Page 27 - The engineering of chemical reactions
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M o d e l i n g  1 1

                             TABLE l-3
                             Top 50 Chemicals*
                             Rank       Chemical       Billions of lb  Rank   Chemical     Billions of lb
                              1     Sulfuric acid         89.20     26     Ethylene oxide     6.78
                             2      Nitrogen              67.54     27     Toluene            6.75
                             3      Oxygen                67.54     28     Hydrochloric acid  6.71
                             4      Ethylene              49.67     29     p-Xylene           6.23
                             5      Lime                  48.52     30     Ethylene glycol    5.55
                             6      Ammonia               38.35     31     Cumene             5.16
                             7      Propylene             37.93     32     Ammonium sulfate   5.08
                             8      Sodium hydroxide      25.83     33     Phenol             4.05
                             9      Phosphoic  acid       25.26     34     Acetic acid        3.82
                             10     Chlorine              24.20     35     Propylene oxide    3.70
                             11     Sodium carbonate      20.56     36     Butadiene          3.40
                             12     Ethylene dichloride   18.70     37     Carbon black       3.31
                             13     Nitric acid           17.65     38     Potash             3.14
                             14     Ammonium nitrate      17.61     39     Acrylonitrile      3.08
                             15     Urea                  16.13     40     Vinyl acetate      3.02
                             16     Vinyl chloride        14.81     41     Acetone            2.77
                             17     Benzene               14.66     42     Titanium dioxide   2.74
                             18     Methyl-tert butyl  ether  13.67  43    Aluminum sulfate   2.30
                             19     Ethylbenzene          11.87     44     Sodium silicate    2.13
                             20     Styrene               11.27     45     Cyclohexane        2.11
                             21     Carbon dioxide        10.99     46     Adipic acid        1 .X0
                             22     Methanol              10.81     47     Caprolactam        1.68
                             23     Xylene                9.06      48     Bisphenol A        1.48
                             24     Terephthalic acid     8.64      49     n  Butyl alcohol   1.45
                             25     Formaldehyde          7.94      50     Isopropyl alcohol  1.39
                             *Data for 1994, from Chemical and Engineering News


                             pressures can change. We will mention these complications but seldom solve problems
                             without assuming constant density.
                                  On the other hand, we will be downright sloppy about dimensions of quantities,
                             frequently switching between English engineering and metric units. This is because one
                             important task of the chemical engineer is in  language translation  between technical and
                             nontechnical people, be they managers or customers. In U.S. industry you will hear amounts
                             in pounds or tons, temperatures in degrees Fahrenheit, and pressures in psi gauge almost
                             exclusively, with many practicing engineers not even knowing the meaning of kilograms,
                             kelvins, and pascals.  We will refer to energies in calories, power in watts, and amounts of
                             material in gram moles, pounds, and tons without apology. Volumes in liters, cubic feet, or
                             gallons and lengths in centimeters or miles must be handled without effort to effectively
                             communicate with one’s colleagues.
                                  However, two types of systems are sufficiently important that we can use them almost
                             exclusively: (1) liquid aqueous solutions and (2) ideal gas mixtures at atmospheric pressure.
                             In aqueous solutions we assume that the density is 1 g/cm3,  the specific heat is 1 Cal/g  K,
                             and at any solute concentration, pressure, or temperature there are -55 moles/liter of water.
                             In gases at one atmosphere and near room temperature we assume that the heat capacity per
                             mole is i R, the density is l/22.4  moles/liter, and all components obey the ideal gas equation
                             of state. Organic liquid solutions have constant properties within  w-20%,  and nonideal  gas
                             solutions seldom have deviations larger than these.
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