RELIEF CAPACITY CURVES

Transcription

1 E (800) TANKAGE VENTING RELIEF CAPACITY CURVES SERIES 6000 PVRV SERIES 4000 MARSH HAWK TRV SERIES 5000 EPRV RE SERIES 200 & 300 TVTH RE

2

3 INTRODUCTION INTRODUCTION A relief capacity curve provides the flow relieving capacity of a particular venting device by plotting the flow rate through the device on the horizontal, or x-axis against the tank pressure specifically pressure at the inlet of the vent, on the vertical or y-axis. These curves can be used to size a venting device for a given application. REQUIRED INFORMATION The type and configuration of the required device must be known in order to size a vent. This information is often integral to the purpose of the vent. For example, if the vent is for emergency pressure relief, an EPRV will likely be selected, if the relieved vapors must be collected or processed then a Pipe-Away PVRV will be selected. Refer to corresponding brochures and technical bulletin TB-1217-TV for assistance in vent selection. A minimum of three quantities based on the design of the tank, process or application are required to size a relief device: required relieving flow capacity for pressure and/or vacuum; maximum relieving pressure/vacuum; and, set pressure/vacuum. Pressure relief and vacuum relief are sized separately. HOW TO USE RELIEF CAPACITY CURVES 1. Use the device and size estimation charts in conjunction with the table of contents to find the type and configuration of the device required. 2. Begin sizing by turning to the pressure flow curve (if applicable) of the smallest available size for the selected device. 3. Flow curves for multiple set pressures/vacuums are displayed on each graph. Identify the flow curve that corresponds to the required set pressure/vacuum. 4. On the vertical axis (Tank Pressure) find the maximum relieving pressure and draw a horizontal line at this pressure until it crosses the previously identified flow curve. 5. At the point where the flow curve and horizontal line cross, draw a vertical line down to the horizontal axis (Flow Rate through Device). The number on this axis represents the flow rate through the device at the maximum relieving pressure. 6. If the flow rate through the device is lower than the required relieving capacity, repeat steps 3-5 for the next larger vent size until the flow relieving capacity of the vent exceeds the required relieving capacity. Notes: i. If the required relieving capacity cannot be satisfied by the largest available size in the selected venting class, a larger venting class, such as an EPRV, or multiple vents can be added to meet the required relieving capacity. ii. iii. iv. If the minimum required vent size differs as a result of pressure sizing and vacuum sizing, the larger vent of the two must be chosen. The gas type and conditions must be the same between units. Follow appropriate conversion method to convert between gas types and conditions. All pressure readings are provided in gauge pressure (zero-referenced to ambient pressure). UNIT CONVERSIONS - PRESSURE The pressures reported on the capacity charts published by Hawkeye are reported in in ounces per square inch (ozsi). To convert from other pressure units to ozsi, select the appropriate conversion factor from this chart: CONVERSION FACTORS PRESSURE TO OUNCES PER SQUARE INCH (OZSI) (5 SIG- FIG) To Convert From: Multiply by: psi pounds per square inch atm atmsophere mbar millibar bar bar Pa pascals kpa kilopascals MPa megapascals kgf/m² kilogram (force) per square metre kfg/cm² kiogram (force) per square centimetre mmhg millimetres of mercury (60 F) inhg inches of mercury inh 2 O inches of water Torr Torr Example: Convert 5 kpa to ozsi. From the chart above, the conversion factor is We ll multiply 5 kpa by this number to get the pressure in ozsi. 5 kpa = ozsi» 11.6 ozsi UNIT CONVERSIONS - VOLUMETRIC FLOW The flow rates reported on the capacity charts published by Hawkeye Industries are equivalent volumetric flows, in cubic feet per hour, of air at standard conditions, and noted as SCFH (air). Unlike liquid or solid quantities, measuring and reporting gaseous properties is complicated by properties that change as temperature and pressure change. As such, gaseous properties are reported in terms of reference conditions. These are conditions specified by API th Edition, Annex D, and may not correspond to other internationally recognized conditions (IUPAC, ISO, etc.). This means that to convert a unit in normal conditions to a different unit in standard conditions, it is a two step process. 1.) Convert conditions 2.) Convert units The first reference conditions, called Standard Conditions, reports the volume of a gas at a pressure of kpa absolute [ psia], and at a temperature of C [60 F]. Units reported in Standard conditions are prefixed with an S. (eg. SCFM instead of CFM) The other common condition, usually associated with metric units, is Normal Conditions. These report volume of a gas at pressure of kpa absolute [ psia] and at 0 C [32 F]. Units reported in Normal conditions are prefixed with an N. (eg Nm3/ hr instead of m3/hr) 2 2

4 INTRODUCTION INTRODUCTION To convert between normal and standard conditions, multiplying the normal condition property by Example: Convert 1000 Nm³/hr to Sm³/hr We see that the provided volume is in Normal conditions, by the N preceding the volume unit. To convert to an equivalent volume in standard conditions, we multiply by Nm 3/hr = Sm 3/hr Note the units remain the same in these conversions, only the conditions change. To complete the conversion to another unit, i.e. CFH, the appropriate conversion factor from the table below must be used. These conversion factors maintain the same condition of the starting unit. CONVERSION FACTORS VOLUMETRIC FLOW TO CUBIC FEET PER HOUR (CFH) (5 SIG- FIG) To Convert From: CFM cubic feet per minute 60 CFS cubic feet per hour 3600 Multiply by: m³/hr cubic metres per hour m³/min cubic metres per minute m³/s cubic metres per second L/hr litres per hour L/min litre per minute L/s litres per second US gph US gallons per hour US gpm US gallons per minute US gps US gallons per second Imperial gph Imp/UK gallons per hour Imperial gpm Imp/UK gallons per minute Imperial gps Imp/UK gallons per second US bpd US Barrels per day Sm³/hr = 18,153.7 SCFH. Example: Convert 1000 US gph to SCFH There is no reference condition on the starting unit, so we can skip the reference condition conversion. Technically then, our answer will be in CFH, not SCFH. 1.) Convert units From the chart, the conversion factor from US gph to CFH is US gph = CFH. MORE COMPLICATED CONVERSIONS Example: Convert 12 ozsi to Pa The values on the pressure conversion chart are for converting to ozsi, not from. However, we can still use these factors and divide by them instead of multiplying. From the chart, the conversion factor from Pa to ozsi is To get bar from ozsi, we will divide by this number. 12 ozsi = 5,171.1 Pa. Example: Convert 20,000 CFH to m³/hr The values on the volumetric flow conversion chart are for converting to CFH, not from. However, we can still use these facts and divide by them instead of multiplying. Note, there is no reference conditions on the units we are working with. From the chart, the conversion factor from m³/hr to CFH is To get m3/hr from CFH, we will divide by this number. 20,000 CFH = m³/hr. Note, if a volumetric flow is provided without a reference condition (i.e not Normal or Standard ) do not perform the condition conversion. However, this does not mean that the end unit does not require a reference condition; please consult engineering in these cases. Example: Convert 500 Nm3/hr to SCFH We see that the provided volume is in Normal conditions, by the N preceeding the volume unit, and we are looking for an answer in Standard conditions. 1.) Convert to standard conditions 500 Nm 3 /hr = Sm 3 /hr Example: Convert 5,000 SCFH to Nm³/hr Note, there are reference conditions on the units we are working with, so we will need to take that into account. The factor of we have is to go from Normal conditions to Standard conditions. We can convert from Standard conditions to normal by dividing by this same number. 1.) Convert to Normal Conditions 5000 SCFH = NCFH 2.) Convert units From the chart, the conversion factor from m³/hr to CFH is To get m3/hr from CFH, we will divide by this number NCFH = Nm³/hr. 2.) Convert units From the chart, the conversion factor from m³/hr to CFH is

5 ALL VENTS DEVICE FLOW RANGE - PRESSURE SERIES 5000 EPRV ALL VENTS DEVICE FLOW RANGE - PRESSURE 4 OZSI 16 OZSI E PR V OZSI 16 OZSI 32 OZSI E PR V OZSI SERIES 6000 PVRV - UBR VALVE 0.5 OZSI 16 OZSI P VRV - 6 U 0.5 OZSI 32 OZSI 16 OZSI P VRV - 4 U 32 OZSI 0.5 OZSI 16 OZSI P VRV - 3 U 32 OZSI 0.5 OZSI 16 OZSI P VRV - 2 U 32 OZSI SERIES 6000 PVRV - STD VALVE 0.5 OZSI 16 OZSI P VRV - 6 S 0.5 OZSI 16 OZSI P VRV - 4 S 0.5 OZSI 16 OZSI P VRV - 3 S 0.5 OZSI 16 OZSI P VRV - 2 S VENTING GAUGE HATCHES 4 OZSI 16 OZSI T VT H 2 OZSI 16 OZSI 32 OZSI M A R S H HAWK 32 OZSI FLOW RATES ARE AT 100% OVERPRESSURE FOR INDICATED SET PRESSURES. LIGHTER SHADED REGION INDICATES EXTENDED SERVICE RANGE (SET PRESSURE > 16OZSI) IF AVAILABLE

6 ALL VENTS DEVICE FLOW RANGE - VACUUM SERIES 6000 PVRV - UBR VALVE ALL VENTS DEVICE FLOW RANGE - VACUUM 0.5 OZSI 8 OZSI P VRV - 6 U 0.5 OZSI 8 OZSI P VRV - 4 U 0.5 OZSI 8 OZSI P VRV - 3 U SERIES 6000 PVRV - STD VALVE 0.5 OZSI 8 OZSI P VRV - 2 U 0.5 OZSI 8 OZSI P VRV - 6 S 0.5 OZSI 8 OZSI P VRV - 4 S 0.5 OZSI 8 OZSI P VRV - 3 S 0.5 OZSI 8 OZSI P VRV - 2 S FLOW RATES ARE AT 100% OVERPRESSURE FOR INDICATED SET PRESSURES. LIGHTER SHADED REGION INDICATES EXTENDED SERVICE RANGE (SET PRESSURE > 16OZSI) IF AVAILABLE

7 VENTING GAUGE HATCHES SIZE ESTIMATION CHART - PRESSURE 100% 95% 90% 85% M A R S H H A W K 8 2 O Z S I M A R S H H A W K O Z S I T V T H 8 4 O Z S I VENTING GAUGE HATCHES SIZE ESTIMATION CHART - PRESSURE T V T H O Z S I 80% 75% 70% 65% 60% 55% 50% 45% 40% 35% 30% 25% 20% 1.) LOCATE FLOW RATE ON HORIZONTAL (X) AXIS. 15% 10% 5% 0% 2.) TRACE LINE UPWARDS TO DESIRED TANK PRESSURE FROM VERTICAL (Y) AXIS [NOTE: PRESSURE IS IN TERMS OF % OVER SET PRESSURE, WHERE 100% = 2 SET PRESSURE] 3.) SELECT DEVICE SIZE WHOSE FLOW PROFILE CONTAINS THE INTERSECTION OF THESE TWO LINES. 4.) IF THE INTERSECTION POINT LIES WITHIN MULTIPLE DEVICE PROFILES, SELECT THE LEFT-MOST DEVICE FOR SMALLER SIZE. 5.) ONCE DEVICE SIZE IS SELECTED, CONSULT THE FLOW CURVE TO THAT SPECIFIC DEVICE, CONFIGURATION SIZE, VALVE TYPE AND CONFIRM SUITABILITY OF FLOW CAPACITY

8 VENTING GAUGE HATCHES VENTING GAUGE HATCHES SIZE ESTIMATION CHART - VACUUM SIZE ESTIMATION CHART - VACUUM 0% 1.) LOCATE FLOW RATE ON HORIZONTAL (X) AXIS. 5% 10% 2.) TRACE LINE UPWARDS TO DESIRED TANK PRESSURE FROM VERTICAL (Y) AXIS [NOTE: PRESSURE IS IN TERMS OF % OVER SET PRESSURE, WHERE 100% = 2 SET PRESSURE] 3.) SELECT DEVICE SIZE WHOSE FLOW PROFILE CONTAINS THE INTERSECTION OF THESE TWO LINES. 4.) IF THE INTERSECTION POINT LIES WITHIN MULTIPLE DEVICE PROFILES, SELECT THE LEFT-MOST DEVICE FOR SMALLER SIZE. 15% 5.) ONCE DEVICE SIZE IS SELECTED, CONSULT THE FLOW CURVE TO THAT SPECIFIC DEVICE, CONFIGURATION SIZE, VALVE TYPE AND CONFIRM SUITABILITY OF FLOW CAPACITY. 20% 25% 30% 35% 40% 45% 50% 55% 60% 65% 70% 75% 80% M A R S H H A W K O Z S I 85% 90% T V T H O Z S I 95% 100%

9 SERIES 5000 EPRV SIZE ESTIMATION CHART - PRESSURE SERIES 5000 EPRV SIZE ESTIMATION CHART - PRESSURE 100% 95% 90% E P R V O Z S I E P R V O Z S I E P R V O Z S I E P R V O Z S I 85% 80% 75% 70% 65% 60% 55% 50% 45% 40% 35% 30% 25% 20% 1.) LOCATE FLOW RATE ON HORIZONTAL (X) AXIS. 15% 10% 5% 0% ) TRACE LINE UPWARDS TO DESIRED TANK PRESSURE FROM VERTICAL (Y) AXIS [NOTE: PRESSURE IS IN TERMS OF % OVER SET PRESSURE, WHERE 100% = 2 SET PRESSURE] 3.) SELECT DEVICE SIZE WHOSE FLOW PROFILE CONTAINS THE INTERSECTION OF THESE TWO LINES. 4.) IF THE INTERSECTION POINT LIES WITHIN MULTIPLE DEVICE PROFILES, SELECT THE LEFT-MOST DEVICE FOR SMALLER SIZE. 5.) ONCE DEVICE SIZE IS SELECTED, CONSULT THE FLOW CURVE TO THAT SPECIFIC DEVICE, CONFIGURATION SIZE, VALVE TYPE AND CONFIRM SUITABILITY OF FLOW CAPACITY. 8 8

10 SERIES 6000 PVRV SIZE ESTIMATION CHART - PRESSURE STD 100% 95% 90% 85% 80% P V R V 2 ½ O Z S I P V R V 3 ½ O Z S I P V R V O Z S I P V R V 4 ½ O Z S I P V R V 6 ½ O Z S I P V R V O Z S I SERIES 6000 PVRV SIZE ESTIMATION CHART - PRESSURE STD P V R V O Z S I P V R V O Z S I 75% 70% 65% 60% 55% 50% 45% 40% 35% 30% 25% 20% 1.) LOCATE FLOW RATE ON HORIZONTAL (X) AXIS. 15% 10% 5% 0% ) TRACE LINE UPWARDS TO DESIRED TANK PRESSURE FROM VERTICAL (Y) AXIS [NOTE: PRESSURE IS IN TERMS OF % OVER SET PRESSURE, WHERE 100% = 2 SET PRESSURE] 3.) SELECT DEVICE SIZE WHOSE FLOW PROFILE CONTAINS THE INTERSECTION OF THESE TWO LINES. 4.) IF THE INTERSECTION POINT LIES WITHIN MULTIPLE DEVICE PROFILES, SELECT THE LEFT-MOST DEVICE FOR SMALLER SIZE. 5.) ONCE DEVICE SIZE IS SELECTED, CONSULT THE FLOW CURVE TO THAT SPECIFIC DEVICE, CONFIGURATION SIZE, VALVE TYPE AND CONFIRM SUITABILITY OF FLOW CAPACITY. 9 9

11 SERIES 6000 PVRV SIZE ESTIMATION CHART - VACUUM STD 0% SERIES 6000 PVRV SIZE ESTIMATION CHART - VACUUM STD 1.) LOCATE FLOW RATE ON HORIZONTAL (X) AXIS. 5% 10% 2.) TRACE LINE UPWARDS TO DESIRED TANK PRESSURE FROM VERTICAL (Y) AXIS [NOTE: PRESSURE IS IN TERMS OF % OVER SET PRESSURE, WHERE 100% = 2 SET PRESSURE] 3.) SELECT DEVICE SIZE WHOSE FLOW PROFILE CONTAINS THE INTERSECTION OF THESE TWO LINES. 4.) IF THE INTERSECTION POINT LIES WITHIN MULTIPLE DEVICE PROFILES, SELECT THE LEFT-MOST DEVICE FOR SMALLER SIZE. 15% 5.) ONCE DEVICE SIZE IS SELECTED, CONSULT THE FLOW CURVE TO THAT SPECIFIC DEVICE, CONFIGURATION SIZE, VALVE TYPE AND CONFIRM SUITABILITY OF FLOW CAPACITY. 20% 25% 30% 35% 40% 45% 50% 55% 60% 65% 70% 75% 80% 85% P V R V 2 ½ O Z S I P V R V 3 ½ O Z S I P V R V 4 ½ O Z S I P V R V 6 ½ O Z S I 90% 95% P V R V 2 8 O Z S I P V R V O Z S I P V R V 4 8 O Z S I P V R V 6 8 O Z S I 100%

12 P V R V 2 ½ O Z S I SERIES 6000 PVRV SIZE ESTIMATION CHART - PRESSURE UBR 100% 95% 90% 85% 80% P V R V 3 ½ O Z S I P V R V O Z S I P V R V 4 ½ O Z S I P V R V 6 ½ O Z S I P V R V O Z S I SERIES 6000 PVRV SIZE ESTIMATION CHART - PRESSURE UBR P V R V O Z S I P V R V O Z S I 75% 70% 65% 60% 55% 50% 45% 40% 35% 30% 25% 20% 15% 10% 5% 0% ) LOCATE FLOW RATE ON HORIZONTAL (X) AXIS. 2.) TRACE LINE UPWARDS TO DESIRED TANK PRESSURE FROM VERTICAL (Y) AXIS [NOTE: PRESSURE IS IN TERMS OF % OVER SET PRESSURE, WHERE 100% = 2 SET PRESSURE] 3.) SELECT DEVICE SIZE WHOSE FLOW PROFILE CONTAINS THE INTERSECTION OF THESE TWO LINES. 4.) IF THE INTERSECTION POINT LIES WITHIN MULTIPLE DEVICE PROFILES, SELECT THE LEFT-MOST DEVICE FOR SMALLER SIZE. 5.) ONCE DEVICE SIZE IS SELECTED, CONSULT THE FLOW CURVE TO THAT SPECIFIC DEVICE, CONFIGURATION SIZE, VALVE TYPE AND CONFIRM SUITABILITY OF FLOW CAPACITY

13 SERIES 6000 PVRV SIZE ESTIMATION CHART - VACUUM UBR 0% SERIES 6000 PVRV SIZE ESTIMATION CHART - VACUUM UBR 1.) LOCATE FLOW RATE ON HORIZONTAL (X) AXIS. 5% 10% 15% 20% 25% 2.) TRACE LINE UPWARDS TO DESIRED TANK PRESSURE FROM VERTICAL (Y) AXIS [NOTE: PRESSURE IS IN TERMS OF % OVER SET PRESSURE, WHERE 100% = 2 SET PRESSURE] 3.) SELECT DEVICE SIZE WHOSE FLOW PROFILE CONTAINS THE INTERSECTION OF THESE TWO LINES. 4.) IF THE INTERSECTION POINT LIES WITHIN MULTIPLE DEVICE PROFILES, SELECT THE LEFT-MOST DEVICE FOR SMALLER SIZE. 5.) ONCE DEVICE SIZE IS SELECTED, CONSULT THE FLOW CURVE TO THAT SPECIFIC DEVICE, CONFIGURATION SIZE, VALVE TYPE AND CONFIRM SUITABILITY OF FLOW CAPACITY. 30% 35% 40% 45% 50% 55% 60% 65% 70% 75% 80% 85% P V R V 2 ½ O Z S I P V R V 3 ½ O Z S I P V R V 4 ½ O Z S I P V R V 6 ½ O Z S I 90% 95% P V R V 2 8 O Z S I P V R V O Z S I P V R V 4 8 O Z S I P V R V 6 8 O Z S I 100%

14 FLOW CURVE INDEX FLOW CURVE INDEX Introduction to Hawkeye Flow Curve Reference Book... 2 Series 200 & 300 TVTH... Pressure + Vacuum Curve... Pressure + Vacuum Relief Atmosphere STD...[P-28VGH] Series 4000 Marsh Hawk... Pressure + Vacuum Curve... Pressure + Vacuum Relief Atmosphere STD...[P-48VGH] Series 5000 EPRV Pressure Curve... Pressure Relief Only Atmosphere STD...[P-50XX/52XX] Series 5000 EPRV Pressure Curve... Pressure Relief Only Atmosphere STD...[P-51XX/53XX] Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere UBR...[P-6200/02] Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere STD...[P-6203/01] Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away UBR...[P-6210/12]...20 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away STD...[P-6213/11] Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere STD...[P-6224]...22 Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere UBR...[P-6225]...23 Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away STD...[P-6234]...24 Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away UBR...[P-6235]...25 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere UBR...[P-6300/02]...26 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere STD...[P-6303/01]...27 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away UBR...[P-6310/12]...28 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away STD...[P-6313/11]...29 Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere STD...[P-6324]...30 Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere UBR...[P-6325] Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away STD...[P-6334]...32 Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away UBR...[P-6335]...33 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere UBR...[P-6400/02]...34 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere STD...[P-6403/01]...35 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away UBR...[P-6410/12]...36 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away STD...[P-6413/11]...37 Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere STD...[P-6424]...38 Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere UBR...[P-6425]...39 Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away STD...[P-6434]...40 Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away UBR...[P-6435] Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere UBR...[P-6600/02]...42 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Atmosphere STD...[P-6603/01]...43 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away UBR...[P-6610/12]...44 Series 6000 PVRV Pressure Curve... Pressure + Vacuum Relief Pipe-Away STD...[P-6613/11]...45 Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere STD...[P-6624]...46 Series 6000 PVRV Pressure Curve... Pressure Relief Only Atmosphere UBR...[P-6625]...47 Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away STD...[P-6634]...48 Series 6000 PVRV Pressure Curve... Pressure Relief Only Pipe-Away UBR...[P-6635]...49 Series 6000 PVRV - 8 API... Pressure Curve... Pressure + Vacuum Relief Atmosphere UBR...[P-6800/02]...50 Series 6000 PVRV - 8 API... Pressure Curve... Pressure + Vacuum Relief Atmosphere STD...[P-6803/01] Series 6000 PVRV - 8 API... Pressure Curve... Pressure + Vacuum Relief Pipe-Away UBR...[P-6810/12]...52 Series 6000 PVRV - 8 API... Pressure Curve... Pressure + Vacuum Relief Pipe-Away STD...[P-6813/11]...53 Series 6000 PVRV - 8 API... Pressure Curve... Pressure Relief Only Atmosphere STD...[P-6824]...54 Series 6000 PVRV - 8 API... Pressure Curve... Pressure Relief Only Atmosphere UBR...[P-6825]...55 Series 6000 PVRV - 8 API... Pressure Curve... Pressure Relief Only Pipe-Away STD...[P-6834]...56 Series 6000 PVRV - 8 API... Pressure Curve... Pressure Relief Only Pipe-Away UBR...[P-6835]...57 Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere UBR...[V-6200/03/10/13]...58 Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere STD...[V-6203/01/12/11]...59 Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere STD...[V-6246]...60 Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere UBR...[V-6247] Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere UBR...[V-6300/03/10/13]...62 Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere STD...[V-6303/01/12/11]...63 Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere STD...[V-6346]...64 Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere UBR...[V-6347]...65 Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere UBR...[V-6400/03/10/13]...66 Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere STD...[V-6403/01/12/11]...67 Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere STD...[V-6446]...68 Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere UBR...[V-6447]...69 Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere UBR...[V-6600/03/10/13]...70 Series 6000 PVRV Vacuum Curve... Pressure + Vacuum Relief Atmosphere STD...[V-6603/01/12/11] Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere STD...[V-6646]...72 Series 6000 PVRV Vacuum Curve... Vacuum Relief Only Atmosphere UBR...[V-6647] Series 6000 PVRV - 8 API... Vacuum Curve... Pressure + Vacuum Relief Atmosphere UBR...[V-6800/03/10/13] Series 6000 PVRV - 8 API... Vacuum Curve... Pressure + Vacuum Relief Atmosphere STD...[V-6803/01/12/11] Series 6000 PVRV - 8 API... Vacuum Curve... Vacuum Relief Only Atmosphere STD...[V-6846] Series 6000 PVRV - 8 API... Vacuum Curve... Vacuum Relief Only Atmosphere UBR...[V-6847]...77 CONTACT YOUR HAWKEYE SALES REPRESENTATIVE TO GET THE FLOW CURVE FOR YOUR SPECIFIC DEVICE

15

16 Contents Hawkeye Industries Inc. This document is uncontrolled, and is subject to change without notice. Please refer to for the most up-to-date product information. Printed in Canada Ave NW Edmonton, AB, Canada T6P 1N6 Toll Free: (800) Phone: (780) Fax: (780) Flow Curve Back Cover Mar 2018