Crankcase pressure regulator Type KVL

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Data sheet Crankcase pressure regulator KVL Crankcase pressure regulator type KVL is fitted in the suction line ahead of the compressor. KVL protects the compressor motor against overload during start-up after long standstill periods or after defrost periods (high pressure in evaporator). Features Accurate, adjustable pressure regulation Wide capacity and operating ranges Pulsation damping design Stainless steel bellows Compact angle design for easy installation in any position Hermetic brazed construction Available in a wide size range of flare and ODF solder types KVL 2-22: Compliant with ATEX hazard zone 2 DKRCC.PD.HH0.D5.02 520H098

Approvals UL LISTED, file SA7200 EAN Technical data Refrigerants Regulating range Maximum working pressure Maximum test pressure KVL 2-22: HCFC, HFC and HC KVL 28-35: HCFC and non-flammable HFC 0.2 6 bar Factory setting = 2 bar PS/MWP = 8 bar Pe = 9.8 bar Medium temperature range -60 30 C Maximum P-band k v-value ) with maximum P-band KVL 2 22: 2 bar KVL 28 35:.5 bar KVL 2 22: 3.2 m 3 / h KVL 28 35: 8.0 m 3 / h ) The k v value is the flow of water in [m 3 / h] at a pressure drop across valve of bar, ρ = 000 kg / m 3. Ordering KVL 2 R22 Rated capacity ) [kw] R34a R404A/ R507 Flare Solder ODF connection 2 ) Code no. R407C [in.] [mm] [in.] [mm] Code no. 7. 5.3 6.3 6.4 2 2 034L004 2 034L0043 7. 5.3 6.3 6.4 2 034L0048 KVL 5 7. 5.3 6.3 6.5 5 8 6 034L0042 5 8 6 034L0049 KVL 22 7. 5.3 6.3 6.5 7 8 22 034L0045 KVL 28 7.8 3.2 5.9 6.4 8 034L0046 7.8 3.2 5.9 6.4 28 034L005 KVL 35 7.8 3.2 5.9 6.4 3 8 35 034L0052 ) Rated capacity is the regulator capacity at: suction temperature t s = -0 C condensing temperature t c = 25 C pressure drop in regulator Δp = 0.2 bar 2 ) KVL supplied without flare nuts. Separate flare nuts can be supplied: 2 in. / 2 mm, code no. 0L03 5 8 in. / 6 mm, code no. 0L67 The connection dimensions chosen must not be too small, as gas velocities in excess of 40 m / s at the inlet of the regulator can result in flow noise. DKRCC.PD.HH0.D5.02 520H098 2

Capacity Max. regulator capacity Q e ) KVL 2 KVL 5 KVL 22 KVL 28 KVL 35 Pressure drop in regulator p Maximum suction pressure PS Capacity Q e in [kw] at suction temperature t s after the regulator [ C] R22 [bar] [bar] -35-30 -25-20 -5-0 -5 0 5 0 5 0..9.2 0. 2 3.0 3.3 3. 2. 0.2 0. 3 3.0 3.3 3.7 4. 4.0 2.2 0. 4 3.0 3.3 3.7 4. 4.6 5.0 3.9 0. 0. 5 3.0 3.3 3.7 4. 4.6 5.0 5.5 5.2.0 0. 6 3.0 3.3 3.7 4. 4.6 5.0 5.5 6.0 6.2.3 0.2 2.6.7 0.2 2 4.2 4.7 4.4 3.0 0.2 0.2 3 4.2 4.7 5.3 5.9 5.6 3. 0.2 4 4.2 4.7 5.3 5.9 6.5 7. 5.5 0. 0.2 5 4.2 4.7 5.3 5.9 6.5 7. 7.8 7.3 0.2 6 4.2 4.7 5.3 5.9 6.5 7. 7.8 8.5 8.7.9 0.3 3.2 2.0 0.3 2 5.2 5.8 5.4 3.7 0.3 0.3 3 5.2 5.8 6.5 7.2 6.9 3.8 0.3 4 5.2 5.8 6.5 7.2 8.0 8.8 6.7 0.2 0.3 5 5.2 5.8 6.5 7.2 8.0 8.8 9.6 9.0.7 0.3 6 5.2 5.8 6.5 7.2 8.0 8.8 9.6 0.5 0.7 2.3 0. 4. 2.6 0. 2 7.4 7.9 7.0 4.6 0.4 0. 3 7.4 8.3 9.3 0.3 8.9 4.7 0. 4 7.4 8.3 9.3 0.3.4 2.3 8.5 0.2 0. 5 7.4 8.3 9.3 0.3.4 2.6 3.8.6 2.2 0. 6 7.4 8.3 9.3 0.3.4 2.6 3.8 5. 3.9 2.8 0.2 5.8 3.6 0.2 2 0.6.2 9.8 6.5 0.5 0.2 3 0.6.8 3.2 4.7 2.5 6.6 0.2 4 0.6.8 3.2 4.7 6.2 7.5 2.0 0.3 0.2 5 0.6.8 3.2 4.7 6.2 7.8 9.6 6.4 3. 0.2 6 0.6.8 3.2 4.7 6.2 7.8 9.6 2.4 9.6 4.0 0.3 7.0 4.4 0.3 2 3.0 3.8 2. 8.0 0.6 0.3 3 3.0 4.6 6.3 8.0 5.4 8. 0.3 4 3.0 4.6 6.3 8.0 9.9 2.5 4.7 0.3 0.3 5 3.0 4.6 6.3 8.0 9.9 2.9 24. 20.0 3.7 0.3 6 3.0 4.6 6.3 8.0 9.9 2.9 24. 26.3 24. 4.9 ) The values in the capacity tables refer to the evaporator capacity and are based on liquid temperature t l = 25 C Correction factors for liquid temperature t l t l [ C] 0 5 20 25 30 35 40 45 50 R22 0.90 0.93 0.96.0.05.0.3.8.24 Plant capacity correction factor = the values in the table DKRCC.PD.HH0.D5.02 520H098 3

Capacity (continued) Max. regulator capacity Q e ) KVL 2 KVL 5 KVL 22 KVL 28 KVL 35 Pressure drop in regulator p Maximum suction pressure PS Capacity Q e in [kw] at suction temperature t s after the regulator [ C] R34a [bar] [bar] -30-25 -20-5 -0-5 0 5 0 5 20 0..8.2 0. 2 2.9 3.3 3. 2.2 0.3 0. 3 2.9 3.3 3.7 4. 4. 2.4 0. 4 2.9 3.3 3.7 4. 4.6 5. 4.2 0.7 0. 5 2.9 3.3 3.7 4. 4.6 5. 5.6 5.6.8 0. 6 2.9 3.3 3.7 4.2 4.6 5. 5.6 6.2 6.7 0.2 2.6.6 0.2 2 4.2 4.7 4.4 3. 0.4 0.2 3 4.2 4.7 5.3 5.9 5.8 3.4 0.2 4 4.2 4.7 5.3 5.9 6.5 7.2 5.9 0.9 0.2 5 4.2 4.7 5.3 5.9 6.5 7.2 7.9 8.0 2.6 0.2 6 4.2 4.7 5.3 5.9 6.5 7.2 7.9 9.5 8.7 0.3 3.2 2.0 0.3 2 5.2 5.8 5.5 3.8 0.5 0.3 3 5.2 5.8 6.5 7.2 7. 4.2 0.3 4 5.2 5.8 6.5 7.2 8.0 8.9 7.3. 0.3 5 5.2 5.8 6.5 7.2 8.0 8.9 9.8 9.8 3.2 0.3 6 5.8 6.5 7.2 8.0 8.9 9.8 0.7 0.7.7 0. 4.0 2.5 0. 2 7.3 7.8 6.9 4.8 0.6 0. 3 7.3 8.2 9.3 0.3 9. 5.2 0. 4 7.3 8.2 9.3 0.3.5 2.7 9.2.4 0. 5 7.3 8.2 9.3 0.3.5 2.7 4.0 2.6 3.9 0. 6 7.3 8.2 9.3 0.3.5 2.7 4.0 5.4 5.3 0.2 5.6 3.5 0.2 2 0.5. 9.8 6.7 0.9 0.2 3 0.5.8 3.2 4.7 2.9 7.3 0.2 4 0.5.8 3.2 4.7 6.3 8. 3. 2.0 0.2 5 0.5.8 3.2 4.7 6.3 8. 9.9 7.8 5.6 0.2 6 0.5.8 3.2 4.7 6.3 8. 9.9 2.9 2.7 0.3 6.9 4.3 0.3 2 2.9 3.7 2. 8.2. 0.3 3 2.9 4.5 6.2 8. 5.8 9.0 0.3 4 2.9 4.5 6.2 8. 20. 22.2 0.3 5 2.9 4.5 6.2 8. 20. 22.2 24.5 2.9 6.8 0.3 6 2.9 4.5 6.2 8. 20. 22.2 24.5 26.9 26.6 ) The values in the capacity tables refer to the evaporator capacity and are based on liquid temperature t l = 25 C Correction factors for liquid temperature t l t l [ C] 0 5 20 25 30 35 40 45 50 R34a 0.88 0.92 0.96.0.05.0.6.23.3 Plant capacity correction factor = the values in the table DKRCC.PD.HH0.D5.02 520H098 4

Capacity (continued) Max. regulator capacity Q e ) KVL 2 KVL 5 KVL 22 KVL 28 KVL 35 Pressure drop in regulator p Maximum suction pressure PS R404A/R507 Capacity Q e in [kw] at suction temperature t s after the regulator [ C] [bar] [bar] -35-30 -25-20 -5-0 -5 0 5 0 5 0. 0.9 0. 2 2.5 2.4.7 0.3 0. 3 2.5 2.9 3.2 3.2.9 0. 4 2.5 2.9 3.2 3.6 4.0 3.4 0.5 0. 5 2.5 2.9 3.2 3.6 4.0 4.5 4.5.5 0. 6 2.5 2.9 3.2 3.6 4.0 4.5 4.9 5.5 2. 0.2.3 0.2 2 3.6 3.4 2.5 0.4 0.2 3 3.6 4.0 4.6 4.5 2.7 0.2 4 3.6 4.0 4.6 5. 5.7 4.8 0.8 0.2 5 3.6 4.0 4.6 5. 5.7 6.3 6.4 2.2 0.2 6 3.6 4.0 4.6 5. 5.7 6.3 7.0 7.8 2.9 0.3.6 0.3 2 4.4 4.2 3.0 0.4 0.3 3 4.4 5.0 5.6 5.6 3.3 0.3 4 4.4 5.0 5.6 6.3 7.0 5.9.0 0.3 5 4.4 5.0 5.6 6.3 7.0 7.8 7.8 2.6 0.3 6 4.4 5.0 5.6 6.3 7.0 7.8 8.6 9.6 3.5 0. 2.0 0. 2 5.9 5.4 3.7 0.5 0. 3 6.2 7. 8.0 7.2 4.2 0. 4 6.2 7. 8.0 9. 0.0 7.4.2 0. 5 6.2 7. 8.0 9. 0.0.2 0. 3.3 0. 6 6.2 7. 8.0 9. 0.0.2 2.4 2.4 4.4 0.2 2.7 0.2 2 8.4 7.6 5.4 0.9 0.2 3 8.9 0..4 0.3 5.9 0.2 4 8.9 0..4 2.9 4.3 0.6.7 0.2 5 8.9 0..4 2.9 4.3 5.9 4.4 4.6 0.2 6 8.9 0..4 2.9 4.3 5.9 7.5 7.6 6.3 0.3 3.4 0.3 2 0.4 9.3 6.5. 0.3 3 0.9 2.5 4.0 2.5 7.2 0.3 4 0.9 2.5 4.0 5.8 7.6 3.0 2. 0.3 5 0.9 2.5 4.0 5.8 7.6 9.6 7.7 5.6 0.3 6 0.9 2.5 4.0 5.8 7.6 9.6 2.6 2.7 7.7 ) The values in the capacity tables refer to the evaporator capacity and are based on liquid temperature t l = 25 C Correction factors for liquid temperature t l t l [ C] 0 5 20 25 30 35 40 45 50 R404A/R507 0.84 0.89 0.94.0.07.6.26.40.57 Plant capacity correction factor = the values in the table DKRCC.PD.HH0.D5.02 520H098 5

Capacity (continued) Max. regulator capacity Q e ) KVL 2 KVL 5 KVL 22 KVL 28 KVL 35 Pressure drop in regulator p Maximum suction pressure PS R407C Capacity Q e in [kw] at suction temperature t s after the regulator [ C] [bar] [bar] -35-30 -25-20 -5-0 -5 0 5 0 5 0..6.0 0. 2 2.5 2.8 2.7.9 0.2 0. 3 2.5 2.8 3.2 3.6 3.6 2.0 0. 4 2.5 2.8 3.2 3.6 4. 4.6 3.6 0. 0. 5 2.5 2.8 3.2 3.6 4. 4.6 5. 4.9.0 0. 6 2.5 2.8 3.2 3.6 4. 4.6 5. 5.6 6.0.3 0.2 2.2.5 0.2 2 3.5 4.0 3.8 2.7 0.2 0.2 3 3.5 4.0 4.6 5.3 5.0 2.9 0.2 4 3.5 4.0 4.6 5.3 5.9 6.5 5. 0. 0.2 5 3.5 4.0 4.6 5.3 5.9 6.5 7.3 6.9 0.2 6 3.5 4.0 4.6 5.3 5.9 6.5 7.3 8.0 8.4.8 0.3 2.7.7 0.3 2 4.4 5.0 4.7 3.3 0.3 0.3 3 4.4 5.0 5.7 6.4 6.2 3.5 0.3 4 4.4 5.0 5.7 6.4 7.2 8. 6.2 0.2 0.3 5 4.4 5.0 5.7 6.4 7.2 8. 8.9 8.5.6 0.3 6 4.4 5.0 5.7 6.4 7.2 8. 8.9 9.9 0.3 2.2 0. 3.4 2.2 0. 2 6.2 6.8 6. 4. 0.4 0. 3 6.2 7. 8. 9.2 8.0 4.3 0. 4 6.2 7. 8. 9.2 0.3.3 7.9 0.2 0. 5 6.2 7. 8. 9.2 0.3.6 2.8 0.9 2. 0. 6 6.2 7. 8. 9.2 0.3.6 2.8 4.2 3.3 2.7 0.2 4.9 3. 0.2 2 8.9 9.6 8.5 5.8 0.2 0.2 3 8.9 0..5 3..3 6. 0.2 4 8.9 0..5 3. 4.6 6..2 0.3 0.2 5 8.9 0..5 3. 4.6 6.4 8.2 5.4 3.0 0.2 6 8.9 0..5 3. 4.6 6.4 8.2 20. 8.8 3.9 0.3 5.9 3.8 0.3 2 0.9.9 0.5 7. 0.5 0.3 3 0.9 2.6 4.2 6.0 3.9 7.5 0.3 4 0.9 2.6 4.2 6.0 7.9 9.8 3.7 0.3 0.3 5 0.9 2.6 4.2 6.0 7.9 20. 22.4 8.8 3.6 0.3 6 0.9 2.6 4.2 6.0 7.9 20. 22.4 24.7 23. 4.8 ) The values in the capacity tables refer to the evaporator capacity and are based on liquid temperature t l = 25 C Correction factors for liquid temperature t l t l [ C] 0 5 20 25 30 35 40 45 50 R407C 0.88 0.9 0.95.0.05..8.26.35 Plant capacity correction factor = the values in the table DKRCC.PD.HH0.D5.02 520H098 6

Sizing For optimum performance, it is important to select a KVL valve according to system conditions and application. The following data must be used when sizing a KVL valve: Refrigerant: KVL 2-22: HCFC, HFC and HC KVL 28-35: HCFC and non-flammable HFC Evaporator capacity: Q e in [kw] Liquid temperature ahead of expansion valve: t l in [ C] Suction temperature ahead of compressor: t s in [ C] Maximum suction pressure after the regulator: PS in [bar] Connection type: flare or solder Connection size in [in.] or [mm] Valve selection Example When selecting the appropriate valve it may be necessary to convert the actual evaporator capacity using a correction factor. This is required when your system conditions are different than the table conditions. The selection is also dependant on the acceptable pressure drop across the valve. The following example illustrates how this is done: Refrigerant: R404A Evaporating capacity: 4.0 kw Liquid temperature ahead of expansion valve: 35 C Suction temperature ahead of compressor: -25 C Maximum suction pressure after the regulator: 3.8 bar ~ -7 C Connectiontype: solder Connection size: 5 8 in. Step Determine the correction factor for liquid temperature t l ahead of expansion valve. From the correction factors table (see below) the correction factor for a liquid temperature at 35 C (R404A) corresponds to a factor of.6. Correction factors for liquid temperature t l t l [ C] 0 5 20 25 30 35 40 45 50 R34a 0.88 0.92 0.96.0.05.0.6.23.3 R22 0.90 0.93 0.96.0.05.0.3.8.24 R404A/R507 0.84 0.89 0.94.0.07.6.26.40.57 R407C 0.88 0.9 0.95.0.05..8.26.35 Step 2 Corrected evaporator capacity is: Q e = 4.0.6 = 4.64 kw Step 3 Now select the capacity table for R404A and choose the column with a suction temperature of -25 C. Using the corrected replacement capacity, select a valve that provides an equivalent or greater capacity than required. KVL 2 / KVL 5 / KVL 22 delivers a capacity of 4.6 kw at a pressure drop of 0.2 bar across the valve and 5.6 kw at a pressure drop of 0.3 bar across the valve. Based on the required connection size of 5 8 in. the KVL 5 valve is the proper selction for this example. Step 4 KVL 5, 5 8 in. solder connection: code no. 034L0049, see ordering table. DKRCC.PD.HH0.D5.02 520H098 7

Design / Function KVL. Protective cap 2. Gasket 3. Setting screw 4. Main spring 5. Valve body 6. Equalization bellows 7. Valve plate 8. Valve seat 9. Damping device The Crankcase pressure regulator type KVL opens at pressure fall on the outlet side, i.e. when the suction pressure ahead of the compressor drops below the set value. The KVL only regulates based on the outlet pressure. Pressure variations on the inlet side of the regulator do not affect the degree of opening since the KVL is equipped with an equalization bellows (6). This bellows has an effective area corresponding to that of the valve seat. The regulator is also equipped with an effective damping device (9) against pulsations, which normally occur in a refrigeration plant. The damping device helps to ensure long life of the regulator without impairing regulation accuracy. DKRCC.PD.HH0.D5.02 520H098 8

P-band and Offset Example with 4 bar setting Capacity Set point [bar] Min. setting point Offset P-band Adjustment range Max. setting point Proportional band The p-band is defined as the difference between the pressure at which the valve plate starts to open (set point) and the pressure at which the valve is completely open. Example If the valve is set to open at 4 bar and the valve p-band is 2 bar, the valve will give maximum capacity when the outlet pressure reaches 2 bar. Offset The offset is defined as the difference between the pressure at which the valve plate starts to open (set point) and the pressure at which the valve reaches the necessary opening for the actual load. The offset is always a part of the p-band Because optimal function of a refrigeration plant is best reached with fully open KVL, the term offset is normally not used in connection with the KVL valve. DKRCC.PD.HH0.D5.02 520H098 9

Dimensions and weights Danfoss 34L05.3 Flare Connection Solder ODF H H 2 B C solder ød Net weight [in.] [mm] [in.] [mm] [mm] [mm] [mm] [mm] [mm] [Kg] KVL 2 2 2 2 2 79 99 64 0 30 0.4 KVL 5 5 8 6 5 8 6 79 99 64 2 30 0.4 KVL 22 7 8 22 79 99 64 7 30 0.4 KVL 28 8 28 259 5 05 20 43.0 KVL 35 3 8 35 259 5 05 25 43.0 Danfoss can accept no responsibility for possible errors in catalogues, brochures and other printed material. Danfoss reserves the right to alter its products without notice. This also applies to products already on order provided that such alterations can be made without subsequential changes being necessary eady agreed. All trademarks in this material are property of the respective companies. Danfoss and the Danfoss logotype are trademarks of Danfoss A/S. All rights reserved. DKRCC.PD.HH0.D5.02 520H098 0