Valve Types and Features

Valve Types and Features The three basic functions of valves are: 1. to stop flow, 2. to keep a constant direction of flow, and 3. to regulate the flow rate and pressure. To select the correct valve to fulfill these functions properly, an outline of the different types of valves and their features is given below. Butterfly valve Check valve Gate valve Globe valve Ball valve Open Open Open Open Open Closed Closed Closed Closed Closed Valve shaped like a butterfly. Tight shut-off and can be used as a control valve. Little resistance to flow (allows smooth flow). Optimal for automated operation with a low operating torque and 90 degrees operating angle. Lightweight and compact (large diameter models are also available). For use when flow is only in one direction. Lightweight disc allows vertical installation. High operating speed prevents water hammer. Like its name implies, the gate is lowered to cut off the path of flow. For use as an on/off valve (not suitable as a control valve). Little resistance to flow when fully open (allows smooth flow). Long stroke requires time to open and close; not suitable for quick operation. The globe-shaped body controls the fluid into a S- shaped flow. Tight shut-off and can be used as a control valve. Large resistance to flow (does not allow smooth flow). Much power is required to open and close the valve (not suitable for large sizes). Valve stopper is ballshaped. For use as an on/off valve (not suitable as a control valve). Little resistance to flow when fully open (allows smooth flow). Optimal for automated operation with a 90 degrees operating angle. Advanced technology is required to manufacture ball. Comparison of butterfly valves with other valves (using mm diameter TOMOE 700G model valve) Butterfly valve and globe valve Butterfly valve and ball valve Butterfly valve and gate valve Item Butterfly valve Globe valve Item Butterfly valve Ball valve Item Butterfly valve Gate valve Pressure loss 0.3 1.5 Pressure loss 0.3 0.05 Pressure loss 0.3 0.2 Flow characteristics Equal Equal Flow characteristics Equal Quick open Flow characteristics Equal Quick open Rangeability 101 301 Rangeability 101 31 Comparison of Cv value Butterfly valve=1 Comparison of pressure loss Butterfly valve=1 Inherent flow characteristics Constant 5 0 Quick open 2 1 1.5 1 Cv 0 Linear Equal 0.7 0.2 Butterfly valve Globe valve Ball valve Gate valve Butterfly valve Globe valve Ball valve Gate valve 0 0 0 0 Valve opening -01 63

Valve Sizing Procedures It is essential to understand the valve sizing formula and selection procedure when determining the size of a valve. The following is the proper selection procedure. The valve sizing calculation is based on ISA. 1. Judge if the flow condition is subcritical or critical based on the given flow condition. 2. Calculate the Cv value by putting the data into an appropriate formula. 3. Select the size of the valve using the Cv value chart. Consider the following points when sizing the valve. q A proper adjustment of the Cv calculation should be made based on the piping adjustment coefficient Fp if a valve is located between reducers. w If the result of the Cv calculation is over 0% compared to the full Cv value, select a valve one size larger. Example: For fresh water with P1 = 0.3 MPa, P2 = 0. MPa, flow rate = m 3 /h, the calculated Cv will be. If 0 mm, 7V is selected, the rated Cv is 176. The calculated Cv () is over 0% of rated the Cv (176) in this case. We recommend mm, 7V. e If no P is given, 5 to 10% of the pump outlet pressure should be used as the assumed P for valve sizing. 6-02

Cv Value Calculation Cv value calculation -03 65

Symbol Legend Symbol Cv: Valve flow coefficient FL: Pressure recovery coefficient G: Specific gravity of gas (Air = 1) Gf: Specific gravity at valve-inlet temperature (Water = 1 at 15 degrees C) P1: Valve-inlet pressure(kpaa) P2: Valve-outlet pressure (kpaa) P: Pressure difference across valve [P1 P2] (kpa) Pc: Critical pressure (kpaa) Pv: Saturated vapour pressure of liquid at valve-inlet temperature (kpaa) PS: Max. DP for sizing Working conditions: Outlet pressure is higher than vapour pressure. PS = P1 Pv (kpa) Working conditions: Outlet pressure is equal to or lower than vapour pressure. Pv DPS = P1 0.960.2 Pv(kPa) PC q: Volume flow rate of liquid (m 3 / h) Q: Volume flow rate of gas [At 15 degrees C, 1 atm](m 3 / h) 2 = Nm 3 /h 273 T: Fluid temperature [273 + degrees C] (K) Tsh: Degree of superheat (degrees C) = T Tc Tc: Saturated vapour temperature at valve-inlet pressure (K) W: Mass flow rate (T / h) = (1,000 kg / h) Fp: Piping geometry factor Cv: Valve flow coefficient d: Valve size (mm) D1: Inlet pipe size (mm) D2: Outlet pipe size (mm) Calculation for piping geometry factor CvR = Fp Cv CvR : Revised Cv value Calculation for modified Cv value 66-0

Conversion Formula for Reference Pressure loss coefficient Cv value Length of pipe D: Inside diameter of pipe (cm) Cv value Kv value Kv value is used in Europe. It shows the flow rate (m 3 /h) of drinking water at a pressure of 1 bar and temperature of 530 degrees C Pressure loss coefficient D: Inside diameter of pipe (cm) Cv value Av value Av value is a SI unit. Kv value D: Inside diameter of pipe (cm) Q: Flow rate ( /min) P: Pressure difference (kpaa) Reference: For performance appraisal of fire safety and disaster prevention equipment, the equivalent pipe length is measured based on the flow rates in the table below. Nominal dia. Flow rate r/min mm 00 65mm 900 0mm 13 mm 2 5mm 00 1mm 00 0mm 0 0mm 13000 300mm 000 Pressure difference : Pressure loss coefficient P: Pressure difference (kpa) : Acceleration of gravity 9. m/sec 2 : Specific gravity (water = 0) (kg/m 3 ) V: Flow velocity (m/sec) -05 67

Guidance for Vacuum Use Valve type Nominal dia. Usable vacuum (kpaa) range (mm) 10 to degrees C to 0 degrees C 0 to degrees C Valve seat leak (kpar/h) Remark 0-0 0.1 0.1 1. 1.0 30A 0-300 1. 1. 2.66.0 3-0 2.66 3.99 5. 0-0 1. 1. 2.66.0 302A 0-300 1. 3.99 5. 1.0 302Y 3-0 0-0 0-300 2.66 1. 2.66 3.99 1. 3.99 5. 2.66 5. 1.0 7Y -0 0-300 1. 2.66 1. 3.99 2.66 5. 1.0 30Y 0-0 0-300 1. 2.66 1. 3.99 2.66 5. 1.0.0 6T 7T 65-0 -300 0.1 1. 2.66 0.3 731P 7P -0 0-300 0.1 0.1 1. 2.66 13.3 26.6 0.3 3.0 Special gland structure required. Leakage increases if heat cycle and open/close frequency is high. 731X 7X 3-0 2.66 13.3 Use not possible. 5.0 0-0 13.3 26.6 Use not possible. 3.0 700G 0-300 26.6 53.2 Use not possible. 5.0 3-0 39.9 66.5 Use not possible. 705G 70G -0 0-300 3-0 13.3 26.6 39.9 26.6 53.2 66.5 Use not possible. Use not possible. Use not possible. 3.0 5.0 722F 5-300 3-0 26.6 39.9 53.2 66.5 Use not possible. Use not possible. 5.0 1T 0-300 3-0 26.6 39.9 53.2 66.5 Use not possible. Use not possible. 5.0 2T 3-0 39.9 66.5 Use not possible. Leak amounts are predicted values based on testing at room temperature with new valves. If you will be using in a range that exceeds the above table, please consult us. -06

Velocity Calculation Velocity limitations are shown below: Velocity limitation Liquid Steam Type of fluid Replaceable rubber seat Vulcanized rubber seat Gas, vapour Saturated steam Superheated steam Velocity limitation (continuous operation) 3 m/s 5 to 6 m/s 1 to 0 m/s to 0 m/s 0 to 1 m/s * Velocity limitation varies depending on the valve models. Please consult us for further information. For liquids Pipe line velocity calculation For gases and vapours For steam Where: V: Flow velocity (m/sec) Q: Flow rate Liquid (m 3 /h) Gas [At 15 degrees C, 1013 Pa] (m 3 /h) = Nm 3 /h Steam (kg/h) U: Specific volume of valve-outlet (m 3 /kg) D: Nominal size (mm) P2: Valve-outlet pressure (kpaa) T: Temperature (degrees C) -07 69

Noise Prediction Methods and Countermeasures Noise measuring method The following are methods recommended by ISA. Note: Parts surrounded by dotted lines are optional. Fig. 1 Laboratory test unit by ISA-RP59.1 Fig. 2 Position of microphone in plant by ISA-RP59.2 Noise calculation formula for 7V and V Types 70-0

Noise calculation formula for valves other than 7V and V Types Formulas are in accordance with those introduced by ISA. For gases When liquid cavitation is generated Where: SP: Noise value [sound pressure level at 91cm] (dba) Cv: Flow coefficient in actual conditions FL: Pressure recovery coefficient P1: Valve upstream pressure (kpaa) P2: Valve downstream pressure (kpaa) m: Weight of pipe wall (kg/m 2 ) : Apparent valve orifice coefficient (butterfly valve: n = 1.) TL: Transmission loss Except for valves releasing directly into the air. *P 2 crit: P1 FL 2 (P1 Pv) (kpaa) Pv: Vapour pressure of liquid (kpaa) X: Conversion fraction of mechanical output X = 1 even if X is bigger than 1. SG: Gas property factor : Acoustical efficiency coefficient (Refer to page -11.) Note: When the difference between Kc and FL 2 exceeds 10% of Kc, substitute Kc for FL 2. -09 71

Specific gravity SG Saturated steam Superheated steam Natural gas Hydrogen Oxygen Ammonia Air Acetylene Carbon dioxide Carbon monoxide gas Helium Methane liquid Nitrogen Propane Ethylene Ethane Refer to the graph on left for fluids other than those above. Specific gravity SG (dba) Specific gravity SG 2 1 0 1 2 3 5 6 7 9 10 0 10 30 0 Molecular weight Weight of pipe (m) mat *A: Basic weight (kg/mmm2) [Steel pipe: 7.5, stainless steel pipe: 7.93] t: Pipe thickness (mm) Nominal dia. mm inch 0 1 12 2 65 2 12 0 3 5 5 1 6 0 0 10 300 3 1 00 1 0 22 5 0 SGP Sch Sch0 27.5 29..0.0 35.3 35.3 39.3 5.5 51. 5.2 62.0 62.0 62.0 62.0.1 35.3 35.3 3.5 0.0 3.2.2.2.2 62.0 62.0 62.0 7.6 7.6 7.6 29.0 30.6 0. 3.2 7.1 51. 55.7 6. 73.0 0.9 7.1 99.7 1.3 11.5. 137. m Sch 35.3 3.5 7.1 51. 55.7 63.6 73.0 0.9 99.7 1.3 11.5 131.1.2 1.7 17.3 3.1 Sch0 0.0 3.2 55.0 59.7 67.5 7.6 6. 99.7 11.5 136.6.2 1.0. 5.7 2.5 3. Sch10S 22.2 22.2... 27.0 27.0 31.7 31.7 35.7 kg/m 2 SchS. 27. 27. 31.7 31.7 39.7 39.7 51.5 51.5 51.5 72-10

...Acoustical efficiency factor -11 73

Aerodynamic noise is discussed here. Noise can be reduced at the following points: 1 Noise source 2 Sound insulation When selecting a countermeasure, controllability of process, initial cost and maintenance cost should be considered along with noise evaluation and noise type. Various factors should be discussed between the customer and manufacturer. Please refer to the section Calculation of Estimated Cavitation and its countermeasure to reduce and prevent cavitation noise. Countermeasures for noise source There are two countermeasures for noise source. Valve noise reduction countermeasures (1) Adoption of low noise valve q 7V and V types: w Globe type low noise valve: (2) Countermeasure at valve downstream side q Insert resistance plate: Max. possible reduction is 10 dba. Max. possible reduction is 15 to.30 dba. Max. possible reduction is 15 dba. Example of low noise unit Sound insulation Example: Pipe lagging materials This countermeasure does not reduce sound generation itself. q Increase of pipe wall thickness (pipe schedule) If it doubles, 5 dba can be reduced. w Soundproof lagging In this countermeasure, piping is covered with layers of heat insulating materials (rock wool), lead plates, or iron plates, etc. e Prepare sound insulating box or wall In order to reduce noise effectively, combine the various methods mentioned above. 7 -

Calculation of Estimated Cavitation Cavitation generation in butterfly valves Cavitation is caused by low pressure areas in fluids. There are four causes of low pressure areas: Fig. 1 Butterfly valves in nearly closed position (1) Fluid is compressed, contraction flow exists, and flow velocity is increased. Then, pressure reduces. (2) Low pressure area inside vortexes at valve-outlet side. (3) Low pressure area is produced at the boundary between the fluid flowing at high velocity and objects such as the protruding portion of the valve-moulded surface, heads of taper pins, and hubs, etc. () When the valve body or disc is vibrating at high frequency, the flow is disturbed and air bubbles form in the fluid. The main causes of cavitation generation in butterfly valves are (1) and (2). Thus, when the valve is nearly closed, the flow passes over the upper and lower edges of the disc as shown in figure. 1. The low pressure area can be caused when high flow velocity is created. VC (vena contracta) Fig. 2 Orifice flow Figure 2 shows orifice flow corresponding to valve flow. The contracted part is called vena contracta. The relation between pressure and flow rate is shown in figure 3. VC When fluids flow at high velocity and pressure drops below the saturated vapour pressure, air bubbles are produced. They are carried away toward the valve downstream side, and then, as surrounding water recovers its original pressure, air bubbles break instantaneously (approx. 1/0 sec) and produce a strong impact force (0 to 0 atm). If air bubbles break near a substance, the impact applies great stress on both the outside and inside of the substance, and causes damage to the surface. Pressure (P) Pv P1 Pvc P2 Flow (V) Fig. 3 Pressure and flow rate relation -13 75

Cavitation generation process in butterfly valves and formula to estimate it There are many stages in cavitation generation, as follows. Flow conditions Pressure conditions Explanation P1 Fig. Normal flow VC P2 Pv Pvc Normal flow means turbulent flow. In this stage, valve flow rate increases in proportion to the square root of the differential pressure. Fig. 5 Cavitation flow P1 Pv VC P2 Cavitation flow has three stages corresponding to the increase in differential pressure. a. Incipient cavitation stage b. Critical cavitation stage c. Full cavitation stage Noise and oscillation may cause damage to the valve and downstream-side piping. Pvc P1 Pv Fig. 6 Flashing flow VC Pvc P2 This occurs when pressure on the valve downstream side drops below the vapour pressure of the liquid. The fluid changes from liquid to gas, bringing rapid velocity change and volume expansion. These two factors are the main causes of a flashing noise. Flashing noise is of lower level than cavitation noise because gas acts as a cushion. Attention must be paid to materials of the valve body (e.g., upgrading to stainless steel or chromium molybdenum steel) or the type of downstream-side piping. 76-1

Cavitation prediction No cavitation P < Kc (P1 Pv) Incipient cavitation P = Kc (P1 Pv) Critical cavitation FL 2 (P1 Pv) > DP > Kc (P1 Pv) Flashing P2 < Pv FL 2 (P1 Pv) > P P: Pressure difference across valve [P1 P2] (kpa) Kc: Cavitation coefficient P1: Valve-inlet pressure (kpaa) P2: Valve-outlet pressure (kpaa) Pv: Vapour pressure of liquid (kpaa) FL: Pressure recovery coefficient Full cavitation P FL 2 (P1 Pv) Cavitation level and availability Type of valve Cavitation level Rubber seated (700G, 702Z) Double Teflon offset metal (302A, 30A) 731P 7V V No cavitation Incipient cavitation Critical cavitation Full cavitation Flashing (Countermeasure is necessary) (Countermeasure is necessary) Suitable Consult us regarding usage. Unsuitable Note: Normal operation material is stainless steel except when. critical cavitation is determined. Cavitation reduction treatment The following are the main methods for reducing or preventing cavitation damage to control valves. (1) Install valves in series and control them. This method is for reducing the pressure load on each valve. In this case, space valves out at least D ( times the pipe diameter). The total Kc or FL will be improved. In order to avoid full cavitation FL should satisfy the following condition: FL > In this case, however, valve control balance may be difficult. Example: When 7V and V types are nearly fully opened, FL is 0.72. When 7V and V types are installed in series, the combined FL is 0.72 = 0. and the permissible pressure difference across the valve is increased by 36%. However, both valves should be operated under exactly the same conditions. -15 (2) Use a resistance plate (perforated orifice for pressure reduction) at the same time. If the flow rate fluctuates heavily, a good result cannot be expected. (3) Use a valve with higher Kc or FL. () Lower the installation position of the valve; that is, lower the secondary pressure. However, this method is hard to adopt in existing piping installations. (5) Rectify the turbulent flow by using a rectifier grid. 77

Concentric type butterfly valve 700 and 00 series Cavitation coefficient Kc and pressure recovery coefficient FL 1.0 1.0 0.9 0.9 0. 0. 0.7 0.7 Kc 0.6 0.5 FL 0.6 0.5 0. 0. 0.3 0.3 0.2 0.2 0.1 0.1 0 10 30 0 70 0 90 0 10 30 0 70 0 90 (Fully closed) Valve opening (%) (Fully open) (Fully closed) Valve opening (%) (Fully open) High performance butterfly valve 300 series 1.0 1.0 0.9 0.9 0. 0. 0.7 0.7 Kc 0.6 0.5 FL 0.6 0.5 0. 0. 0.3 0.3 0.2 0.2 0.1 0.1 0 10 30 0 70 0 90 0 10 30 0 70 0 90 (Fully closed) Valve opening (%) (Fully open) (Fully closed) Valve opening (%) (Fully open) Rotary control valve 7V and V types 1.0 1.0 0.9 0.9 0. 0. 0.7 0.7 Kc 0.6 0.5 FL 0.6 0.5 0. 0. 0.3 0.3 0.2 0.2 0.1 0.1 0 10 30 0 70 0 90 (Fully closed) Valve opening (%) (Fully open) 0 10 30 0 70 0 90 (Fully closed) Valve opening (%) (Fully open) 7 -

Face to Face Dimensions Face to face dimensions Series Diameter 0 65 0 5 1 0 0 300 3 00 0 0 Tomoe applicable types JIS B 02 Wafer shape for Wafer shape API59 tandard equipment for ships Class5 6 7 3 3 6 6 52 56 56 7 7 102 11 7 15 92 102 11 7 15 302A30A 302A (0mm to 300mm) 30A 302Y30Y V (3mm to 6T7T 0mm) 773Z77Z 700G70G705G 731P7P 7X731X 702Z (discontinued) 110 110 1 130 1 1 170 722F 5 67 67 3 95 7 10 11 906C 56 56 66 70 76 95 10 1 903C90C 1 0 0 901C Reference: Maker s face-to-face dimension 0 6 56 56 62 76 5 96 1 7Y 7V 0 0 0 52 62 9 9 9 10 5 5 55 65 90 90 110 1 10 1 1T2T 5 5 55 65 0 90 110 1 10 1 700S (discontinued) 700E 35 35 35 0 0 5 700Z (discontinued) 90 110 110 1 130 1 1 0 107H10H (discontinued) Unit: mm 3 6 6 6 70 76 9 11 11 7Y Y (discontinued) Remark: For detalied dimensions, please refer to the individual dimensional drawings. -17 79

Unit Conversion Conversion from flow rate unit for each type to K/h Gas m 3 /h Gas m 3 /h (at 15 101kPa kg/h kr/h t/h R/h R/min. t/min. Lb/h CFHft 3 /h) SCFH (Nft 3 /h) BBL/h (barrel) BBL/min. GPM (gallon/min.) CFM (ft 3 /min.) SCFM Nm 3 /h (at 0 101kPa) ı ı ı Å Å Å Å Å Å Å Å Å Å ı Torque conversion table Pressure conversion table Pressure unit conversion Conversion from pressure unit for each type to MPaA N N N N O Cavitation prediction O O Specific gravity conversion O O Temp. conversion table Temperature conversion 0-1

Physical Properties Physical properties of liquids Acetaldehyde Acetic acid Acetone Aero motor oil (typical) Alcohol, allyl-n Alcohol, butyl-n Alcohol, ethyl-n (grain) Alcohol, methy-n (wood) Alcohol, propyl-n Ammonia (liquid) Aniline Automobile crankcase oils, SAE 10 SAE SAE 30 SAE 0 SAE SAE SAE 70 Automobile transmission lub, SAE 0 SAE 90 SAE 10 SAE 0 Beer Benzol (Benzene) Brine, calcium chloride, % Brine, sodium chloride, % Bromine Butyric acid-n Carbolic acid (phenol) Carbon disulphide Carbon tetrachloride Castor oil Chloroform Compounded steam cyl oil (5% tal, ow) Decane-n Diethyl ether Ethyl acetate Ethyl biomide Ethylene btomide Ethylene chloride Formic acid Fluid Boiling point Gravity when air pressure is 1 Temp. Water C F C F = 1 at C.6 11.3 56.1 69 5 1 97.2 117.2 117.2 77. 66.1 97.2 7 3 3 172 151 7.3 2 13.9 363 0 61.1 157..2 6.1 76.7 61.1 172. 3.7 77.2 3.3 131.7 3.9.6 176 12 3 3 115 170 12 33 9. 171 101 269 13 213 70 17. 1.3 15 15 0 65 59.72 1.09.79.95.55.1.7.79.79.0.662 1.022..9..9..9..9..9..9..9..9..9..9..9 1.01.79 1. 1. 2.9.959 1.0 1.263 1.59.96 1.9.90.73.71.90 1.5 2.1 1.6 1.221 Molecular weight.05.05 5.0 5.05 7. 6.07 102.17.09 17.31 93. 7.11 159.3.10 9.11 76.1 153. 1.39 12.2 7..10 10.9 17. 9.97 6.03-1

Physical properties of liquids Fluid Freon 11 Freon Freon 21 Fuel oil, No.1 No.2 No.3 No.5 No.6 Gasoline, typical (a) (b) (c) Glycerine, % Glycerine and water. % Glycol, Ethylene Heptane-n Hexane-n Hydrochloric acid, 31.5% Kerosene Lard oil Linseed oil (raw) Marine engine oil (% blown rape) Methy acetate Methy iodide Milk Naphthelene Neatsfoot oil Nitric acid, % Nitrobenzene Nonane-n Octane-n Olive oil Pentane-n Petroleum ether (benzine) Propionic acid Quenching oil (typical) Rapeseed oil Soya bean oil Sperm oil Sugar, % 0% % Sulfuric acid, % 95% % Turbine oil (typical medium) Turpentine Water (fresh) Water (sea) Xyolene-o Boiling point when air pressure is 1 Temp. Gravity C F C F 290 9.3.9 2.1 57.2 2.2 217. 211.1 1 5.6 (29.9) 36.1 11.1 (9.3) 7. 1 11.7 55 9 156 53 135 10 302 (570) 97 26 (9) 60 3 2 27 21.1 26.1 21.1 1. 1. 1. 70 79 70 6 6 6 77 Water = 1 at C 1.9 1. 1.37.2.95.2.95.2.95.2.95.2.95.7.72. 1.26 1.13 1.5..66 1.05.7.2.91.92.92.9.9.93 2.2 1.02 1.0 1.15.91.92 1.37 1.3.71.70.91.63.6.99.6.9.91.9. 1.0 1.1 1.29 1.3 1.3 1..91.6.7 1.0 1.03.7 Molecular weight 92.03 62.07. 6.17 5.0 11.9.6 3.11. 11.22 72.09 7.0 9.0 136. 2 -

Density of fluids Fluid Density Density Temp. g/cm 3 C Acetone 0.792 9. Alcohol, ethyl 0.791 9. Alcohol, methyl 0.10.5 0 Benzene 0.99 56.1 0 Carbolic acid 0.9 0.965 59.2.2 15 Carbon disulfide 1.293 0.7 0 Carbon tetrachloride 1.595 99.6 Chloroform 1.9 93.0 Ether 0.736 5.9 0 Gasoline 0.66 0.69 1.0 3.0 Glycerin 1.2 7.6 0 Kerosene 0.2 51.2 Mercury 13.6 9.0 Milk 1.02 1.035 6.2 6.6 Naphtha, petroleum ether 0.665 1.5 15 Wood 0. 0.10 52.9.5 0 Oils: Castor 0.969.5 15 Coconut 0.9 57.7 15 Cotton seed 0.926 57. Creosote 1.00 1. 6.9.6 15 Linseed, boiled 0.92 5. 15 Olive 0.91 57.3 15 Sea water 1.0 63.99 15 Turpentine (spirits) 0.7 5.3 Water 1.00 62.3-21 3

Critical pressures and temperatures Fluid Critical pressure Pc Critical temperature Tc kpaa Bars (abs.) F C Acetic acid 579 5.0 6 2 Acetone 76 7.6 55 5 Acetylene 620 62.9 97 36 Air 3771 37. 222 11 Ammonia 7 113.0 270 1 Argon.6 1 2 Benzene. 552 29 Butane 367 36.5 307 153 Carbon dioxide 7390 7.0 31 Carbon monoxide 353 35.5 21 139 Carbon tetrachloride 557 5.6 51 Chlorine 770 77.0 291 1 Ethane 9 9.5 90 Ethyl alcohol 6391 6.0 69 3 Ethylene 5115 51.2 10 Ethyl ether 3599 36.0 5 Fluorine 30.3 7 155 Helium 22.9 2.29 2 Heptane 27 27.2 513 267 Hydrogen 96 13.0 00 0 Hydrogen chloride 266 2.6 51 Isobutane 37 37.5 273 13 Isopropyl alcohol 5370 53.7 55 5 Methane 60 6. 117 3 Methyl alcohol 7970 79.6 6 0 Nitrogen 92 3.0 2 17 Nitrous oxide 7267 72.7 99 37 Octane 96.0 565 296 Oxygen. 1 Pentane.5 37 7 Phenol 69 61.3 76 Phosgene 567 56.7 3 Propane 2.6 7 97 Propylene 557 5.6 92 Refrigerant 0 0.1 1 Refrigerant 22 915 9.2 7 97 Sulfur dioxide Water 773 2210 7. 221.0 315 705 157 37-22

Physical properties of gases Fluid Density kgm 3 (0C, 1013 Pa) Gravity Air = 1 Gravity Oxygen = 1 Molecular weight Acetylene 1.173 0.9073 0. 26.0 Air 1.2929 1.0000.907 2.97 Ammonia.7710.5963.5395 17.03 Argon 1.737 1.3796 1.2 39.9 Arsenic fluoride 7.71* 5.96* 5.0* 9.91 Arsenic hydride 3.* 2.695* 2.3* 76.93 Boron fluoride 2.99* 2.31* 2.09* 61.2 Butane (n) 2.* 2.05* 1.* 5. Butane, iso 2.673 2.067 1.70 5. Carbon dioxide 1.9769 1.5290 1..01 Carbon monoxide 1.0.9671.7 2.01 Carbon oxysulfide 2.72 2.10 1.90.07 Chlorine 3.21 2.6 2.9 70.91 Chlorine dioxide 3.0911 2.3911 2.11 67.6 Chlorine monoxide 3.9 3.01 2.72 6.91 Cyanogen 2.5* 1.06 1.63* 52.0 Dimethylamine 1.96617 1.52117 1.37617 5.0 Ethane 1.3566 1.093.993 30.07 Ethylene 1..979. 2.05 Fluorine 1.696 1.3 1.17 3.00 Germanium hydride (digermane) 6.7 5.21.72 151. Germanium tetrahydride 3. 2.65 2.393 76.63 Helium.177.130.9.003 Hydrogen.09.06952.06290 2.0 Hydrogen bromide 3.65 2. 2.53 0.92 Hydrogen chloride 1.6392 1.267 1.171 36.7 Hydrogen iodide 5.791.776.0510 7.93 Hydrogen selenide 3.670 2.39 2.5 0.9 Hydrogen sulfide 1.539 1.0 1.077 3.0 Hydrogen telluride 5.1.9.07 9.63 Krypton 3.70 2. 2.595 3.70 Methane.71.55..0 Methylamine 1.396 1.00.9769 31.06 Methyl chloride 2.3076 1.7 1.61.9 Methyl ether 2.109 1.631 1.76 6.07 Methyl fluoride 1.552 1.51 1.013 3.03 Neon Nitric oxide.90036 1.302.6963 1.0366.6300.937.1 30.01-5

Physical properties of gases Fluid Density kgm 3 (0C, 1013 Pa) Gravity Air = 1 Gravity Oxygen = 1 Molecular weight Nitrogen 1.055.967.7510 2.02 Nitrogen (atm.) 1..9721.795 Nitrosyl chloride 2.992 2.31 2.09 65.7 Nitrosyl fluoride 2.176* 1.3* 1.5* 9.01 Nitrous oxide 1.977 1.5297 1.30.02 Nitroxyl chloride 2.57* 1.99* 1.79* 1.7 Nitroxyl fluoride 2.90 2. 2.03 65.01 Oxygen 1.290 1.10527 1.0000.00 Ozone 2.1 1.65 1.0.00 Phosphine 1.529 1.9 1.0702 3.00 Phosphorus fluoride 3.907* 3.022* 2.73* 7.9 Phosphorus oxyfluoride. 3.7 3. 103.9 Phosphorus pentafluoride 5.1.9.066 5.9 Propane 2.0096 1.55 1.07.09 Radon 9.73 7.526 6.09 222.00 Silicane, chloro- 3.03 2.3 2. 66.5 Silicane, chloromethyl 3.6 2.2 2.55 0. Silicane, dichloromethyl 5.3.1 3.7 115.02 Silicane, dimethyl 2.73 2.11 1.91.1 Silicane, methyl 2.0 1.61 1.6 6. Silicane, trifluoro- 3.6 2.99 2.70 6.07 Silicon fluoride. 3.6 3.27 10.06 Silicon hexahydride 2.5 2. 1.99 62.17 Silicon tetrahydride 1. 1.11 1.00.09 Stibine (15C, 75A) 5.30.10 3.71 5.00 Sulfur dioxide 2.9269 2.263 2.02 6.07 Sulfur fluoride 6.* 5.03*.55* 16.07 Sulfuric oxyfluoride 3.72* 2.* 2.* 102.07 Trimethylamine 2. 1.996 1.05 59.11 Trimethyl boron 2.52 1.95 1.76 55.92 Tungsten fluoride.9 9.9 9.03 297.92 Xenon 5.51.5.09 131.30 * Density at C. 6 -

0 10 21 27 3 3 9 5 66 71 77 2 93 99 10 1 7 13 177 2 2 2 3 33 371 0 70 0 90 110 1 130 10 1 1 170 10 0 0 210 2 2 0 2 20 300 3 00 0 5 0 6 700 0.6107 0.35 1.22 1.7656 2. 3.353.9 6..799 11.6699 15.3.913.636.75 1.3135 51.711 6.3905 79.613 97.3653 101.313 117.99 172.136.5 9.2 61.92 927.97 170.59 2913.07 69. 77.3 10639.2 152. 2. 999.7 0.1 999.1 999.1 99.13 996.76 995.10 993.1 991.03 9.65 96.03 93. 90. 977. 973.1 971. 966.69 962.91 959.00 95. 955.00 96. 937. 927.9 91.06 90.9 59.. 7.15 736.22 677.66 599.0 37.6 1.00 1.00 1.00 1.00 1.00 1.00 1.00.99.99.99.99.9.9.9.97.97.97.96.96.96.96.95.9.93.92.9.6.2.7.7... C F Water temperature kpaa Vapour pressure kgf/m 3 Gravitational weight Gravity - Physical properties of water 7

Saturated steam (Based on temperature) Saturated steam (Based on pressure) This data is provided by the Japan Mechanical Society. -26

Flange Standards Nominal pressure 5K steel flange reference dimensions (JIS B2-96) 0 65 0 5 1 0 0 300 3 00 0 5 0 6 700 7 00 900 0 1 10 13 1 1/2 2 2 1/2 3 5 6 10 1 1 22 26 2 30 3 36 0 5 1 130 155 10 0 5 265 3 35 30 0 5 655 7 770 75 95 995 105 1095 15 1305 1 1575 1 1 1 1 22 22 26 26 26 26 2 2 2 30 3 3 95 105 130 15 5 0 0 20 35 390 35 95 555 5 665 715 770 0 930 90 1030 1130 0 13 15 2 2 15 15 15 27 27 27 27 M M M M M M M M M M M M M M Nominal diameter Flange outer diameter Thickness Bolt nominal screw designation Center diameter Number Bolt hole Diameter Nominal pressure 10K steel flange reference dimensions (JIS B2-96) 10 155 175 15 210 0 20 0 00 5 90 5 6 675 75 795 5 905 970 10 1070 11 35 135 165 30 1 1 1 22 22 26 2 30 30 3 3 36 36 36 3 0 2 105 1 10 1 175 210 0 290 355 00 5 510 565 6 0 730 70 0 900 9 0 10 11 70 130 1 2 2 2 2 2 36 27 27 27 39 39 39 5 M M M M M M M M M M M M36 M36 M36 M2 mm inch 0 65 0 5 1 0 0 300 3 00 0 5 0 6 700 7 00 900 0 1 10 13 1 1/2 2 2 1/2 3 5 6 10 1 1 22 26 2 30 3 36 0 5 mm inch Nominal diameter Flange outer diameter Thickness Bolt nominal screw designation Center diameter Number Bolt hole Diameter -27 9

Nominal pressure K steel flange reference dimensions (JIS B2-96) 10 155 175 0 2 270 305 3 30 0 5 675 730 5 1 22 22 26 2 30 3 3 0 2 6 105 1 10 1 15 2 2 305 30 30 0 5 6 770 27 27 39 M M M M M M M 3 3 3 3 M363 Nominal pressure K steel flange reference dimensions (JIS B2-96) 10 155 175 0 2 270 305 3 30 0 5 675 730 5 1 1 22 26 2 30 3 36 0 6 5 105 1 10 1 15 2 2 305 30 30 0 5 6 770 27 27 39 M M M M M M M 3 3 3 3 M363 0 65 0 5 1 0 0 300 3 00 0 0 1 1/2 2 2 1/2 3 5 6 10 1 1 mm inch 0 65 0 5 1 0 0 300 3 00 0 0 1 1/2 2 2 1/2 3 5 6 10 1 1 mm inch Nominal diameter Flange outer diameter Thickness Bolt nominal screw designation Center diameter Number Bolt hole Diameter Nominal diameter Flange outer diameter Thickness Bolt nominal screw designation Center diameter Number Bolt hole Diameter -2 90

Nominal pressure 30K steel flange reference dimensions (JIS B2-96) Nominal diameter mm 65 0 5 1 0 0 300 inch 2 2 1/2 3 5 6 10 Flange outer diameter 5 0 210 0 275 3 370 515 Thickness 22 26 2 36 3 2 52 Center diameter 130 1 170 5 0 275 3 390 Bolt hole Number Diameter 27 27 Bolt nominal screw designation M M M M M 3 3 ANSI class 1 steel flange reference dimensions (ANSI/ASME B.5-96) Nominal diameter mm inch 0 1 1/2 2 65 2 1/2 0 3 5 5 1 6 0 0 10 300 3 1 00 1 0 0 Flange outer diameter 7 152 17 1 229 279 33 06 3 5 597 635 69 13 Thickness 17.5.1 22.3.9.9.9. 2.6 30.2 31. 35.0 36.6 39.7 2.9 7.7 Center diameter 9.5 1.6 139.7 152. 0.5 215.9 1.3 29. 361.9 31. 76.2 539.7 577. 635.0 79.3 Bolt hole Number Diameter 26 26 29 29 35 Bolt nominal screw designation U1/2-13UNC U5/-11UNC U5/-11UNC U5/-11UNC U5/-11UNC U3/-10UNC U3/-10UNC U3/-10UNC U7/- 9UNC U7/- 9UNC U1 - UNC U1 - UNC U1 1/-UN U1 1/-UN U1 1/-UN ANSI class 300 steel flange reference dimensions (ANSI/ASME B.5-96) mm Nominal diameter 65 0 5 1 0 0 300 inch 2 2 1/2 3 5 6 10 Flange outer diameter 5 1 210 279 31 31 521 Thickness 22.3. 2.6 31. 35.0 36.6 1.3 7.7. Center diameter 7.0. 1.1 0.2 5.0 269.7 0.2 37..9 Bolt hole Number Diameter 26 29 Bolt nominal screw designation U5/-11UNC U3/-10UNC U3/-10UNC U3/-10UNC U3/-10UNC U3/-10UNC U7/- 9UNC U1 - UNC U1 1/-UN -29 91