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Cubic section

1. If the tube inside diameter is 0.300 in., find a for the tube-side flow for surface 8.0-iT. 2. A surface 8.0-i T is used as a heat-exchanger core. A cubic section of 1 ft3 is used. If hair = 10 Btu/hr-ftl-oF and hw = 400 Btu/hr-ft2-oF,evaluate U A. The fin material is aluminum; tube […]

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Binary classification Malignant:Load breast cancer

In these assignment use the load breast cancer from sklearn.datasets  and discuss the causes of breast cancer and its treatment. However, the binary classification include 212 Malignant and 357 Benign cases Binary classification Malignant:Load breast cancer Briefly, use the load_breast_cancer() from sklearn.datasets to get a copy of the breast cancer (diagnostic) data with 569 instances

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Water-pressure drop

A compact heat exchanger using surface 8.0-i T is to be designed. The entrance and exit temperatures, as well as the flow rates of each fluid, are given. List the steps, and describe how you would design a heat exchanger (if air flows over the tubes and water through the tubes) such that a specified

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The entrance header

In a shell-and-tube heat exchanger consisting of 1-in. schedule 40 steel pipe, 10,000 standard cubic feet per minute of air is to be heated from 1 atm and 70° to 205°P’ On the outside of the tubes, steam is condensing at 220°P’ A fan is available that will deliver cold air to the entrance header

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ECM607A: Microeconometrics 1

1ECM607A: Microeconometrics 1SET EXERCISE INFORMATIONCredit level: 7Credits: 10Module convenor: Shulin Deng (shulin.deng@reading.ac.uk)2This exercise is worth 50% of the final module marks for ECM607AExercise BackgroundThis project is intended to give you practice of: using a panel dataset and Stata; selecting asuitable empirical strategy (econometric estimators) to answer the set research question andto test hypotheses; interpreting output

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The pressure drop

Water is to be heated from 55° to 105°P at the rate of 275,000 gallhr in a single-pass shell-andtube heat exchanger consisting of l-in. schedule 40 steel pipe. The surface coefficient on the steam side is estimated to be 9,000 Btulhr-ft2 _ 0F. A pump is available that can deliver the desired quantity of water,

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The inlet pressure

A cross-flow heat exchanger is to be designed which will cool 3 Ibm/sec of air from 2000P to 100°P’ The cooling flow is 3 Ibm/sec of air with an inlet temperature of SO°p’ The hot fluid is to be cooled in surface 17.8-i W, a wavy-fin plate surface, and the cold fluid is to flow

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