Interpretation:
The values of
Concept Introduction:
The formula to calculate enthalpy change of vapor
Value of
Here,
The formula to calculate entropy change of vapor
Value of
Here,
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Loose Leaf For Introduction To Chemical Engineering Thermodynamics
- velocis the air and water. Answer: 0.02605 kgs-1, 61.1 kgm 3, 0.94, 0.822 ms-1, 0.051 ms-1 5. Describe, with the use of sketches, the various two-phase flow regimes that can exist in a horizontal pipe carrying a liquid and a gas. 6. Explate what is mean by gas hold up and describe way which itarrow_forward10. A mixture of high pressure water and steam at a rate of 0.5 kgs-1 flows up a vertical tube with an inside diameter of 25.4 mm at a pres- sure 22 bar. Determine the type of flow if the mass quality is 1%. The density of the water is 845 kgm³, the density of steam is 10.8 kgm³, and the viscosity of the water is 1.24 × 104 Nsm 2. Answer: Slug flowarrow_forward2. Describe, with the use of sketches, the various flow regimes that can exist in a vertical pipe carrying two-phase flow (liquid and gas). •arrow_forward
- 12. A mixture of oil and gas flows through a horizontal pipe with an inside diameter of 150 mm. The respective volumetric flow rates for the oil and gas are 0.015 and 0.29 m³s-¹. Determine the gas void frac- tion and the average velocities of the oil and gas. The friction factor may be assumed to be 0.0045. The gas has a density of 2.4 kgm³ and viscosity of 1 x 10-5 Nsm-2. The oil has a density of 810 kgm-3 and density of 0.82 Nsm-2. Answer: 0.79, 20.8 ms-1, 4 ms-1arrow_forward14. A bubbly mixture of gas and liquid flows up a vertical glass tube with an internal diameter of 25 mm. The liquid flow is controlled to be 0.02 litres per second, and the gas flow is 10 litres per second. The bubble velocity is determined photographically to have a velocity of 30 ms-¹. Determine the gas void fraction for the two-phase mixture and the liquid velocity. Answer: 0.68, 0.13 ms-¹ CLarrow_forward8.9 × 10-4 Nsm-2. Answer: 2.7 kNm²²m-1 4. An experimental test rig is used to examine two-phase flow regimes in horizontal pipelines. A particular experiment involved uses air and water at a temperature of 25°C, which flow through a horizontal glass tube with an internal diameter of 25.4 mm and a length of 40 m. Water is admitted at a controlled rate of 0.026 kgs-¹ at one end and air at a rate of 5 x 104 kgs¹ in the same direction. The density of water is 1000 kgm³, and the density of air is 1.2 kgm³. Determine the mass flow rate, the mean density, gas void fraction, and the superficial velocities of the air and water. Answer: 0.02605 kgs-1, 61.1 kgm-3, 0.94, 0.822 ms-1, 0.051 ms-1arrow_forward
- A 1 μm radius water droplet is settling in paraffin oil. The oil contains an oil-soluble surfactant. The surface dilatational viscosity is 1×104 kg/s. Calculate the settling velocity using the Stokes, Hadamard-Rybczynski and the Boussinesq equations. Compare your results. The density of the oil is 770 kg/m³ and its viscosity is 0.8×10-³ Pa s. Sel Given: The semino velochy v. t the drop is calcula out in a song Rd=1×10-6 m, nath d=1×104 kg/s, Pooib Md=1×10-³ Pa s. S. μ=0.8×10-3 Pas Garing bigit p=770 kg/m³, logo Pd=1000 kg/m³arrow_forward1. Determine the range of mean density of a mixture of air in a 50:50 oil-water liquid phase across a range of gas void fractions. The den- sity of oil is 900 kgm³, water is 1000 kgm³, and gas is 10 kgm³.arrow_forward9. Characterise the main concepts of a homogeneous flow model, sepa- rated flow models, and specific flow pattern models. 10 A mixture of high pressure water and steam at a rate of 0.5 kgs-1 hows up a vertical tube with an inside diameter of 25.41 at pres- sure 22 bai. Determine the type of flow if the mass quality is 1%. Thearrow_forward
- Subject: Engineering Foundation Class: Fourth AL-Mansour University College Civil Engineering Department Monthly Exam اسم الطالبة Date: 12/11/2024 Time: 1.5 hrs Lec: Dr. Lubna Abrahman Answer ALL questions Q1: Standard penetration tests were carried out in normally consolidated fine sands at different locations. The following data were collected, with average unit weights assumed for the entire depth. Determine the (N)60 values using the cor- rection factors proposed by (a) Liao and Whitman (1986) and (b) Skempton (1986). Liao and Whitman's relationship (1986): 705 Depth (m) Average unit weight (kN/m²) N 3.5 18.0 8.8 18.0 12.4 18.5 18.5 18.5 23.6 19.0 21 16.9 19.0 285922 12 15 19 26 26 Skempton's relationship (1986): 2 CN- 1+ blearrow_forward100 kmol/h of a stream containing 20 mol% CO, 20 mol% H₂O, and 60 mol% H2 is combined with additional steam and fed to a water-gas shift reactor to produce more hydrogen according to the reaction: CO+H,O—CO,+H2 The equilibrium constant of the water-gas shift reaction is 200, and the mole fraction of hydrogen at the outlet is 0.75. Write and balance the www.EngineeringBooksPdf.com erial Balances on Reactive Systems 181 chemical equation. How much additional steam is fed to the water- gas shift reactor? (5.1 kmol/h)arrow_forward1/2 Apg R₁ = 2R qo 3yarrow_forward
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