Cibse Variable Flow Dpcv Cpd

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1 Andy Lucas Technical Development Manager CRANE BS&U CRANE BS&U supporting the Building Services Industry

Transcript of Cibse Variable Flow Dpcv Cpd

Page 1: Cibse Variable Flow Dpcv Cpd

1Andy LucasTechnical Development Manager CRANE BS&U

CRANE BS&U supporting the Building Services

Industry

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Crane Co founded in 1855 by Richard Teller Crane who made the following resolution -

“I am resolved to conduct my business in the strictest honesty and fairness; to avoid all deception and trickery; to deal fairly with both customers and competitors; to be liberal and just towards employees; and to put my whole mind upon the business”

Crane Limited founded in Ipswich in 1919

Crane Building Services & Utilities created 2009

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Building Services

Water UtilitiesGas Utilities

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CRANE BS&U 2010 sales £110m

Water Utilities

Gas Utilities Building Services

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industry organisations

• CIBSE

• SoHPE

• BSRIA

• CSA

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6Andy LucasTechnical Development Manager CRANE BS&U

VARIABLE FLOW SYSTEMSincorporating

DPCVs

CIBSE approved CPD

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VARIABLE FLOW SYSTEMS

To give an overview of Variable FlowSystem design and commissioning using Differential Pressure Control Valves

Title

Objective

this applies to both heating and chilled water systems

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Drivers of Change

• driven by Government legislation

• energy conservation

• subsequent CO emissions 2

The move from constant to variable flow design can give up to 80% pump energy savings; about 6 - 8% total energy saving

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• fixed speed pumps – no energy saving for part load

• constant volume of water is pumped around the system

• 3 or 4 port control valve diverts water through by-pass

• commissioned by proportional balancing or by the use of constant flow regulators – ABV (Automatic Balancing Valves)

Constant volume flow systems

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constant amount of water pumped around a system controlled by 3 or 4 port control valves and would be

Constant flow

• through terminal

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constant amount of water pumped around a system controlled by 3 or 4 port control valves and would be

Constant flow

• through terminal• split between terminal and

by-pass

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constant amount of water pumped around a system controlled by 3 or 4 port control valves and would be

Constant flow

• through terminal• split between terminal and

by-pass• diverted back if not required

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• variable speed pumps – energy saving for part load

• variable volume of water to match demand

• diversity factor

• 2 port control valve

• commissioned by combination of;

proportional balancing

DPCV – Differential Pressure Control Valves

Variable volume flow systems

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Variable flow

open

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Variable flow

open modulating between open and closed

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Variable flow

open modulating between open and closed

closed

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Pump energy saving

Pre

ssur

e

P (K

Pa)

Maximum load operating point

as system demand change, flow rate is changed by varying speed of pump

direct relationship between pump speed and flow rate:

50% pump speed = 50% flow rate

50% flow rate = over 85% energy saving

minimum flow rate approx 20%

Flow Rate Q (kg/s)100%20%

100%

4%

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DPCVs to protect 2 port control valves

DPCV holds pressure constant between points A and B

A

B

to enable modulating 2 port control valves to operate with an acceptable authority, a DPCV is installed to limit the pressure differential against which the 2 port valves have to close. The installation of DPCVs on sub-branches with 2 port control valves is therefore essential to achieve good control, as well as to avoid noise or cavitation.

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Installation of 2 port control valvesdue to fluctuating system pressures created by the 2 port control valves opening & closing, consideration needs to be given to valve authority.

valve authority is;

• is ability of the control valve to control flow

• is calculated by dividing the pressure drop across the 2 port at design flow by the pressure drop at no flow

• should not be below 0.3

• higher authority gives better flow control

the installation of Differential Pressure Control Valves (DPCV) protects the 2 ports from the fluctuating/rising pressures

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Installation of 2 port control valvesexample without DPCV

80kPa

20kPa

at design flow rate

valve authority ß = Δp across 2 portΔp across circuit

ß =20 kPa80 kPa

ß = 0.25

too low - unacceptable

always given as a decimal

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Installation of 2 port control valvesexample with DPCV fitted

80kPa

20kPa

at design flow rate

valve authority ß = Δp across 2 portΔp across circuit

ß =20 kPa40 kPa

ß = 0.5

acceptable

40kPa

controlled by DPCV

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Installation of 2 port control valvesposition of DPCV?

at design flow rate

valve authority ß = Δp across 2 portΔp across circuit

ß =20 kPa25 kPa

ß = 0.8

80kPa

25kPa 20kPa

position can influence authority

on single terminal circuits – as closes as possible to control valves gives higher authority

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Installation of 2 port control valves

Valve characteristic

Per

cent

age

flow

rate Coil

characteristic

Percentage open

for good modulating control the control valve needs to achieve equal percentage characteristic i.e. a characteristic that mirrors the characteristic of the coil.

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% open

Installation of 2 port control valves

% h

eat o

utpu

t

equal percentage control valves will only operate with near to an equal percentage characteristic where authority, β, is greater than 0.3

50% output

20% flow

with β = 1

mirror image of coil characteristic

50% valve opening = 50% heat output

flow rate reduces to 20%

output increases

Coil output characteristic

β = 1

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% open

Installation of 2 port control valves

% h

eat o

utpu

t

equal percentage control valves will only operate with near to an equal percentage characteristic where authority, β, is greater than 0.3

with β = 1

mirror image of coil characteristic

authority is reduced as pressure drop increases

Coil output characteristic

β = 1

β = 0.5

β = 0.3

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% open

Installation of 2 port control valves

% h

eat o

utpu

t

equal percentage control valves will only operate with near to an equal percentage characteristic where authority, β, is greater than 0.3

50% outputwith β = 1

mirror image of coil characteristic

effect of reduction in β to 0.3

output increases

Coil output characteristic

β = 0.3

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2 Port

DPCV – operating principle

Upper chamberLower chamber

rising pressure closes DPCV

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for any flow rate there is only one possible pressure drop between any 2 points

the DPCV identifies the 2 points by the connecting impulse tube

setting the DPCV to control Δp (pressure drop) between A & B at 100% DFR controls flow rate between these 2 points

A

B

DPCV – operating principle

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System layout – position of DPCV

Branches are broken down into sub-circuits, each controlled by a DPCV

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System layout – position of DPCV

Branches are broken down into sub-circuits, each controlled by a DPCV

Note: each circuit must only flow through a single DPCV

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Commissioning features around DPCVs

a ‘Companion Valve’ (FODRV) should be installed so that the DPCV can be adjusted until the required design flow rate is achieved.

if required, pressure test points could be installed so that the pressure controlled by the DPCV can be measured and recorded.

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P

test points to check sensor by-pass with isolating valve

should be included to allow the differential pressure to be checked and zeroed

to control pump speed, differential pressure sensor should be located across the most remote DPCV controlled sub-branch with additional sensors on branches that might become the index circuit under part load conditions.

Differential pressure sensors

sensor

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P

to control pump speed, the differential pressure sensor sends signal to BMS which varies pump speed

Differential pressure sensors

BMS

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at maximum pump turndown, typically 10 - 20%, consideration needs to be given to branches to ensure

pump flow at minimum load

circulation of water treatment

ready supply of heating/chilled water

Minimum flow

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end terminal could have a 3 or 4 port control valve

on larger circuits additional 3 or 4 ports could be added

possible solution

Minimum flow

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a constant flow regulator (ABV) could be used

possible solution

Minimum flow

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a pressure relief valve could be installed

possible solution

Minimum flow

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a RADPCV (Reverse Acting DPCV) could be used

possible solution

Minimum flow

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Commissioning Variable Flow Systems

because each sub-circuit is separated by a DPCV from fluctuating system pressure & therefore holds a constant pressure within the sub-circuit, commissioning sub-circuits can be carried out totally independently

sub-circuits are independent of each other

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Commissioning Variable Flow Systems

commissioning within the sub-circuits is carried out by ‘proportional balancing’ in the conventional manner

reference

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Commissioning Variable Flow Systems

each sub-circuit is balanced by measuring flow thro the ‘Companion Valve’ and adjusting DPCV to regulate flow

commissioning valve normally fully open

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Commissioning Variable Flow Systems

for circuits nearer the pump the regulating function of the commissioning valve may be used to reduce the pressure drop across the DPCV to bring it into a better operating position, ie splits residual pressure

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To summarise • change in system design to variable flow controlled by 2 port

control valve resulting in pump energy saving

• fluctuation in system pressure undermines control valve authority

• DPCV installed into sub-circuits to ‘protect’ control valves from fluctuating pressure to maintain control valve authority

• provision for pump turndown, typically 10 – 20%

• terminal units commissioned by conventional proportional method

• branches commissioned by use of ‘Companion’ Valve & DPCV

• branches commissioned independently of each other

• pressure sensors used to set pump speed

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Written byAndy Lucas

Technical Development Manager CRANE BS&U

VARIABLE FLOW SYSTEMSincorporating

DPCVs