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8 The inside of the card is on the second page The left inside panel is the left column, and the right inside panel is the right column Enter text and images as necessary to lay out the card you want to create 9 When you re done, you ll need to print your card manually so that it doesn t print the second page of the document on a second sheet of paper To do that, you have two choices:

(d) n-Pentane:

( e ) Toluene:

Operator overloading is a useful tool, and I have grown especially fond of the CType overload. Let s add a CType overload to a class we first designed back in 8: ListItemData. This class exposes both ItemText and ItemData properties, providing access to the textual and numeric aspects of the class content. Its primary purpose is to support the tracking of ID numbers in ListBox and ComboBox controls. If we need to know the ID number of a selected item in a ListBox control (let s name it SomeList), we use code similar to the following:

If you re printing on an inkjet printer, make sure you wait for the first side to dry before turning the paper over and printing the second side See 15 for more information on printing

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413 A method for determination of the second virial coefficient of a pure gas is based on the Clapeyron equation and measurements of the latent heat of vaporization A HI^, the molar volume of saturated liquid v l , and the vapor pressure P Sat Determine B in cm3 mol-' for methyl ethyl ketone at 34815 K (75 C) from the following data at this temperature:

414 One hundred kmol per hour of subcooled liquid at 300 K and 3 bar is superheated to 500 K in a steady-flow heat exchanger Estimate the exchanger duty (in kW) for one of the following: (a) Methanol, for which T Sat = 3680 K at 3 bar (b) Benzene, for which T Sat = 3923 K at 3 bar (c) Toluene, for which T Sat = 4269 K at 3 bar

There s nothing wrong with that code. But I thought, Wouldn t it be nice to convert the ListItemData instance to an Integer using the CInt function, and not have to mess with member variables like ItemData

415 Saturated-liquid benzene at pressure P, = 10 bar (TIsat= 4517 K) is throttled in a steady-flow process to a pressure P2 = 12 bar (TzSat= 3587 K), where it is a liquidhapor mixture Estimate the molar fraction of the exit stream that is vapor For liquid benzene, Cp= 162 J mold' K-l Ignore the effect of pressure on the enthalpy of liquid benzene

Equipped with Microsoft Publisher or a similar page layout program, you can create professional and attractive newsletters for the office, family, or your club or organization Publisher comes in most versions of Microsoft Office, and I highly recommend it for generating your own newsletters (as well as business cards and other projects) Publisher is a wizard-based program All you have to do is follow the directions to set up the overall look and feel of your document, and then fill in the text and replace the placeholder images with your own pictures

for one of the following compounds as a liquid at 29815 K (25 C) 416 Estimate (a) Acetylene, (b) 1,3-Butadiene, (c) Ethylbenzene, (d) n-Hexane, (e) Styrene

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417 A reversible compression of 1 mol of an ideal gas in a piston/cylinder device results in a pressure increase from 1 bar to P2and a temperature increase from 400 K to 950 K The path followed by the gas during compression is given by

418 Hydrocarbon fuels can be produced from methanol by reactions such as the following, which yields 1-hexene:

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Compare the standard heat of combustion at 29815 K (25 C) of 6CH30H(g) with the standard heat of combustion at 29815 K (25 C) of C6H12(g) reaction products for C02(g) and H20(g)

Dim recordID As Integer = _ CInt(CType(SomeList.SelectedItem, ListItemData))

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