Tech Manual for Erjavec's Automotive Technology: A Systems Approach
Tech Manual for Erjavec's Automotive Technology: A Systems Approach
6th Edition
ISBN: 9781133933731
Author: ERJAVEC, Jack, Thompson, Rob
Publisher: Delmar Cengage Learning
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Chapter 10, Problem 12RQ

Which of the following is not considered part of the organic soil grouping?

  1. Petroleum by-products derived from crude oil, including tar, road oil, engine oil. gasoline, diesel fuel, grease, and engine oil additives

  • Rust that is a product of coolant and aluminum
  • By-products of combustion, including carbon, varnish, gum, and sludge
  • Coatings, including such items as rust-proofing materials, gasket sealers and cements, paints, waxes, and sound-deadener coatings
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    Problem 1) A fractional factorial design has been used to study on the effect of 3 parameters including adsorbent concentration (300 and 500 ppm), pH value (4 and 10) and reaction time (6 and 12 hours) on the adsorption capacity of a composite for removing of methylene blue from a wastewater. If the results obtained for two repetitions of the tests are according to the following table, it is desirable: A) Design Resolution Y₁ Y₂ Run (mg/g) (mg/g) B) Drawing graphs of the effect of each parameter on the adsorption capacity 1 28 26 2 36 34 C) Analysis of interactions 3 18 20 D) Calculate the effects percentage of each parameter and error 4 32 30 E) Determining the optimum conditions to achieve the highest adsorption capacity
    Thermophysical Properties of Petroleum Fractions and Crude Ofls 67 3.4. A gas oil has the following TBP distillation data Volume % TBP (°C) 0 216 10 243 30 268 50 284 70 304 90 318 95 327 100 334 It also has an average boiling point of 280 °C and an average density of 0.850 g/cm³. (a) Split this gas oil fraction into five pseudo-components. Calculate T., Pc and w for each pseudo-component. (b) Calculate T, Pc and w for the whole gas oil fraction. (c) Calculate the enthalpy of this gas oil fraction at 400 °C using the Lee- Kessler correlation with a reference state of ideal gas at 273.15 K.
    3.3. Use the following crude assay data with crude API of 36 to estimate cut vol%, critical properties and molecular weight for Light Naphtha (90- 190 °F) and Kerosene (380-520 °F). In addition, calculate the fractions of paraffins, naphthenes and aromatics in the two cuts. ASTM D86 (°F) Volume % Cum vol% SG 86 0.0 0.0 122 0.5 0.5 0.6700 167 1.2 1.7 0.6750 212 1.6 3.3 0.7220 257 2.7 6.0 0.7480 302 3.1 9.1 0.7650 347 3.9 13.0 0.7780 392 4.7 17.7 0.7890 437 5.7 23.4 0.8010 482 8.0 31.4 0.8140 527 10.7 42.1 0.8250 584 5.0 47.1 0.8450 636 10.0 57.1 0.8540 689 7.8 64.9 0.8630 742 7.0 71.9 0.8640 794 6.5 78.4 0.8890 20.8 99.2 0.9310
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