Please solve clearly and handwritten with steps pls ... Here n=5 .How much heat and moisture is removed in the process is shown below. Thevolume flow rate at state 1 is (10+n) 'n' = question number. Write thesolution step by step. Make sure to present your solutions clearly and legibly.(Example: If question number is 2, n = 2)mamin2T₂ =15°C₂ = 100%Cooling coilselllllllllllll14°CCondensateremovalAirCondensate1T₁=28°C₁ = 80%

Answered: Image /qna-images/answer/0933bccf-06bc-4782-af2a-231e74a70686.jpg

.How much heat and moisture is removed in the process is shown below. volume flow rate at state 1 is (10+n) m 'n' = question number. Write solution step by step. Make sure to present your solutions clearly and legi (Example: If question number is 2, n = 2) min Cooling coils Telllllllllllll eeeet Air+

.How much heat and moisture is removed in the process is shown below. volume flow rate at state 1 is (10+n) m 'n' = question number. Write solution step by step. Make sure to present your solutions clearly and legi (Example: If question number is 2, n = 2) min Cooling coils Telllllllllllll eeeet Air+

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

See similar textbooks

Similar questions

8. The exact differential equation of enthalpy can be expressed as below: dH=-uCpdp + C₂dT where C: constant pressure heat capacity u: Joule-Thomson coefficient μl= a) Derive the exact differential equation of enthalpy from the general exact differential equation of enthalpy: = (3), dp + (7) dr T dH = b) Considering that you use nitrogen gas to make a temperature drop to an isenthalpic system, how much pressure drop is required to cool the system by 20 K? The Joule-Thomson coefficient of nitrogen is u 3 0.27 K atm¹. c) Prove that the Joule-Thomson expansion can occur without change of enthalpy (isenthalpic process).
b) The high pressure units on a steam plant operate at 10bar (gauge), and the condensate is sub-cooled by 9.5K. If the mass flow rate of condensate is 10 kg/s, use the provided steam tables to determine how much saturated steam at 1.5 bar this condensate could produce. Note it is sufficiently accurate for high pressure condensate, as in this question, to assume that the specific enthalpy is the same as for the saturated liquid at the same temperature.
Homwork-6.png Homework-6 P.1 Calculate the dryness fraction (quality) of steam which has 1.5 Kg of water in suspension with 50 Kg of steam? A vessel having a volume of 0.05 m contains a mixture of saturated water and saturated steam at a temperature of 245 ° C. The mass of liquid present is 10 Kg. P.2 Find the following: (a) The pressure. (b) The mass. (c) The specific volume. (d) The specific enthalpy (e) The specific entropy. (f) The specific internal energy.
PLEASE SHOW SOLUTION AND PROVIDE RESOURCES THANK U 1.What is the state of a water vapor at dew point temperature and dry-bulb temperature?(use the psychometric chart to determine the state of the steam)
T,"c -8 30 100 вкра 500 770.64 326 600 v₁ m²/kg 0.0007571 0.022 0063604. 0.002630 Phase description table for refrigerant-134a: CSI สแกนด้วย CamScanntr Saturated vipa verpe
500 kilograms of dressed chicken enter a chiller at 10°C are frozen and chilled to a final temperature of -15°C for storage in 20 hours. Compute the product load.Specificheat above freezing............3.2 kJ/kg-°KSpecific heat below freezing............1.6 kJ/kg-°KLatent heat...........250 kJ/kgFreezing Temperature.......... -5°CA. 2.18 kwB. 6.67 kwC. 3.67 kwD. 7.67 kw
A test on a single cylinder, four stroke oil engine having a bore of 15cm and stroke 30 cm gave the following results: speed 300 rpm, brake torque 200 Nm, indicated mean effective pressure 7 bar, fuel consumption 2.4 kg/h, air fuel ratio 22, room temperature 20°C and pressure at 1 bar. The fuel has a calorific value of 42 MJ/kg and contains of 15% by weight of hydrogen. Calculate: i. indicated thermal efficiency ii. volumetric efficiency
3- Consider a counterflow heat exchanger that must cool 3000 kg/h of mercury from 150°F to 128°F. The coolant is 100 kg/h of water, supplied at 70°F. If U is 300 W/m²K, complete the design by determining reasonable value for the area and the exit-water temperature. [A = 0.147 m2.] %3D
Problem 2 An Air Force Research Lab engineer is asked to evaluate the maximum theoretical work that could be produced by the first stage turbine section of an experimental jet engine. Test stand measurements provide the following information: a. Entering air conditions: 1400 K, 8 bar b. Exiting air conditions: .8 bar Part 1: Since you don't have a mass flow rate measurement, what will be the units will you report maximum theoretical work in? Part 2: Write the first law equation for your control volume showing all terms. What assumptions will you make to simplify the equation. Part 3: Pin down the outlet state on a notional T-s diagram for air (just show the two isobars). Why did you select this point? Part 4: What assumption about the properties of air will you make in order to solve this problem? Part 5: Use the appropriate form of the 'Tds' equation and the air tables to solve for the exit state. Part 6: Calculate the max theoretical work
Required information Problem 03.100 - DEPENDENT MULTIPART PROBLEM - ASSIGN ALL PARTS NOTE: This is a multi-part question. Once an answer is submitted, you will be unable to return to this part. A 1-m tank contains 2.3019 kg of steam at 0.6 MPa. The gas constant, the critical pressure, and the critical temperature of steam are R=0.4615 kPa-m/kg-K, Ter = 6471 K, and Per = 22.06 MPa. Use data from the steam tables. Problem 03.100.b - Van der Waals final temperature Determine the temperature of the steam using the van der Waals equation. (You must provide an answer before moving to the next part) The temperature is K.
How is the Limit State Design applied?
Steam leaves an industrial boiler at 645.3kPa and 151.2°C. A portion of the steam is fed through a throttling calorimeter and released to the atmosphere when the calorimeter pressure exceeds 104.3kPa. If the calorimeter's steam temperature is 113.8°C, a. What is the amount of moisture that is escaping from the boiler container? Show unit analysis & conversion. b. Calculate the mass of the saturated vapor if the mass of the saturated liquid is 15kg. Show unit analysis & conversion. @645.3kPa and 151.2°C: hf = 624.56kJ/kg hfg =2123.3kJ/kg @104.3kPa and 113.8°C: h2=2506.7kJ/kg