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Q1:Relative permeability measurements are made on three core samples. The measured data are summarized below: Core sample 1 h = 1 ft k = 100 mD Soc= 0.35 Swc= 0.25 Water Saturation Sw 0.20 0.25 0.30 0.40 0.50 0.60 0.65 0.72 *Value at critical saturation Core sample 2 h = 1 ft k=80 mD 0.850* 0.754 0.557 0.352 0.131 0.000 Soc= 0.28 Swc = 0.30 Core sample 1 Kro Krw Core sample 2 Kro Krw 0.000 0.018 0.800 0.092 0.593 0.198 0.393 0.327 0.202 0.400* 0.111 0.000 0.000 0.077 0.191 0.323 0.394 0.500* Core sample 3 h = 1 ft k=150 mD Soc= 0.35 Swc = 0.20 Core sample 3 Krw 0.000 0.008 0.027 0.088 0.176 0.286 0.350* Kro 1.000* 0.872 0.839 0.663 0.463 0.215 0.000 It is believed that a connate water saturation of 0.27 and critical oil saturation of 30% better describe the formation. Generate Oil and water relative permeability data using new critical saturation. Plot the averaging relative permeability data. Using data given, de-normalize the data to generate the required relative permeability data.See Answer
Q2:HIRA Homework Assignment ✓ CPE 624 - Process Safety and Sustainability: HIRA HW Assignment Each student will be assigned a processing node to perform a Hazard and Operational 1 of 3 analysis (see the attached excel sheet for your node assignment). In your s, Identify the node you are performing the HAZOP on, the provided diagram of the node, the 2 highest priority process parameters (if you cannot identify 2 please provide an explanation as to why) you are going to be analyzing, and at least 2 deviations associated with each process parameter. Organize your HAZOP analysis into a table as presented to you in the HIRA notes below. Nodes: Distillation column • Continuous Stir Tank Reactor (With cooling jacket) Reactant A Reactant B Coolant inlet • Flash Unit F, XF Feed Feed Preheater Steam TC TT Product Coolant outlet Valve Flash at P bar & T°C Vapour V,y Flash Vessel Liquid L, x/n CPE 624 - Process Safety and Sustainability: HIRA HW Assignment Each student will be assigned a processing node to perform a Hazard and Operational Study (HAZOP) analysis (see the attached excel sheet for your node assignment). In your HAZOP analysis, Identify the node you are performing the HAZOP on, the provided diagram of the node, the 2 highest priority process parameters (if you cannot identify 2 please provide an explanation as to why) you are going to be analyzing, and at least 2 deviations associated with each process parameter. Organize your HAZOP analysis into a table as presented to you in the HIRA notes below. Nodes: • Distillation column 8 3 2 16 -1 5 Continuous Stir Tank Reactor (With cooling jacket) TC Reactant A M TT Reactant B Coolant inlet Product Coolant outlet • Flash Unit F, XF Feed Decanter Feed Preheater Feed Stream- • Steam Valve V1 LC Decanter V1 Heat Exchanger Steam Feed PT PC (TC Condensate Product Flash at P bar & Vapour тос Flash Vessel V,y Liquid L, x LT Liquid Products Solid Products • Fixed Bed Reactor Gas out Liquid feed Packed bed Air or gas inlet Stripper Unit Liquid out (+ solid) EXHAUST (GAS OUTLET) FLOW METER AIR STRIPPER PUMP FEED TANK FLOW METER AIR COMPRESSOR HEATER COLLECTION TANK HEATERSee Answer
Q3:1. Discuss the two commercially most important properties of crude oils See Answer
Q4:2. What is the specific gravity of a 30° API gravity oil? (0.5 Marks) See Answer
Q5:3. What do you mean by Reid vapor pressure. How is performance of a spark ignition motor engine effected if the fuel's Reid vapor pressure is too high or too low ? See Answer
Q6:5. What has been the impact of Russia Ukraine conflict on the global oil market? See Answer
Q7:Solve the following BVP-ODE with the Finite-Difference, Shooting, and Successive Over- relaxation Methods. Use a step size of 0.01. You may use MATLAB or Excel/VBA to solve these BV-ODES. Remember to completely annotate your programs and turn in your complete programs and output. Also turn in a complete description of your algorithm that you used in the program, i.e., as shown in the notes and examples in class. Compare and contrast the use of all three BVPnumerical methods that were used to solve this problem. A chemical reactor with axial dispersion is governed by the following equations:See Answer
Q8: Explain what is the difference between Andesite and Diorite? (4 marks)See Answer
Q9: What is the main difference between extracting Oil Shales and Tar Sands?See Answer
Q10: A mixed hydrocarbon stream must be distilled in a continuous distillation column. The flow rate of the feed is 1000 kmol/h. The feed enters as a liquid at its boiling point. The feed mixture containing six components (CH4 = 0.032, C2H4 = 0.068, C2H6 = 0.17, C3H6= 0.30, C3H8 = 0. 32, n-C4H10 = 0.11) is to be separated by distillation. It is desired to recover 98.5% mole fraction of the light key in the distillate and 98% of the heavy keyin the bottom product. The average relative volatility (a) values are given in Table 1.The a can be assumed to remain constant with any temperature variation. 1.Determine the light key (LK) and heavy key (HK). 2.Use Underwood's method to determine the minimum reflux ratio (the 0 valuesto try are 1.1.1.17 and 1.2).(15) Use the Fenske equation to determine the minimum number of trays.See Answer
Q11: e) Explain different types of petroleum traps and their importance in trapping mechanism of oil.See Answer
Q12: a) Explain how Geological Time Scale describes the timing and relationships between events that have occurred throughout Earth's history? (4 Marks)See Answer
Q13: 1. A drillstring consists of 9,000 ft 5 in, 19.5 lbm/ft drillpipe, and1,000 ft of 8 in OD, 3in ID drill collars. What is the: (a) Volume of the drillpipe in bbl. (b) Volume of the drill collars in bbl (c) Number of pump cycles required to pump surface mud to the bit(duplex pump, 6 in liners, 2.5 in rods, 16 i strokes, pumping at 85 % volumetric efficiency). (d) Displacement of drillpipes in bbl/ ft (e) Displacement of drill collars in bbl/ft.See Answer
Q14: ) What differentiates cleavage from fracture of a mineral? (1.5 marks)See Answer
Q15: O Explain the process of diagenesis, catagenesis and metagenesis in detail.See Answer
Q16: The following PVT data are from a volumetric oil reservoir at an initial pressure of 2000 psia.The connate water saturation is 25%. Assume negligible rock and water compressibilities. 1. Was this reservoir initially saturated or under saturated? Why? 2. When the reservoir pressure fell to 1500 psia, the cumulative production of oil and gas were 7.5 MMstb and 9.5 Bscf respectively. Estimate the initial oil in place. 3. What was the initial reservoir pore volume?See Answer

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