API MPMS 11.3.2.1-2013 Manual of Petroleum Measurement Standards Chapter 11.3.2.1 Ethylene Density (Second Edition)《石油计量标准手册.第11.3.2.1章 乙烯密度》.pdf

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1、Manual of PetroleumMeasurement StandardsChapter 11.3.2.1Ethylene DensitySECOND EDITION, MAY 2013Special NotesAPI publications necessarily address problems of a general nature. With respect to particular circumstances, local, state, and federal laws and regulations should be reviewed.Neither API nor

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14、e director.Generally, API standards are reviewed and revised, reaffirmed, or withdrawn at least every five years. A one-time extension of up to two years may be added to this review cycle. Status of the publication can be ascertained from the API Standards Department, telephone (202) 682-8000. A cat

15、alog of API publications and materials is published annually by API, 1220 L Street, NW, Washington, DC 20005.Suggested revisions are invited and should be submitted to the Standards Department, API, 1220 L Street, NW, Washington, DC 20005, standardsapi.org.iiiContentsPage1 Scope . . . . . . . . . .

16、. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12 Normative References. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

17、 . . 13 Terms and Definitions. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14 Ethylene Equations of State. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

18、 . . . . . . . . . . . . 14.1 General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14.2 IUPAC-88 Equation of State . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

19、. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25 Implementation Procedures . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3Bibliography . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

20、 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4vIntroductionThe purpose of this standard is to provide an equation of state that can be used to obtain an accurate determination of ethylene density. Other thermodynamic properties can be calculated using

21、the equation of state, but this standard is primarily concerned with the determination of ethylene density. Temperature and pressure can have significant effects on the accurate determination of ethylene density, and as a result, the means for temperature and pressure determination have to be assess

22、ed appropriately for these applications. The previous edition of this standard, published in 1974, was in the form of a measurement manual and was not confined to calculating the physical properties of ethylene. The previous edition included orifice and turbine metering calculations, as well as data

23、 that were not in agreement with the current API Manual of Petroleum Measurement Standards (MPMS) that cover these metering devices. The original density lookup tables were based on FORTRAN code originally published in the mid-1960s as API 2565 Subroutine Ethyl. This Second Edition of API MPMS Chapt

24、er 11.3.2.1 is intended to replace the 30+ year old equations with references to more modern equations of state, limited to the physical properties of ethylene.Typically, ethylene equations of state are used in custody transfer metering applications. Such is the case with modern flow computers, whic

25、h have various options for selecting which equation of state is utilized in determining flowing ethylene density. vi1Ethylene Density1 ScopeThis standard identifies an equation of state (EOS) suitable for use in custody transfer measurement of pure ethylene (99 %) in the gaseous, liquid, and super c

26、ritical phases. Given flowing temperature and pressure, an EOS is capable of calculating density and other thermodynamic properties used to calculate mass and volumetric flow of ethylene to custody transfer accuracy. All accuracy and uncertainty statements in this standard are limited to the EOS res

27、ults and do not include the uncertainty added by the primary and secondary measuring equipment. 2 Normative ReferencesThe following referenced documents are indispensable for the application of this document. For dated references, only the edition cited applies. For undated references, the latest ed

28、ition of the referenced document (including any amendments) applies.IUPAC-88 1, Ethylene (Ethene), International Thermodynamic Tables of the Fluid State, Volume 10 (1988)3 Terms and DefinitionsFor the purposes of this document, the following definitions apply.3.1critical regionThermodynamic state of

29、 a fluid in which phase boundaries cease to exist. NOTE In the case of ethylene, a vapour-liquid critical region exists. Density determination is extremely sensitive in the critical region, as minor changes in flowing pressure can bring about significant changes in density for a given temperature.3.

30、2equation of stateEOSThermodynamic equation describing the state of matter under a given set of physical conditions.NOTE An EOS provides a mathematical relationship between two or more state functions associated with the material, such as its temperature or pressure. 4 Ethylene Equations of State4.1

31、 GeneralThis standard provides a reference for an ethylene EOS: IUPAC-88, part of the Ethylene, International Thermodynamic Tables of the Fluid State, Volume 10 (1988) publication.IUPAC-88 is a publication that incorporates the work carried out by Jahangiri et al. 1 on ethylene. The paper “Thermodyn

32、amic Properties of Ethylene from the Freezing Line to 450 K at Pressures to 260 MPa” was published a year or so before IUPAC published lookup tables in 1988. 1International Union of Pure and Applied Chemistry, 104 T.W. Alexander Drive, Building 19, Research Triangle Park, North Carolina 27709, www.i

33、upac.org.2 API MPMS CHAPTER 11.3.2.1The IPUAC EOS is acceptable for use in custody transfer applications. However, the user should be aware that a critical region for ethylene exists across pressures ranging approximately from 5171.1 kPa to 5860.5 kPa (750 psig to 850 psig) and temperatures ranging

34、approximately from 10 C to 21.1 C (50 F to 70 F). Density predictions using the IUPAC EOS are not recommended in this region. For the IUPAC-88 density prediction, the estimated uncertainty of the EOS is less than 0.08 % for pressures up to 260 MPa (65,266.9 psig) and temperatures up to 176.85 C (350

35、.3 F), with the exception of the critical region. 4.2 IUPAC-88 Equation of StateThe paper by Jahangiri et al. 1 is the basis for the IUPAC-88 EOS. According to the paper, the Helmholtz energy for ethylene is given below by the fundamental equation:(1)where is the ideal gas contribution to the Helmho

36、ltz energy of any state. The term is the contribution represented by the compressibility of the real gas. After additional manipulation, the functional form used for the fundamental equation for ethylene is a nondimensional Helmholtz energy potential function below: (2)where(3)wherecis the critical

37、density;Tcis the critical temperature;T0is the reference temperature 298.15 K;P0is the reference pressure 0.101525 MPa;0is the ideal gas density at T0and P0;is the reference enthalpy at T0;is the reference entropy at T0and P0;R is the gas constant 0.00831434 (MPa dm3)/(mol K). Given the equations ab

38、ove, it is possible to derive functions for calculating properties of ethylene such as density. The equations and procedures described in Section 5.4 of Jahangiri et al.s paper illustrate how density can be calculated from the methods above. A T,()AT,()A T,()+=AT,()A T,() ,()A T,()R T ,(),()+=H0RTc-

39、S0R- 100-R-Cp2-0d1R-Cp-0d+ln+= TcT 0, TcT0, c0, 0c=H0S0ETHYLENE DENSITY 35 Implementation ProceduresTo properly implement an ethylene EOS, the user should follow the implementation procedures in the IUPAC-88 publication. Through mathematical manipulation it is possible to derive a form in terms of d

40、ensity, pressure and temperature. However, it is recognized that tolerances for solutions and validation procedures are not provided in the publication itself. To maintain industry consistency, a technical report will be issued separate of this standard providing guidance on how to perform the calcu

41、lations. Ultimately though, the end use for an ethylene EOS will determine the procedures of implementation. In some custody transfer applications, programming support could be required to implement the proper code for each EOS. In other custody transfer applications, the EOS could already be in a c

42、ompiled form and available for use. An example of this would be the use of an ethylene EOS in flow computing applications to determine mass flow rate. Example and auxiliary calculations are presented in the individual publication IUPAC-88.4Bibliography1 Majid Jahangiri, Richard T. Jacobsen, and Rich

43、ard B. Stewart, “Thermodynamic Properties of Ethylene from the Freezing Line to 450 K at Pressures to 260 MPa,” Journal of Physical and Chemical Reference Data(1986), Vol. 15, No. 2, 1986API MonogramLicensing ProgramSales: 877-562-5187(Toll-free U.S. and Canada)(+1) 202-682-8041(Local and Internatio

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