systems .................................................................................................70

7.1 Pressure Relief Devices....................................................................................70

7.2 Pressure and Temperature Limiting Devices ...............................................................74

7.3 Liquid Level Devices ......................................................................................75

7.4 Refrigerant detector ......................................................................................76

7.5 Summary.................................................................................................78

7.6 Reference Documents ....................................................................................78

8. Refrigerant Pump Controls .....................................................................................79

8.1 Pump Protection with Dierential Pressure Control ........................................................79

8.2 Pump Bypass Flow Control................................................................................81

8.3 Pump Pressure Control....................................................................................82

8.4 Summary.................................................................................................83

8.5 Reference Documents ....................................................................................83

9. Others .........................................................................................................84

9.1 Filter Driers in Fluorinated Systems ........................................................................84

9.2 Water Removal for Ammonia Systems .....................................................................86

9.3 Air purging systems.......................................................................................90

9.4 Heat Recovery System ....................................................................................92

9.5 Reference Documents ....................................................................................94

10. Using CO

2

in refrigeration systems .............................................................................95

10.1 CO

2

as a refrigerant ......................................................................................96

10.2 CO

2

as a refrigerant in industrial systems..................................................................97

10.3 Design pressure .........................................................................................99

10.4 Safety ..................................................................................................101

10.5 Eciency ..............................................................................................102

10.6 Oil in CO

2

systems ......................................................................................102

10.7 Comparison of component requirements in CO

2

, ammonia and R134a systems ...........................104

10.8 Water in CO

2

Systems ...................................................................................106

10.9 Removing water........................................................................................109

10.10 How does water enter a CO

2

system? ...................................................................113

10.11 Miscellaneous features to be taken into consideration in CO

2

refrigeration systems ......................114

11. Pumped CO

2

in Industrial Refrigeration Systems...............................................................117

12. Control methods for CO

2

systems .............................................................................127

13. Design of a CO

2

sub-critical installation .......................................................................128

13.1 Electronic solution for liquid level control ...............................................................128

13.2 Hot Gas Defrost for Pumped Liquid Circulation Air Coolers ...............................................129

13.2 Hot Gas Defrost for Pumped Liquid Circulation Air Coolers ...............................................130

14. Filter Driers in CO

2

Systems . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 131

15. Danfoss sub-critical CO

2

components.........................................................................132

16. Full range of stainless steel products .........................................................................134

17. Appendix ....................................................................................................136

Reference Documents - Alphabetical overview...................................................................149

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

Foreword

This Danfoss application guide is designed

to be used as a reference document by all

those involved in the workings of industrial

refrigeration systems.

This guide aims to provide answers to the various

questions relating to industrial refrigeration

system control: - Why a type of control method

is necessary for the refrigeration system? Why

should it be designed in this way? What type of

components can be used? How to select control

methods for dierent refrigeration systems? In

answering these questions, the principles of the

dierent control methods are introduce followed

by same control examples, comprising Danfoss

Industrial Refrigeration products.

The main technical data of the components is

also provided. Finally, comparisons between

dierent solutions for each control method are

made, so that the reader should know how to

select a solution.

In this application guide, the pilot-operated servo

valve ICS is recommended as a pressure and

temperature regulator. Please note that the well

established PM valve could also be applied where

ICS is used.

The application guide is designed to be used

as a reference document. The guide aims to

provide answers to the various questions relating

to industrial refrigeration system control and

in answering these questions, the principles of

the dierent control methods are introduced

followed by some control examples, comprising

Danfoss Industrial Refrigeration products. It

is non capacity and performance related and

operating parameters of each application should

be considered accordingly before adopting any

particular layout.

Not all valves are shown and the application

drawings are not to be used for construction

purposes.

For the nal design of the installation it is

necessary to use other tools, such as the

manufacturer’s catalogues and calculation

software (e.g. Danfoss Industrial Refrigeration

catalogue and DIRcalc software).

DIRcalc is the software for calculation and

selection of Danfoss Industrial Refrigeration

valves. DIRcalc is delivered free of charge.

Please contact your local Danfoss sales company.

Please do not hesitate to contact Danfoss, if

you have questions about control methods,

application and controls described in this

application guide.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

4 DKRCI.PA.000.C4.02 / 520H1623 © Danfoss A/S (AC-SMC/MWA), 2013-02

1. Introduction

Refrigeration System with Pump Circulation

Danfoss

Tapp_0015_02

10-2012

À

Compressor Control

Why?

– Primary: to control the suction pressure;

– Secondary: reliable compressor operation

(start/stop, etc.)

How?

– Control the compressor capacity according

to the refrigeration load by means of

bypassing hot gas from the HP side back into

the LP side, compressor ON/OFF step control or

controling the rotating speed of the

compressor;

– Install check valve on the discharge line in

order to prevent reverse ow of the refrigerant

to the compressor;

– Keep pressures and temperatures on the inlet

and outlet of the compressor within the

working range.

Á

Oil control

Why?

– Keep optimal oil temperature and pressure

in order to guarantee reliable compressor

operation.

How?

– Pressure: maintain and control the pressure

dierential across the compressor for oil

circulation, maintain the crankcase pressure

(only for piston compressors);

– Temperature: bypass some oil around the oil

cooler; control the cooling air or water to the

oil cooler;

– Level: return the oil in ammonia systems and

low temperature uorinated systems.

Oil

separator

Oil cooler

Condenser

Receiver

Liquid separator

Expansion

valve 1

Refrigerant pump

Evaporator

LP vapour refrigerant

LP liquid refrigerant

Oil

HP vapour refrigerant

HP liquid refrigerant

Liquid/vapour mixture of refrigerant

Compressor

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

1. Introduction

(continued)

Â

Condenser Control

Why?

– Maintain the condensing pressure above the

minimum acceptable value in order to

guarantee sucient ow through the

expansion devices;

– Ensure the right distribution of the refrigerant

in the system.

How?

– On/o operation or control the speed of the

condenser fans, control the ow of the cooling

water, ood the condensers with liquid

refrigerant.

Ã

Liquid Level Control

Why?

– Provide the correct ow of liquid refrigerant

from the high pressure side to the low pressure

side according to the actual demand;

– Ensure safe and reliable operation of the

expansion devices.

How?

– Control the opening degree of the expansion

device according to the change of the liquid

level.

Ä

Refrigerant Pump Control

Why?

– Maintain the pump running in trouble free

mode by maintaining the ow through the

pump within the permissible operating range;

– Maintain a constant dierential pressure across

the pump in some systems.

How?

– Design a bypass loop so that the ow can be

maintained above the minimum permissible

ow;

– Shut o the pump if it fails to build up enough

dierential pressure.

– Install a pressure regulating valve.

Å

Evaporating System Control

Why?

– Primary: maintain a constant media

temperature;

– Secondary: optimise operation of the

evaporators;

– For direct expansion systems: guarantee

that no liquid refrigerant from the evaporators

enters the suction line of the compressor.

How?

– Change the ow rate of the refrigerant into

evaporators according to the demand;

– Defrost evaporators.

Æ

Safety Systems

Why?

– Avoid unintended pressure of the vessels;

– Protect the compressor from being damaged

by liquid hammering, overloading, oil shortage

and high temperature, etc;

– Protect the pump from being damaged by

cavitation.

How?

– Install safety relief valve on vessels and other

necessary places;

– Shut o the compressor and pump if the

inlet/outlet pressure or dierential is out of

permissible range;

– Shut o the system of part of the system when

the level in the liquid separator or the receiver

exceeds the permissible level.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

6 DKRCI.PA.000.C4.02 / 520H1623 © Danfoss A/S (AC-SMC/MWA), 2013-02

2. Compressor Controls

The compressor is the “heart” of the refrigeration

system. It has two basic functions:

1. Maintain the pressure in the evaporator so

that the liquid refrigerant can evaporate at the

required temperature;

2. Compress the refrigerant so that it can be

condensed at a normal temperature.

The basic function of compressor control,

therefore, is to adjust the capacity of the

compressor to the actual demand of the

refrigeration system so that the required

evaporating temperature can be maintained.

If the compressor capacity is bigger than

the demand, the evaporating pressure and

temperature will be lower than that required, and

vice versa.

Additionally, the compressor should not be

allowed to operate outside of the acceptable

temperature and pressure range, in order to

optimise its running conditions.

2.1

Compressor Capacity Control

The compressor in a refrigeration system is

normally selected to be able to satisfy the highest

possible cooling load. However, the cooling load

during normal operation is usually lower than the

design cooling load. This means that it is always

necessary to control the compressor capacity so

that it matches the actual heat load. There are

several common ways to control the compressor

capacity:

1. Step control.

This means to unload cylinders in a multi-cylinder

compressor, to open and close the suction ports

of a screw compressor, or to start and stop some

compressors in a multi-compressor system. This

system is simple and convenient. Furthermore,

eciency decreases very little during part-load.

It is especially applicable to systems with several

multi-cylinder reciprocating compressors.

2. Slide valve control.

The most common device used to control the

capacity of a screw compressor is the slide valve.

The action of the oil-driven slide valve allows

part of the suction gas to avoid from being

compressed. The slide valve permits a smooth

and continuous modulation of capacity from

100% down to 10%, but the eciency drops at

part load.

3. Variable speed control.

Variable speed regulation. This solution is

applicable to all kinds of compressors, and

is ecient. A two-speed electric motor or a

frequency converter can be used to vary the

speed of the compressor. The two-speed electric

motor regulates the compressor capacity by

running at the high speed when the heat load is

high (e.g. cooling down period) and at the low

speed when the heat load is low (e.g. storage

period). The frequency converter can vary the

rotation speed continuously to satisfy the actual

demand. The frequency converter observes

limits for min. and max. speed, temperature and

pressure control, protection of compressor motor

as well as current and torque limits. Frequency

converters oer a low start up current.

4. Hot gas bypass.

This solution is applicable to compressors with

xed capacities and more typical for commercial

refrigeration. In order to control the refrigeration

capacity, part of the hot gas ow on the

discharge line is bypassed into the low pressure

circuit. This helps to decrease the refrigeration

capacity in two ways: by diminishing the supply

of liquid refrigerant and releasing some heat into

the low pressure circuit.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

Application example 2.1.1:

Step control of compressor

capacity

À

Step Controller

Á

Pressure Transmitter

Danfoss

Tapp_0016

10-2012

HP vapour refrigerant

LP vapour refrigerant

Oil

Step control solution for compressor capacity can

be achieved by using a step controller EKC 331 À.

EKC 331 is a four-step controller with up to four

relay outputs. It controls the loading/unloading

of the compressors/pistons or the electric motor

of the compressor according to the suction

pressure signal from the pressure transmitter AKS

33 Á or AKS 32R. Based on a neutral zone control,

EKC 331 can control a pack system with up to four

equally sized compressor steps or alternatively

two capacity controlled compressors (each

having one unload valve).

EKC 331T version can accept a signal from a

PT 1000 temperature sensor, which may be

necessary for secondary systems.

Neutral Zone Control

A neutral zone is set around the reference value,

in which no loading/unloading occurs.

Outside the neutral zone (in the hatched areas

“+zone” and “- zone”) loading/unloading will

occur as the measure pressure deviates away

from the neutral zone settings.

If control takes place outside the hatched area

(named ++zone and --zone), changes of the cut-

in capacity will occur somewhat faster than if it

were in the hatched area.

For more details, please refer to the manual of

EKC 331(T) from Danfoss.

Technical data

Pressure transmitter-AKS 33 Pressure transmitter-AKS 32R

Refrigerants All refrigerants including R717 All refrigerants including R717

Operating range [bar] –1 to 34 –1 to 34

Max. working pressure PB [bar] 55 (depending on operating range) 60 (depending on operating range)

Operating temp. range [°C] –40 to 85

Compensated temp. range [°C] LP: –30 to +40 / HP: 0 to +80

Rated output signal 4 to 20 mA 10 to 90% of V supply

Pressure transmitter - AKS 3000 Pressure transmitter - AKS 32

Refrigerants All refrigerants including R717 All refrigerants including R717

Operating range [bar] 0 to 60 (depending on range) –1 to 39 (depending on range)

Max. working pressure PB [bar] 100 (depending on operating range) 60 (depending on operating range)

Operating temp. range [°C] –40 to 80 –40 to 85

Compensated temp. range [°C] LP: –30 to +40 / HP: 0 to +80 LP: –30 to +40 / HP: 0 to +80

Rated output signal 4 to 20 mA 1 to 5V or 0 to 10V

From liquid

separator

evaporator

Piston compressor

To

condenser

Oil

separator

Not all valves are shown.

Not to be used for construction

purposes.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

8 DKRCI.PA.000.C4.02 / 520H1623 © Danfoss A/S (AC-SMC/MWA), 2013-02

Application example 2.1.2:

Compressor capacity control

by hot gas bypass

À

Stop valve

Á

Capacity regulator

Â

Stop valve

Danfoss

Tapp_0017

10-2012

HP vapour refrigerant

HP liquid refrigerant

LP vapour refrigerant

LP liquid refrigerant

Oil

Hot gas bypass can be used to control the

refrigeration capacity for compressors with xed

capacity. The pilot-operated servo valve ICS

Á with a CVC pilot valve is used to control the

hot gas bypass ow according to the pressure

on the suction line. The CVC is a back pressure

controlled pilot valve, which opens the ICS and

increases the ow of hot gas when the suction

pressure is below the set value. In this way, the

suction pressure ahead of the compressor is kept

constant, therefore the refrigeration capacity

satises the actual cooling load.

Technical data

Pilot-operated servo valve - ICS

Material Body: low temp. steel

Refrigerants All common refrigerants, incl. R717 and R744

Media temp. range [°C] –60 to +120

Max. working pressure [bar} 52

DN [mm] 20 to 150

Pilot valve - CVC (LP)

Refrigerants All common refrigerants

Media temp. range [°C] –50 to 120

Max. working pressure [bar] High pressure side: 28

Low pressure side: 17

Pressure range [bar] –0.45 to 7

K

v

value [m

3

/h] 0.2

Pilot valve - CVC (XP)

Refrigerants All common refrigerants

Media temp. range [°C] –50 to 120

Max. working pressure [bar] High pressure side: 52

Low pressure side: 28

Pressure range [bar] 4 to 28

K

v

value [m

3

/h] 0.2

Compressor

To

condenser

From receiver

Evaporator

Oil

separator

Not all valves are shown.

Not to be used for construction

purposes.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

Application example 2.1.3:

Compressor variable speed

capacity control

Danfoss

Tapp_0139

10-2012

À

Frequency converter

Á

Controller

Â

Pressure transducer

HP vapour refrigerant

LP vapour refrigerant

Frequency converter control oer the following

advantages:

Energy savings

Improved control and product quality

Noise reduction

Longer lifetime

Simplied installation

Easy to use complete control of the system

Technical data

Frequency converter AKD 102

Frequency converter

VLT FC 102 / FC 302

kW rating 1.1 kW to 45 kW 1.1 kW to 250 kW Up to 1200 kW

Voltage 200-240 V 380-480 V 200-690 V

To oil separator

From liquid

separator

evaporator

From liquid

separator

evaporator

From liquid

separator

evaporator

PLC/OEM

controller

Not all valves are shown.

Not to be used for construction

purposes.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

10 DKRCI.PA.000.C4.02 / 520H1623 © Danfoss A/S (AC-SMC/MWA), 2013-02

2.2

Discharge Temperature

Control with Liquid Injection

Compressor manufacturers generally

recommend limiting the discharge temperature

below a certain value to prevent overheating of

values, prolonging their life and preventing the

breakdown of oil at high temperatures.

From the log p-h diagram, it can be seen that the

discharge temperature may be high when:

the compressor runs with high pressure

dierential.

the compressor receives highly superheated

suction vapour.

the compressor runs with capacity control by

hot gas bypass.

There are several ways to reduce the discharge

temperature. One way is to install water cooled

heads in reciprocating compressors, another

method is liquid injection, by which liquid

refrigerant from the outlet of the condenser

or receiver is injected into the suction line, the

intermediate cooler, or the side port of the screw

compressor.

Application example 2.2.1:

Liquid injection with

thermostatic injection valve

À

Stop valve

Á Solenoid valve

Â Thermostatic injection valve

Ã Stop valve

Ä Thermostat

HP vapour refrigerant

HP liquid refrigerant

LP vapour refrigerant

LP liquid refrigerant

Oil

Danfoss

Tapp_0018

10-2012

When the discharge temperature rises above

the set value of the thermostat RT 107 Ä, RT 107

will energise the solenoid valve EVRA Á which

will start liquid injection into the side port of the

screw compressor.

The thermostatic injection valve TEAT Â

controls the injected liquid ow according to

the discharge temperature, which prevents the

discharge temperature from rising further.

Technical data

Thermostat - RT

Refrigerants R717 and uorinated refrigerants

Enclosure IP 66/54

Max. bulb temp. [°C] 65 to 300

Ambient temp. [°C] –50 to 70

Regulating range [°C] –60 to 150

Dierential Δt [°C] 1.0 to 25.0

Thermostatic injection valve - TEAT

Refrigerants R717 and uorinated refrigerants

Regulating range [°C] Max. bulb temp.: 150°C

P band: 20°C

Max. working pressure [bar] 20

Rated Capacity* [kW] 3.3 to 274

* Conditions: T

e

= +5°C, p = 8 bar, T

sub

= 4°C

Compressor

To oil

separator

From

receiver

Oil injection

From liquid

separator

evaporator

Not all valves are shown.

Not to be used for construction

purposes.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

Application example 2.2.2:

Liquid injection with motor

valve

À

Stop valve

Á Solenoid valve

Â Motor valve

Ã Stop valve

Ä Controller

Å Temperature sensor

HP vapour refrigerant

HP liquid refrigerant

LP vapour refrigerant

LP liquid refrigerant

Oil

An electronic solution for liquid injection control

can be achieved with the motorised valve

ICM Â. An AKS 21 PT 1000 temperature sensor Å

will register the discharge temperature and

transmit the signal to the temperature controller

EKC 361 Ä. The EKC 361 controls the ICAD actuator

which adjusts to opening degree of the ICM motor

valve in order to limit and maintain the required

discharge temperature.

Technical data

Danfoss

Tapp_0019

10-2012

ICM for expansion

Material Body: Low temperature steel

Refrigerants All common refrigerants including R717 and R744

Media temp. range [°C] –60 to 120

Max. working pressure [bar] 52 bar

DN [mm] 20 to 80

Nominal Capacity* [kW] 72 to 22,700

* Conditions: T

e

= –10°C, p = 8.0 bar, T

sub

= 4K

Actuator - ICAD

Media temp. range [°C] –30 to 50 (ambient)

Control input signal 0/4-10mA, or 0/2-10

Open-close time with

maximum selected speed

3 to 45 seconds depending on valve size

From liquid

separator

evaporator

Oil injection

From

receiver

To oil

separator

Compressor

Not all valves are shown.

Not to be used for construction

purposes.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

12 DKRCI.PA.000.C4.02 / 520H1623 © Danfoss A/S (AC-SMC/MWA), 2013-02

Application example 2.2.3:

A compact solution for liquid

injection with ICF

À

Valve station with:

Stop valve

Filter

Solenoid valve

Manual opener

Motor valve

Stop valve

Á Controller

Â Temperature sensor

HP vapour refrigerant

HP liquid refrigerant

LP vapour refrigerant

LP liquid refrigerant

Oil

For liquid injection, Danfoss can supply a very

compact control solution ICF À. Up to six

dierent modules can be assembled into the

same housing. This solution works in the same

way as example 2.2.2, and is very compact and

easy to install.

Technical data

Danfoss

Tapp_0020

10-2012

ICF control solution

Material Body: Low temperature steel

Refrigerants All common refrigerants including R717 and R744

Media temp. range [°C] –60 to 120

Max. working pressure [bar] 52 bar

DN [mm] 20 to 40

M

From liquid

separator

evaporator

Oil injection

From

receiver

To oil

separator

Compressor

Not all valves are shown.

Not to be used for construction

purposes.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

2.3

Crankcase Pressure Control

During start-up or after defrost, the suction

pressure has to be controled, otherwise it can

be too high, and the compressor motor will be

overloaded.

The electric motor for the compressor may be

damaged by this overloading.

There are two ways to overcome this problem:

1. Start the compressor at part load. The

capacity control methods can be used to

start compressor at part load, e.g. unload

part of the pistons for multi-piston

reciprocating compressors, or bypass some

suction gas for screw compressors with slide

valves, etc.

2. Control the crankcase pressure for

reciprocating compressors. By installing a

back pressure controlled regulating valve in

the suction line, which will not open until

the pressure in the suction line drops below

the set value, suction pressure can be kept

under a certain level.

Application example 2.3.1:

Crankcase pressure control with

ICS and CVC

À

Crankcase pressure regulator

Á Stop valve

HP vapour refrigerant

LP vapour refrigerant

Oil

In order to control the crankcase pressure during

start-up, after defrost, or in others cases when

the suction pressure may run too high, the

pilot-operated servo valve ICS À with the back

pressure controlled pilot valve CVC is installed

in the suction line. The ICS will not open until

the downstream suction pressure falls below

the set value of the pilot valve CVC. In this way,

the high pressure vapour in the suction line

can be released into the crankcase gradually,

which ensures a manageable capacity for the

compressor.

Technical data

Danfoss

Tapp_0021

10-2012

Pilot-operated servo valve - ICS

Material Body: low temp. steel

Refrigerants All common refrigerants, incl. R717 and R744

Media temp. range [°C] –60 to +120

Max. working pressure [bar] 52

DN [mm] 20 to 150

Capacity* [kW] 11 to 2440

* Conditions: T

e

= –10°C, T

l

= 30°C, p = 0.2 bar, T

sub

= 8K

Pilot valve - CVC (LP)

Refrigerants All common refrigerants

Media temp. range [°C] –50 to 120

Max. working pressure [bar] High pressure side: 28

Low pressure side: 17

Pressure range [bar] –0.45 to 7

K

v

value [m

3

/h] 0.2

Pilot valve - CVC (XP)

Refrigerants All common refrigerants

Media temp. range [°C] –50 to 120

Max. working pressure [bar] High pressure side: 52

Low pressure side: 28

Pressure range [bar] 4-28

K

v

value [m

3

/h] 0.2

Compressor

Oil

separator

To condenser

From

evaporator

Not all valves are shown.

Not to be used for construction

purposes.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

14 DKRCI.PA.000.C4.02 / 520H1623 © Danfoss A/S (AC-SMC/MWA), 2013-02

2.4

Reverse Flow Control

Reverse ow and condensation of refrigerant

from the condenser to the oil separator and

the compressor should be avoided at all time.

For piston compressors, reverse ow can result

in liquid hammering. For screw compressors,

reverse ow can cause reversed rotation

and damage to the compressor bearings.

Furthermore, migration of refrigeration into the

oil separator and further into the compressor at

standstill should be avoided. To avoid this reverse

ow, it is necessary to install a check valve on the

outlet of the oil separator.

Application example 2.4.1:

Reverse ow control

À

Stop check valve

HP vapour refrigerant

LP vapour refrigerant

Oil

The stop check valve SCA À can function as a

check valve when the system is running, and

can also shut o the discharge line for service

as a stop valve. This combined stop/check valve

solution is easier to install and has lower ow

resistance compared to a normal stop valve plus

check valve installation.

When selecting a stop check valve, it is important

to note:

1. Select a valve according to the capacity and

not the pipe size.

2. Consider both the nominal and part load

working conditions. The velocity in the

nominal condition should be near to the

recommended value, at the same time

the velocity in the part load condition should

be higher than the minimum recommended

velocity.

For details on how to select valves, please refer to

the product catalogue.

Technical data

Danfoss

Tapp_0023_02

10-2012

Stop check valve - SCA

Material Housing: special cold resistant steel approved for low temperature operation.

Spindle: polished stainless steel

Refrigerants All common non-ammable refrigerants, incl. R717.

Media temp. range [°C] –60 to 150

Opening dierential pressure [bar] 0.04 (0.3 bar spring availble as spare part)

Max. working pressure [bar] 40

DN [mm] 15 to 125

Not all valves are shown.

Not to be used for construction

purposes.

Compressor

To condenser

From

evaporator

Oil

separator

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

Solution Application Benets Limitations

Compressor Capacity Control

Step control of compressor

capacity with EKC 331 and

AKS 32/33

Applicable to multi-

cylinder compressor, screw

compressor with multiple

suction ports, and systems

with several compressors

running in parallel.

Simple.

Almost as ecient at part

load as at full load.

The control is not

continuous, especially when

there are only few steps.

Fluctuations in the suction

pressure.

Compressor capacity control

with hot gas bypass using

ICS and CVC

Applicable to compressors

with xed capacities.

Eective to control the

capacity continuously

according to the actual

heat load.The hot gas can

help the oil return from the

evaporator.

Not ecient at part load.

Energy consuming.

Compressor variable speed

capacity control

Applicable to all

compressors with the ability

to run at reduced speed.

Low start up current

Energy savings

Lower noise

Longer lifetime

Simplied installation

Compressor must be suited

for reduced speed operation.

Discharge Temperature Control with Liquid Injection

Mechanical solution for

liquid injection with TEAT,

EVRA(T) and RT

Applicable to systems where

the discharge temperatures

may run too high.

Simple and eective. Injection of liquid refrigerant

may be dangerous to the

compressor. Not as ecient

as intermediate cooler.

Electronic solution for liquid

injection control with EKC

361 and ICM

Applicable to systems where

the discharge temperatures

may run too high.

Flexible and compact.

Possible to monitor and

control remotely.

Not applicable to ammable

refrigerants. Injection of

liquid refrigerant may

be dangerous to the

compressor. Not as ecient

as intermediate cooler.

Electronic solution for liquid

injection control with EKC

361 and ICF

Crankcase Pressure Control

Crankcase pressure control

with ICS and CVC

Applicable to reciprocating

compressors, normally

used for small and medium

systems.

Simple and reliable. Eective

in protecting reciprocating

compressors at start-up or

after hot gas defrost.

Gives constant pressure

drop in the suction line.

Crankcase pressure control

with ICS and CVP

Reverse Flow Control

Reverse ow control with

SCA

Applicable to all

refrigeration plants.

Simple.

Easy to install.

Low ow resistance.

Gives constant pressure

drop in the discharge line.

2.5

Summary

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

2.6

Reference Documents

For an alphabetical overview of

all reference documents please

go to page 149

To download the latest version of the literature please visit the Danfoss internet site

http://www.danfoss.com/Products/Literature/RA_Documentation.htm

Type Literature no.

AKD 102 PD.R1.B

AKS 21 RK.0Y.G

AKS 32R RD.5G.J

AKS 33 RD.5G.H

CVC PD.HN0.A

CVP PD.HN0.A

EKC 331 RS.8A.G

EKC 361 RS.8A.E

EVRA(T) PD.BM0.B

Type Literature no.

ICF PD.FT0.A

ICM PD.HT0.B

ICS PD.HS0.A

REG PD.KM1.A

SCA PD.FL1.A

SVA PD.KD1.A

TEAT RD.1F.A

Technical Leaet / Manual

Type Literature no.

AKD 102 MG.11.L

AKS 21 RI.14.D

AKS 32R PI.SB0.A

AKS 33 PI.SB0.A

CVC RI.4X.L

CVP PI.HN0.C

EKC 331 RI.8B.E

EKC 361 RI.8B.F

EVRA(T) RI.3D.A

Type Literature no.

ICF PI.FT0.A

ICM 20-65 PI.HT0.A

ICM 100-150 PI.HT0.B

ICS 25-65 PI.HS0.A

ICS 100-150 PI.HS0.B

REG PI.KM1.A

SCA PI.FL1.A

SVA PI.KD1.A

TEAT PI.AU0.A

Product instruction

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

3. Condenser Controls

In areas where there are large variations in

ambient air temperatures and/or load conditions,

it is necessary to control the condensing

pressure to avoid it from falling too low. Too

low condensing pressures results in there being

insucient pressure dierential across the

expansion device and the evaporator is supplied

with insucient refrigerant. It means that

condenser capacity control is mainly used in the

temperate climate zones and to a lesser degree in

subtropical and tropical zones.

The basic idea of control is to control the

condenser capacity when the ambient

temperature is low, so that the condensing

pressure is maintained above the minimum

acceptable level.

This condensing capacity control is achieved

either by regulating the ow of circulating air or

water through the condenser, or by reducing the

eective heat exchange surface area.

Dierent solutions can be designed for dierent

types of condensers:

3.1 Air cooled condensers

3.2 Evaporative condensers

3.3 Water cooled condensers

3.1

Air Cooled Condensers

An air-cooled condenser consists of tubes mounted

within a n block. The condenser can be horizontal,

vertical or V-shaped. The ambient air is drawn across

the heat exchanger surface with axial or centrifugal

fans.

Air-cooled condensers are used on industrial

refrigeration systems where the relative air humidity

is high. Controlling the condensing pressure for air-

cooled condensers can be achieved in the following

ways:

3.1.1 - Step Control of Air Cooled Condensers

The rst method was using the required number

of pressure controls in the form the Danfoss RT-5

and adjusting them to dierent set cut-in and

cut-out pressures.

The second method of controlling the fans was

by using a neutral zone pressure controller in the

form of the Danfoss type RT-L. Initially it was used

together with a step controller with the required

number of contacts for the number of fans.

3.1.2 - Fan speed control of air cooled condensers

This method of condenser fan control is mainly

used whenever a reduction in noise level is

desired due to environmental concerns.

For this type of installation Danfoss frequency

converter AKD can be used.

3.1.3 - Area control of air cooled condensers

For area or capacity control of air cooled

condensers a receiver is required. This receiver

must have sucient volume to be able to

accommodate the variations in the amount of

refrigerant in the condenser.

Two ways this condenser area control can be

done:

1. Main valve ICS or PM combined with the

constant pressure pilot CVP(HP) mounted in

the hot gas line on the inlet side to the

condenser and ICV combined with a

dierential pressure pilot CVPP(HP) mounted

in the pipe between the hot gas line and the

receiver. In the pipe between the condenser

and the receiver a check valve NRVA is

mounted to prevent liquid migration from the

receiver to the condenser.

However this system reacted too fast and timers

were used for delaying the cut-in and cut-out of

the fans.

The Third method is today’s step controller the

Danfoss EKC-331.

2. Main valve ICS combined with the constant

pressure pilot CVP(HP) mounted in the pipe

between the condenser and the receiver and

a ICS combined with a dierential pressure

pilot CVPP(HP) mounted in the pipe between

the hot gas line and the receiver. This method

is mainly used in commercial refrigeration.

Application Handbook Industrial Refrigeration ammonia and CO

2

applications

Application example 3.1.1:

Step control of fans with step

controller EKC 331

À Step controller

Á Pressure transmitter

Â Stop valve

Ã Stop valve

Ä Stop valve

HP vapour refrigerant

HP liquid refrigerant

EKC 331 À is a four-step controller with up to

four relay outputs. It controls the switching of the

fans according to the condensing pressure signal

from a pressure transmitter AKS 33 Á or AKS 32R.

Based on neutral zone control, EKC 331 À

can control the condensing capacity so that the

condensing pressure is maintained above the

required minimum level.

For more information on neutral zone control,

please refer to section 2.1.

The bypass pipe where SVA Ä is installed is

an equalizing pipe, which helps balance the

pressure in the receiver with the inlet pressure of

the condenser so that the liquid refrigerant in the

condenser can be drained into the receiver.

In some installations, EKC 331T is used. In this

case the input signal could be from a PT 1000

temperature sensor, e.g. AKS 21. The temperature

sensor is usually installed in the outlet of the

condenser.

Note! The EKC 331T + PT1000 temperature

sensor solution is not as accurate as the EKC

331 + pressure transmitter solution because

the condenser outlet temperature may not

entirely reect the actual condensing pressure

due to the liquid subcooling or the presence of

incondensable gasses in the refrigeration system.

If the subcooling is too low, ash gas may occur

when the fans start.

Technical data

Danfoss

Tapp_0031_02

10-2012

Pressure transmitter-AKS 33 Pressure transmitter-AKS 32R

Refrigerants All refrigerants including R717 All refrigerants including R717

Operating range [bar] –1 to 34 –1 to 34

Max. working pressure PB [bar] 55 (depending on operating range) 60 (depending on operating range)

Operating temp. range [°C] –40 to 85

Compensated temp. range [°C] LP: –30 to +40 / HP: 0 to +80

Rated output signal 4 to 20 mA 10 to 90% of V supply

Pressure transmitter - AKS 3000 Pressure transmitter - AKS 32

Refrigerants All refrigerants including R717 All refrigerants including R717

Operating range [bar] 0 to 60 (depending on range) –1 to 39 (depending on range)

Max. working pressure PB [bar] 100 (depending on operating range) 60 (depending on operating range)

Operating temp. range [°C] –40 to 80 –40 to 85

Compensated temp. range [°C] LP: –30 to +40 / HP: 0 to +80 LP: –30 to +40 / HP: 0 to +80

Rated output signal 4 to 20 mA 1 to 5V or 0 to 10V

Not all valves are shown.

Not to be used for construction

purposes.

From

discharge line

To expansion

device

Condenser

La page charge ...

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