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                                           2. CHARACTERIZATION AND PROPERTIES OF PURE HYDROCARBONS 37
            1. API: Technical Data Book—Petroleum Refining [2]. The first
              chapter of API-TDB compiles basic properties of more than  sources for physical property data (http://tigger.uic.edu/
                                                                    ∼mansoori/Thermodynamic.Data.and.Property-html/).
              400 pure hydrocarbons and some nonhydrocarbons that
              are important in petroleum refining. For some compounds  In many occasions different sources provide different values
              where experimental data are not available, predicted values  for a particular property depending on the original source
              from the methods recommended by the API are given.  of data. Calculated properties such as critical constants and
            2. DIPPR: Design Institute for Physical and Property Data  acentric factor for compounds heavier than C 18 should be
              [19]. The project initially supported by the AIChE began in  taken with care as in different sources different methods have
              early 1980s and gives various physical properties for both  been used to predict these parameters.
              hydrocarbon and nonhydrocarbon compounds important
              in the industry. A computerized version of this data bank is  2.2.2 Properties of Selected Pure Compounds
              provided by EPCON [20].
            3. TRC Thermodynamic Tables—Hydrocarbons [21]. The    The basic properties of pure hydrocarbons from different
              Thermodynamic Research Center (formerly at the Texas  groups that will be used in the predictive methods presented
              A&M University) currently at the National Institute of Stan-  in the following chapters are tabulated in Tables 2.1 and 2.2.
              dards and Technology (NIST) at Boulder, CO, (http://www.  The basic properties of M, T M , T b , SG, d 20 , n 20 , T c , P c , V c , Z c ,
              trc.nist.gov/) in conjunction with the API Research Project  and ω are presented in Table 2.1. Secondary properties of kine-
              44 [22] has regularly published physical and basic proper-  matic viscosity, API gravity, K W , vapor pressure, aniline point,
              ties of large number of pure hydrocarbons.          flash and autoignition points, flammability range, and oc-
                                                                                                                  --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
            4. API Research Project 44 [22]. This project sponsored by the  tane number are given in Table 2.2. Compounds selected are
              API was conducted at Texas A&M University and provides  mainly hydrocarbons from paraffins, naphthenes, and aro-
              physical properties of selected hydrocarbons.       matics that constitute crude oil and its products. However,
            5. API Research Project 42 [18]. This data compilation com-  some olefinic and nonhydrocarbons found with petroleum
              pleted in the 1960s provides experimental data on den-  fluids are also included. Most of the compounds are from ho-
              sity, refractive index, viscosity, and vapor pressure for  mologous hydrocarbon groups that are used as model com-
              more than 300 hydrocarbons with carbon number greater  pounds for characterization of petroleum fractions discussed
              than C 11 .                                         in Chapter 3. The properties tabulated are the basic prop-
            6. Dortmund Data Bank (DDB) [23]. This project on physical  erties needed in characterization techniques and thermody-
              properties has been conducted at the University of Olden-  namic correlations for physical properties of petroleum frac-
              burg in Germany. DDB contains experimental data from  tions. Although there are separate chapters for estimation of
              open literature on various thermodynamic properties of  density, viscosity, or vapor pressure, these properties at some
              pure compounds and some defined mixtures. Data have  reference temperatures are provided because of their use in
              been programmed in a computer software convenient for  the characterization methods given in Chapter 3 and 4. Other
              extracting data. Majority of data are on thermodynamic  physical properties such as heat capacity or transport prop-
              properties, such as vapor–liquid equilibrium (VLE), activ-  erties are given in corresponding chapters where the predic-
              ity coefficients, and excess properties. However, data on  tive methods are discussed. Data for more than 100 selected
              viscosity, density, vapor pressure, thermal conductivity, and  compounds are presented in this section and are limited to
              surface tension have also been complied as mentioned in  C 22 mainly due to the lack of sufficient experimental data for
              their Web site. Unfortunately they have not compiled char-  heavier compounds. Data presented in Tables 2.1 and 2.2 are
              acteristic data on hydrocarbons and petroleum fractions  taken from the API-TDB [2, 22]. Standard methods of mea-
              important in the petroleum industry. Also the data on trans-  surement of these properties are presented in Chapter 3.
              port properties are mainly for pure compounds at atmo-
              spheric pressures.                                  Example 2.2—Assume large amount of toluene is poured on
            7. The fourth and fifth editions of The Properties of Gases  the ground in an open environment at which the temperature
                                                                     ◦
                                                                           ◦
              and Liquids [4] also provide various properties for more  is 38 C (100 F). Determine if the area surrounding the liquid
              than 400 pure compounds (hydrocarbons and nonhydro-  surface is within the flammability range.
              carbons). However, data in this book have been mainly
              taken from the TRC Tables [21].                     Solution—From Table 2.2, the flammability range is 1.2–7.1
            8. There are also some free online sources that one may use to  vol% of toluene vapor. From this table, the vapor pressure of
              obtain some physical property data. The best example is the  toluene at 38 C is 0.071 bar (0.07 atm). Substituting this vapor
                                                                            ◦
              one provided by NIST (http://webbook.nist.gov). Various  pressure value in Eq. (2.11) gives the value of vol% = 100 ×
              universities and researchers have also developed special on-  0.07/1.0 = 7% of toluene in the air mixture. This number is
              line sources for free access to some data on physical proper-  within the flammability range (1.2 < 7 < 7.1) and therefore
              ties. For example the Center for Research in Computational  the surrounding air is combustible.
              Thermochemistry (CRCT) of Ecole Ploytechnique Mon-
              treal provides online calculational software at http://www.  2.2.3 Additional Data on Properties
              crct.polymtl.ca/fact/index.php/. The Center for Applied  of Heavy Hydrocarbons
              Thermodynamic Studies (CATS) at the University of Idaho
              also provides softwares for property calculations at its web-  Some data on density, refractive index, and viscosity of some
              site (http://www.webpages.uidaho.edu/∼cats/). G. A. Man-  heavy hydrocarbons are given in Table 2.3. These data are
              soori in his personal Web site also provides some online  taken from API RP 42 [18]. Values of R i and VGC in the table















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