
A)
Interpretation:
Change in internal energy of the system at constant pressure and reduced temperature.
Concept introduction:
Thermodynamic property tables is provide the data about pressure, temperature, , specific enthalpy and entropy and specific volume at particular saturation pressure or saturation temperature or both are combined in superheat condition.
The change in internal energy of the system.
Here, the mass of steam is M.
B)
Interpretation:
Change in internal energy of the system at constant pressure and increase in temperature.
Concept introduction:
Thermodynamic property tables:
Thermodynamic property tables is provide the data about pressure, temperature, , specific enthalpy and entropy and specific volume at particular saturation pressure or saturation temperature or both are combined in superheat condition.
The change in internal energy of the system:
Here, the mass of steam is M.

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Chapter 1 Solutions
EBK FUNDAMENTALS OF CHEMICAL ENGINEERIN
- The energy release (Q_g) and energy loss (Q_r) curves of an irreversible oxidation reaction are shown below. Q_r curves can be shifted by adjusting the feed temperature. Q,& QE E Qg (a) Are these points of intersection between energy release and energy loss curves stable operating conditions? Point of Intersection A Stable or Unstable B A D T (b) Which point represents the ignition condition? B с D E F Garrow_forwardProblem 1. For an irreversible liquid phase reaction 2A -> B, the reaction rate is of the 2nd order with respect to the reactant concentration CA. The concentration-dependent reaction rate is plotted below. This reaction is performed in a cascade of two identical CSTRS (same reactor size and temperature). The inlet concentration of A of the 1st CSTR is 2 mol/L. The outlet concentration of A of the 2nd CSTR is 1 mol/L. The inlet flow rate of the 1st reactor is 100 L/h. Please use the graphical method to determine the outlet concentration of A of the first CSTR and the size of each CSTR. Please briefly show the procedure for reactor size calculation. (-4-7) 15225050 45 40 35 30 0 0.5 11.761.5 C₂ Q C (mol.L¹) Co 20 2.5arrow_forward15.15 A 0.20-m-thick brick wall (k = 1.3 W/m K) separates the combustion zone of a furnace from its surroundings at 25°C. For an outside wall surface temperature of 100°C, with a convective heat-transfer coefficient of 18 W/m² K, what will be the inside wall surface temperature at steady-state conditions? .arrow_forward
- An MF membrane has pore-size distribution as follows: d(pore)0.33 fraction¼ 1.5 mm, d(pore)0.33 fraction¼ 1.0 mm, and d(pore)0.33 fraction¼ 0.5 mm. Required (a) Determine the distribution of flux density for each pore size. (b) Show by a plot the distribution of pore sizes and the distribution of flux density. solvearrow_forwardPlease show me your steps please thank you.arrow_forwardPlease show your work thanks.arrow_forward
- A pipe 1.2 m diameter and 20 km long transmits water of velocity of 2 m/s. The friction coefficient of pipe is 0.007. Calculate the head loss due to friction?arrow_forwardA gas pipeline, NPS 20 with 0.500 in. wall thickness, transports natural gas (specific gravity = 0.6) at a flow rate of 250 MMSCFD at an inlet temperature of 60°F. Assuming isothermal flow, calculate the velocity of gas at the inlet and outlet of the pipe if the inlet pressure is 1000 psig and the outlet pressure is 850 psig. The base pressure and base temperature are 14.7 psia and 60°F, respectively. Assume compressibility factor Z = 1.00. What is the erosional velocity for this pipeline based on the above data and a compressibility factor Z = 0.90?arrow_forwardH.W.1 : The elementary liquid phase reaction A + BR + S is conducted in a setup consisting of a mixed reactor, into which two reactant solutions are introduced, followed by a plug flow reactor. The component B is used in a large excess so that the reaction is first order with respect to A. Various ways to increase the production rate are suggested, one of which is to reverse the order of these units. How would this change/affect conversion?arrow_forward
- H.W.2 : The kinetics of the liquid phase decomposition of A is studied in two mixed flow reactors in series, the second unit having twice the volume of the first one. At steady state with a feed with CA, = 1 mol/l and mean residence time of 96 s in the first reactor, the concentration of A in the first unit (reactor) is 0.5 mol/l and in the second is 0.25 mol/l. Find the rate equation for the decomposition of A.arrow_forwardA natural gas consists of the following molar composition: C1 = 0.871, C2 0.084, C3 = 0.023, CO2 = 0.016 and H2S = 0.006. Calculate the gas gravity to airarrow_forward8 9:07 D Asiacell من تدوير العجلة. إستمر في إستخدام تطبیق آسياسيل للحصول على المزيد من العروض المميزة! الأحد، ١٦ مارس إنتهت صلاحية الإنترنت التي تلقيتها من تدوير العجلة. إستمر في إستخدام تطبیق آسياسيل للحصول على المزيد من العروض المميزة! الاثنين، ۱۷ مارس 1000 د ارسلت من ر رصيدك الى 7707268140 في 2025/03/17. 350 د تم إستقطاعها من رصيدك لهذه العملية 8000 د ارسلت من رصيدك الى 7707268140 في 2025/03/17. 350 د تم إستقطاعها من رصيدك لهذه العملية Vol) Voi) ٨:٥٤ ص ٢:١٤ ص ٩:٥٢ م 29:07 III =arrow_forward
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