STAP. Differential pressure controller DN 15-50

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Differential pressure controller 15-50 Pressurisation & Water Quality Balancing & Control Thermostatic Control ENGINEERING ADVANTAGE is a high-performing differential pressure controller that keeps the differential pressure over the load constant. This delivers accurate and stable modulating control, ensures less risk of noise from control valves, and results in easy balancing and commissioning. s unrivalled accuracy and compact size make it particularly suitable for use on the secondary side of heating and cooling systems.

DIFFERENTIAL PRESSURE CONTROLLERS - Pressure relief cone Ensures accurate differential pressure control. Adjustable set-point and shut-off function Delivers desired differential pressure ensuring accurate balancing. Shut-off function makes maintenance easy and straightforward. Measuring points with drain option Simplifies the balancing procedure, and increases its accuracy. Technical description Application: Heating and cooling systems. Functions: Differential pressure control Adjustable Δp Measuring point Shut-off Draining (accessory) Dimensions: 15-50 Pressure class: PN 16 Max. differential pressure (ΔpV): 250 kpa Setting range: 15-20: 5* - 25 kpa 32-40: 10* - 40 kpa 15-25: 10* - 60 kpa 32-50: 20* - 80 kpa *) Delivery setting Temperature: Max. working temperature: 120 C Min. working temperature: -20 C Material: Valve body: AMETAL Bonnet: AMETAL Cone: AMETAL Spindles: AMETAL O-rings: EPDM rubber Membrane: HNBR rubber Spring: Stainless steel Handwheel: Polyamide Smooth ends: Nipple: AMETAL Sealing ( 25-50): EPDM O-ring AMETAL is the dezincification resistant alloy of TA. Marking: Body: TA, PN 16/150,, inch size and flow direction arrow. Bonnet:, Δp L 5-25, 10-40, 10-60 or 20-80. 2

DIFFERENTIAL PRESSURE CONTROLLERS - Operating instruction 1. Setting Δp L (allen key) 2. Shut-off 3. Connection capillary pipe Venting Connection measuring point 4. Measuring point 5. Connection draining kit (accessory) Measuring point Remove the cover and then insert the probe through the selfsealing nipple. Measuring point (accessory) can be connected to the venting if the STAD valve is out of reach for measuring of differential pressure. Drain Draining kit available as accessory. Can be connected during operation. Installation Note! The must be placed in the return pipe and with correct flow direction. To simplify installations in tight spaces, the bonnet can be detached. When extending the capillary pipe, use e.g. 6 mm copper pipe and extension kit (accessory). Note! The supplied capillary pipe must be included. Balancing of system with presettable valves. (Suitable for Application examples 1, 3, 4 and 5) Balancing of system with non presettable valves. (Suitable for Application example 2) STAD 1 1 ΔH Δp L 2 2 1. Inlet 2. Return For further installation examples, see Handbook No 4 - Hydronic balancing with differential pressure controllers. STAD see catalogue leaflet STAD. 3

DIFFERENTIAL PRESSURE CONTROLLERS - Diagram The diagram shows the lowest pressure drop required for the valve to be within its working range at different flows. q [l/s] 0,00 0,28 0,56 0,83 1,11 50 15 20 25 45 40 35 ΔpV min [kpa] 30 25 20 15 10 5 0 0 1000 2000 3000 4000 q [l/s] [l/s] 0,00 0,56 1,11 1,67 2,22 2,78 3,33 3,89 4,44 5,00 5,56 6,11 80 32 40 50 75 70 65 60 55 2 50 Δpv [kpa] Δp v [kpa] 45 40 35 30 25 2 20 15 10 2 5 0 0 2000 4000 6000 8000 10000 12000 14000 16000 18000 20000 22000 1 4

DIFFERENTIAL PRESSURE CONTROLLERS - Example: Desired flow 6000 l/h, Δp L = 23 kpa and available differential pressure ΔH = 60 kpa. 1. Desired flow (q) 6000 l/h. 2. Read the pressure drop ΔpV min 32 ΔpV min = 50 kpa 40 ΔpV min = 22 kpa 50 ΔpV min = 6 kpa 3. Calculate required available differential pressure ΔH min. At 6000 l/h and fully open STAD the pressure drop is, 32 = 18 kpa, 40 = 10 kpa and 50 = 3 kpa. ΔH min = Δp STAD + Δp L + ΔpV 32: ΔH min = 18 + 23 + 50 = 91 kpa 40: ΔH min = 10 + 23 + 22 = 55 kpa 50: ΔH min = 3 + 23 + 6 = 32 kpa 4. In order to optimise the control function of the select the smallest possible valve, in this case 40. ( 32 is not suitable since ΔH min = 91 kpa and available differential pressure 60 kpa only). Δp STAD ΔH Δp L ΔpV ΔH = Δp STAD + Δp L + ΔpV TA recommends the software TA Select for calculating the size. TA Select can be downloaded from www.tahydronics.com 5

DIFFERENTIAL PRESSURE CONTROLLERS - Working range Kv min Kv nom Kv m 15 0,07 1,0 1,4 20 0,16 2,2 3,1 25 0,28 3,8 5,5 32 0,42 6,0 8,5 40 0,64 9,0 12,8 50 1,2 17,0 24,4 Note! The flow in the circuit is determined by its resistance, i.e. Kv C : q c = Kv c Δp L Δp L A B C Δp nom D A. Kv min B. Kv nom (Delivery setting) C. Kv m D. Working range Δp L ±20%. 5-25 and 10-40 kpa ±25%. q q min q nom q max Sizing 1. Select the desired Δp L in the tables. 2. Select the same size of the valve as the pipe. 3. Check that the desired flow is smaller than the specified q max. If not, select the nearest bigger dimension, alternatively a bigger Δp L. 6

DIFFERENTIAL PRESSURE CONTROLLERS - The tables are valid for: ΔH 2 x Δp L, but the valve works properly between ΔH ~1,5 x Δp L to 250 kpa + Δp L. 5-25 kpa Δp L [kpa] 5 10 15 20 25 q min q nom q max q min q nom q max q min q nom q max q min q nom q max q min q nom q max 15 15 220 310 20 320 440 25 390 540 30 450 630 35 500 700 20 35 490 690 50 700 980 60 850 1200 70 980 1390 80 1100 1550 10-40 kpa Δp L [kpa] 10 20 30 40 q min q nom q max q min q nom q max q min q nom q max q min q nom q max 32 130 1900 2690 190 2680 3800 230 3290 4660 270 3790 5380 40 200 2850 4050 290 4020 5720 350 4930 7010 400 5690 8100 10-60 kpa Δp L [kpa] 10 20 30 q min q nom q max q min q nom q max q min q nom q max 15 20 320 440 30 450 630 40 550 770 20 50 700 980 70 980 1390 90 1200 1700 25 90 1200 1740 130 1700 2460 150 2080 3010 Δp L [kpa] 40 50 60 q min q nom q max q min q nom q max q min q nom q max 15 45 600 900 50 710 990 55 770 1080 20 100 1400 2000 110 1560 2190 120 1700 2400 25 180 2400 3500 200 2690 3890 220 2940 4260 20-80 kpa Δp L [kpa] 20 30 40 50 q min q nom q max q min q nom q max q min q nom q max q min q nom q max 32 190 2680 3800 230 3290 4660 270 3790 5380 300 4240 6010 40 290 4020 5720 350 4930 7010 400 5690 8100 450 6360 9050 50 540 7600 10900 660 9310 13400 760 10800 15400 850 12000 17300 Δp L [kpa] 60 70 80 q min q nom q max q min q nom q max q min q nom q max 32 330 4650 6580 350 5020 7110 380 5370 7600 40 500 6970 9910 540 7530 10700 570 8050 11400 50 930 13200 18900 1000 14200 20400 1070 15200 21800 7

DIFFERENTIAL PRESSURE CONTROLLERS - Application examples 1. Stabilising the differential pressure across a circuit with presettable radiator valves In plants equipped with presettable radiator valves (TRV), it is easy to get a good result. The presetting of the radiator valves limit the flow so that overflows do not occur. limits the differential pressure and prevents noise. stabilises Δp L. The preset Kv-value of TRV limits the flow in each radiator. STAD is used for flow measuring, shut-off and connection of the capillary pipe. TRV TRIM STAD ΔH 2. Stabilising the differential pressure across a circuit with non-presettable radiator valves In plants equipped with non-presettable radiator valves it is not so easy to get an optimal result. Such radiator valves are common in older plants and will not limit the flow, which can be significantly too high in one or several circuits. Consequently, it is not enough that limits the differential pressure across each circuit. Letting work together with STAD will solve the problem. STAD limits the flow to design value (using TA s balancing instrument to find the correct value). The correct distribution of the total flow between the radiators is however not achieved, but this solution can significantly improve a plant equipped with non-presettable radiator valves. stabilises Δp L. There is no presettable Kv-value on the radiator valve in order to limit the flow in each radiator. STAD limits the total flow in the circuit. STAD ΔH 8

DIFFERENTIAL PRESSURE CONTROLLERS - 3. Stabilising the differential pressure across a circuit with control and balancing valves When several small terminal units are close to one another, the differential pressure can be stabilised by using in combination with STAD-1 across each circuit. STAD-2 for each terminal unit limits the flow and STAD-1 is used to measure the flow. stabilises Δp L. The set Kv-value in STAD-2 limits the flow in each terminal unit. STAD-1 is used for flow measuring, shut-off and connection of the capillary pipe. STAD-1 STAD-2 ΔH 4. Stabilising the differential pressure across a riser with balancing valves ( Modular valve method ) The Modular valve method is suitable when a plant is put into operation phase. Install one differential pressure controller on every riser, so that each controls one module. keeps the differential pressure from the main pipe at a stable value out to the risers and circuits. STAD-2 downstream on the circuits guarantees that overflows do not occur. With working as a modular valve, the whole plant does not need to be re-balanced when a new module is taken into operation. There is no need for balancing valves on the main pipes (except for diagnostic purposes), since the modular valves distribute the pressure out to the risers. reduces a big and variable ΔH to a suitable and stable Δp L. The set Kv-value in STAD-2 limits the flow in each circuit. STAD-1 is used for flow measuring, shut-off and connection of the capillary pipe. TRV TRIM STAD-2 STAD-1 ΔH 9

DIFFERENTIAL PRESSURE CONTROLLERS - 5. Keeping the differential pressure across a control valve constant Depending of the design of the plant, the available differential pressure across some circuits can vary significantly with the load. To keep the correct control valve characteristic in such a case, the differential pressure across the control valves can be kept almost constant by a connected directly across each control valve. The control valve will not be over-sized and the authority is and will remain close to 1. If all control valves are combined with, there is no need for other balancing valves, except for diagnostic purposes. keeps Δp across the control valve constant, giving a valve authority ~ 1. The Kvs of the control valve and the chosen Δp gives the design flow. STAD-1 is used for flow measuring, shut-off and connection of the capillary pipe. STAD-1 STAD-1 STAD STAD-1 ΔH STAD Sizing the control valve A control valve should give a flow of 1000 l/h at a ΔH varying between 55 and 160 kpa. With a differential pressure of 10 kpa over the control valve, the Kvs will be 3,16. Control valves are normally available with Kvs-values according to the series 0,25 0,4 0,63 1,0 1,6 2,5 4,0 6,3. Choose Kvs=2,5, which will give a Δp of 16 kpa. Since the guarantees a high control valve authority, a low pressure drop over the control can be chosen. Therefore, choose the biggest Kvs value that gives a Δp above the minimum set point of (i.e. 5, 10 or 20 kpa depending on size and type). Adjust to give Δp L = 16 kpa. Check the flow with TA s balancing instrument over STAD-1 and with the control valve fully open. 10

DIFFERENTIAL PRESSURE CONTROLLERS - Articles Female threads 1 m capillary pipe and transition nipples G1/2 and G3/4 are included. L D Article No EAN D L H B Kv m Kg G1/16 B H 5-25 kpa 52 265-115* 7318793946607 15 G1/2 84 137 72 1,4 1,1 52 265-120* 7318793946706 20 G3/4 91 139 72 3,1 1,2 10-40 kpa 52 265-132 7318793790002 32 G1 1/4 133 179 110 8,5 2,6 52 265-140 7318793790101 40 G1 1/2 135 181 110 12,8 2,9 10-60 kpa 52 265-015* 7318793623201 15 G1/2 84 137 72 1,4 1,1 52 265-020* 7318793623300 20 G3/4 91 139 72 3,1 1,2 52 265-025 7318793623409 25 G1 93 141 72 5,5 1,3 52 266-315 7318793958501 15 Rc1/2 84 137 72 1,4 1,1 52 266-320 7318793958600 20 Rc3/4 91 139 72 3,1 1,2 52 266-325 7318793958709 25 Rc1 93 141 72 5,5 1,3 20-80 kpa 52 265-032 7318793623805 32 G1 1/4 133 179 110 8,5 2,6 52 265-040 7318793623904 40 G1 1/2 135 181 110 12,8 2,9 52 265-050 7318793624000 50 G2 137 187 110 24,4 3,5 52 266-332 7318793958808 32 Rc1 1/4 133 179 110 8,5 2,6 52 266-340 7318793958907 40 Rc1 1/2 135 181 110 12,8 2,9 52 266-350 7318793959003 50 Rc2 137 187 110 24,4 3,5 Smooth ends 1 m capillary pipe and transition nipples G1/2 and G3/4 are included. L ØD Article No EAN D L H B Kv m Kg G1/16 B H 5-25 kpa 52 465-115 7318793949905 15 15 148 137 72 1,4 1,2 52 465-120 7318793950000 20 22 173 139 72 3,1 1,4 10-40 kpa 52 465-132 7318793935304 32 35 242 179 110 8,5 3,0 52 465-140 7318793935403 40 42 265 181 110 12,8 3,4 10-60 kpa 52 465-015 7318793934703 15 15 148 137 72 1,4 1,2 52 465-020 7318793934802 20 22 173 139 72 3,1 1,4 52 465-025 7318793934901 25 28 191 141 72 5,5 1,6 20-80 kpa 52 465-032 7318793935007 32 35 242 179 110 8,5 3,0 52 465-040 7318793935106 40 42 265 181 110 12,8 3,4 52 465-050 7318793935205 50 54 287 187 110 24,4 4,3 = Flow direction Kv m = m 3 /h at a pressure drop of 1 bar and opening corresponding to the p-band (-20% respectively -25%). *) Can be connected to smooth pipes by KOMBI compression coupling. See accessories or catalogue leaflet KOMBI. G = Thread according to ISO 228. Thread length according to ISO 7/1. Rc = Thread according to ISO 7 ( BS 21). 11

DIFFERENTIAL PRESSURE CONTROLLERS - /STAD /STAD package For more information on STAD see separate catalogue leaflet Article No EAN STAD 5-25 kpa 52 265-101 7318793974303 15 15 52 265-102 7318793974402 20 20 10-40 kpa 52 265-103 7318793974501 32 32 52 265-104 7318793974600 40 40 10-60 kpa 52 265-001 7318793974709 15 10 52 265-002 7318793974808 15 15 52 265-003 7318793974907 20 20 52 265-004 7318793975003 25 25 20-80 kpa 52 265-005 7318793975102 32 32 52 265-006 7318793975201 40 40 52 265-007 7318793975706 50 50 Accessories Draining kit Article No EAN d 52 265-201 7318793660404 G1/2 52 265-202 7318793660503 G3/4 Measuring point Article No EAN 52 265-205 7318793660602 73 G1/16 Measuring point, two-way For connection of capillary pipe while permitting simultaneous use of TA s balancing instrument. Article No EAN 52 179-200 7318793784100 Extension kit for capillary pipe Complete with connections for 6 mm pipe Article No EAN 52 265-212 7318793781505 Setting tool Δp L Article No EAN L H L H 52 265-305 7318793975508 107 85 3 mm 12

DIFFERENTIAL PRESSURE CONTROLLERS - D Compression connection KOMBI See catalogue leaflet KOMBI. Article No EAN D Pipe Ø 53 235-109 7318792874901 G1/2 10 53 235-111 7318792875007 G1/2 12 53 235-112 7318792875106 G1/2 14 53 235-113 7318792875205 G1/2 15 53 235-114 7318792875304 G1/2 16 53 235-117 7318792875403 G3/4 15 53 235-121 7318792875601 G3/4 18 53 235-123 7318792875700 G3/4 22 Insulation For heating/cooling Article No EAN For L H B 52 265-225 7318793658906 15-25 145 172 116 52 265-250 7318793659002 32-50 191 234 154 Spare parts G1/16 Capillary pipe Article No EAN L 52 265-301 7318793661500 1 m Plug Venting Article No EAN 52 265-302 7318793661609 Protective cap Draining Article No EAN 52 265-303 7318793661708 Transition nipple Article No EAN d 52 179-981 7318793660206 G1/2 52 179-986 7318793660305 G3/4 Handwheel Article No EAN 52 265-900 7318793952202 15-25 52 265-901 7318793952301 32-50 13

The products, texts, photographs, graphics and diagrams in this document may be subject to alteration by TA Hydronics without prior notice or reasons being given. For the most up to date information about our products and specifications, please visit www.tahydronics.com. 6-5-5 03.2011