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API data book

API Data Book, Vapor Pressure Section, 1986 edition. [Pg.33]

Adiabatic flash calculation Liquid and vapor enthalpies off charts in the API data book are fitted with linear equations... [Pg.378]

In the discussion appendix of the original paper by Carson and Katz (1942), Hammerschmidt indicated that, while the method was acceptable for gases of normal natural gas composition, an unacceptable deviation was obtained for a gas rich in ethane, propane, and the butanes. More work is also required to revise the Kvs -value charts for two components, namely, carbon dioxide and nitrogen. In three-phase hydrate data for binary mixtures of carbon dioxide and propane, Robinson and Mehta (1971) determined that the Kvs method for carbon dioxide gave unsatisfactory results. The API Data Book shows the Kvs values for nitrogen to be only a function of pressure, without regard for temperature Daubert (Personal... [Pg.220]

At this point, it is important to present a disclaimer. Many notable engineers could claim the author is loco to think he can resolve all database needs with only the eight physical properties given or otherwise derived in this book. Let me quickly state that many other extended database resources are indeed referenced in this book for the user to pursue. Only in such retrieval of these and many other database resources, such as surface tension and solubility parameters, can PPE be applied. An example is that surface tension and solubility parameters must both be determined before the liquid/liquid software program given herein can be applied. This liquid-liquid extraction program (Chemcalc 16 [1]) is included as part of the PPE presentation. (See Chap. 7.) It is therefore important to keep in mind that many database references are so pointed to in this book—Perry s, Maxwell s, and the American Petroleum Institute (API) data book, to name a few. [Pg.2]

From the API data book and a heat of cracking of 332Btu/(lb gas + gasoline) ... [Pg.212]

K values from company files, API data book, GPS A data book, etc. [Pg.982]

You will need to use a vapor-pressure chart for this calculation. One source is your API Data Book (American Petroleum Institute). [Pg.70]

American Petroleum Institute (API) Data Books, www.api.org. American Petroleum Institute, New York. Vapor Pressure of Normal Paraffin Technical Data Book, Ch. 5, P. 5A1.1,1970. [Pg.687]

The physical properties of the fluids being processed can be studied and calculated by the methods of Edmister (2) and Maxwell (3). The API Data Book (4)... [Pg.78]


See other pages where API data book is mentioned: [Pg.2]    [Pg.218]    [Pg.372]    [Pg.90]    [Pg.2]    [Pg.218]    [Pg.372]    [Pg.2]    [Pg.5]    [Pg.218]    [Pg.372]    [Pg.2]    [Pg.218]    [Pg.372]    [Pg.19]    [Pg.329]    [Pg.90]   
See also in sourсe #XX -- [ Pg.144 ]




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