1、Designation:D277992(Reapproved 2020)Standard Test Method forEstimation of Solubility of Gases in Petroleum Liquids1This standard is issued under the fixed designation D2779;the number immediately following the designation indicates the year oforiginal adoption or,in the case of revision,the year of
2、last revision.A number in parentheses indicates the year of last reapproval.Asuperscript epsilon()indicates an editorial change since the last revision or reapproval.1.Scope1.1 This test method covers the estimation of the equilib-rium solubility of several common gases encountered in theaerospace i
3、ndustry in hydrocarbon liquids.These includepetroleum fractions with densities in the range from 0.63 to0.90 at 288 K(59F).The solubilities can be estimated over thetemperature range 228 K(50F)to 423 K(302F).1.2 This test method is based on the Clausius-Clapeyronequation,Henrys law,and the perfect g
4、as law,with empiri-cally assigned constants for the variation with density and foreach gas.1.3 The values stated in SI units are to be regarded as thestandard.The values in parentheses are for information only.1.4 This standard does not purport to address all of thesafety concerns,if any,associated
5、with its use.It is theresponsibility of the user of this standard to establish appro-priate safety,health,and environmental practices and deter-mine the applicability of regulatory limitations prior to use.1.5 This international standard was developed in accor-dance with internationally recognized p
6、rinciples on standard-ization established in the Decision on Principles for theDevelopment of International Standards,Guides and Recom-mendations issued by the World Trade Organization TechnicalBarriers to Trade(TBT)Committee.2.Referenced Documents2.1 ASTM Standards:2D1298 Test Method for Density,Re
7、lative Density,or APIGravity of Crude Petroleum and Liquid Petroleum Prod-ucts by Hydrometer Method3.Terminology3.1 Definitions:3.1.1 Bunsen coeffcientthe solubility of a gas expressedas the volume,reduced to 273 K(32F)and 101.3 kPa(1 atm),dissolved by 1 volume of liquid at the specified temperature
8、and 101.3 kPa.3.1.2 Henrys lawthe principle that the ratio of partialpressure to mole fraction of gas in solution is a constant.3.1.2.1 DiscussionIn non-ideal systems the fugacity isused to replace the pressure,but the systems within the scopeof this test method can be considered ideal within the li
9、mits ofthe accuracy statement.3.1.3 Ostwald coeffcientthe solubility of a gas expressedas the volume of gas dissolved per volume of liquid when thegas and liquid are in equilibrium at the specified partialpressure of gas and at the specified temperature.3.2 Symbols:d=density of the liquid at 288 K(5
10、9F),kg/L,T=specified temperature,K,Lo=Ostwald coefficient at 273 K for a liquid ofd=0.85,L=Ostwald coefficient at T for a liquid ofd=0.85,Lc=Ostwald coefficient at T for a liquid of thespecified density,p=pressure of the gas,or mixed gases,MPa,pv=vapor pressure of the liquid at the specifiedtemperat
11、ure,MPa,p1,p2.pi=partial pressures of the gases in a mixture,MPa,G=solubility,mg/kg,B=Bunsen coefficient at the specified d,p,and T,X=mole fraction of gas in equilibrium solution,Lm,Bm=coefficients for mixture of gases,M=molecular weight of the gas,g/mol,Ml=molecular weight of the liquid,g/mol,H=Hen
12、rys law constant,MPa,andC=molarity,kg mol/m3.4.Summary of Test Method4.1 Correlations have been established by the NationalAeronautics and Space Administration(formerly National1This test method is under the jurisdiction of ASTM Committee D27 onElectrical Insulating Liquids and Gases and is the dire
13、ct responsibility of Subcom-mittee D27.07 on Physical Test.Current edition approved Nov.1,2020.Published November 2020.Originallyapproved in 1969.Last previous edition approved in 2012 as D277992(2012).DOI:10.1520/D2779-92R20.2For referenced ASTM standards,visit the ASTM website,www.astm.org,orconta
14、ct ASTM Customer Service at serviceastm.org.For Annual Book of ASTMStandards volume information,refer to the standards Document Summary page onthe ASTM website.Copyright ASTM International,100 Barr Harbor Drive,PO Box C700,West Conshohocken,PA 19428-2959.United StatesThis international standard was
15、developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for theDevelopment of International Standards,Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade(TBT)Committee.1Advisory Committe
16、e onAeronautics)in NACATechnical Note3276(1956)3Their work was extended to include most of thedata published since that time,and extrapolated by semi-empirical methods into regions where no data are available.4.2 The only data required are the density of liquid at 288 K(59F)and the nature of the gas.These are used in theequations,with the specific constant for the gas from Table 1,or with Fig.1,to estimate the Ostwald coefficient.5.Significance and Use5.1 Knowledge of gas solubility is of extrem