School of Petroleum Engineering Design Project for Petroleum Engineers PTRL 3022 Group Report Mass & Energy Balances Group 3 Done by; Student No; Khalid Al-Abadi 3392461 Ahmed Al-Suleimani 3389102 Munther Al-Kalbani 3389087 Due date: 29/ 8/ 2012 Contents 1. Executive summary 2 2. Introduction 3 3. GOSP diagram 4 4. Gas Fractionation diagram 5 5. Three phase separation
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Name ID # A Fill the following table Substance H2O H2O H2O R134a R134a T‚ oC 250 105 340 Substance H2O H2O H2O R134a R134a P‚ kPa 1800 v‚ m3/kg u kJ/kg x Phase description 1 0.025 50 8200 360 2000 T‚ oC 250 105 340 5.82 50 P‚ kPa 1800 120.8 8200 360 2000 v‚ m3/kg 0.125 1.42 0.02806 0.025 0.0009013 * quality not defined 2645 u kJ/kg 2685 2512 2715 134.6 121.4 X * 1 * 0.4322 * Phase description Superheated
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Strategy * Logistics * Organization Strategy 4) Logistics Network Design This is the implementation phase of the key start-up actions of the logistics plan. The logistics system needs to be designed to provide the ILMS which will execute the logistics plan. It is this ILMS which will work in a coordinated manner to execute the logistics plan developed in response to the business operations strategy and CS goals. Key Considerations in Network Design * Demand * Customer Service *
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AIR QUALITY IMPACT ASSESSMENT REPORT OF THE PROPOSED BASE TRANSCEIVER STATION (BTS) October‚ 2012 1.0 Introduction The sources of ambient air pollution‚ especially in urban environments‚ are often quite diverse. These sources can be broadly classified as stationary‚ mobile and area emission sources. Emissions of pollution from these three classes of sources typically result in complex spatial and temporal distributions of ambient air pollution concentrations. Emission inventories form
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low-pressure hot-water battery to 30 0C d.b. Identify all the condition data for both entry and exit states. 3. Re-circulated room air at 21°C d.b.‚ 50% saturation is mixed in equal amounts with summer outdoor air at 31°C d.b.‚ 22 °C w.b. State the condition of the mixed air. 4. An air-handling unit receives re-circulated room air at 23 °C d.b.‚ 50% saturation and a flow rate of 2 m3/s‚ and fresh air at -5 °C d.b.‚ 100% saturation with a flow rate of 0.5 m3/s. The mixed air is heated to 35
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Vol. 1 ACETIC ACID 115 ACETIC ACID 1. Introduction Acetic acid [64-19-7]‚ CH3COOH‚ is a corrosive organic acid having a sharp odor‚ burning taste‚ and pernicious blistering properties. It is found in ocean water‚ oilfield brines‚ rain‚ and at trace concentrations in many plant and animal liquids. It is central to all biological energy pathways. Fermentation of fruit and vegetable juices yields 2–12% acetic acid solutions‚ usually called vinegar (qv). Any sugar-containing sap or juice can
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The objective : 1. To determine the head loss and friction factor for laminar & turbulent flow in a smooth pipe over a range of Reynolds’s number . 2. To obtain the following relationships : a. Head loss as a function of the velocity of flow . b. Friction factor as a function of Reynolds number . Theory : The friction resistance to the flow of fluid through a pipe results in a loss of pressure energy for a given fluid flowing a long a given pipe‚ experiments show that for laminar flow
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Chapter 4 Homework: Correlation and Prediction Your answers should be typed. Please attach your hand written calculations on a separate sheet(s). 14. Predicted VO2 = 30 +1 × (X)‚ where X is the time in minutes to complete a 1.5-mile run and the SEE is 5 ml/kg/min. VO2= 30+1(8) VO2=38 If John runs the 1.5-mile run in 8 minutes‚ what is his predicted VO2? 22‚ Define the terms positive correlation and negative correlation. What is the difference? Give an example of each. Positive
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innovation and change as required by a practising or potential middle manager. note An ILM Assessment Task provides an opportunity to relate your learning directly to your current organisation. It is recommended that you discuss the assignment with your line manager to explore and agree how the task could be used to support the needs of your employer (as well as evidencing your learning as part of completing your ILM qualification). If you are not currently working within an organisation‚ then you
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Determine velocity of gas inside a pipe flow if water manometer connected to Pitot-Static probe show 2.5 cm height. Take density of water and air 1000 kg/m3 and 1.25 kg/m3. 4. Determine velocity of water inside a pipe flow if mercury manometer connected to Pitot-Static probe show 10 cm height. Take density of mercury and water 13600 kg/m3 and 1000 kg/m3. 5. Describe 5 advantage and disadvantage of orifice and venturi flowmeter. 6. Derive equation for obstruction flowmeters which is connected to a manometer
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