PETE 2032
Problem 1310
Perform a threestage separator calculation for the following black oil.
Refer to Excel Spreadsheet for composition chart
Use Kfactor of decane for heptane plus. The black oil
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Exam 1:
2ll3
Physics
Sprin 92016
6:00 pM, Monday, February
302016
Last Name
First Name
Clearly circle your section:
Mox/WeoslpnrJEcrroNs
Abdelwahab
Sec
10:30
Abdelwahab
Lee
Sec 2
Zuniga
Sec 3
Sec 4
2:
Lecture1
17:47
As fluids are produced from reservoirs, the conditions of their existence, namely pressure,
temperature and composition change.
Major fluids: gas, oil, water
Also produce sand
Standard
PETE 2032 FALL 2014
HOMEWORK ASSIGNMENT #2 (Phase Behavior)
2 pages (1/2 pages)
Due:4:00 PM, Wednesday, 9/17/14
1. (a) State Gibbs phase rule. What is the essential condition for applying Gibbs
phase
PETE 2032 FALL 2011
SOLUTION KEYS # 11
Thursday, 11/17/11
1.
a)
Fill in the relative volume column for the flash vaporization test.
Pressure, psig
3500
3000
2800 = Pb
2500
2100
b)
Total Volume, cc
82.
Solution # 10 (Pete2032)
Answer:
For ideal solution case in 121, following derivation was made.
Let, the components be 1 & 2 for the binary mixture.
By applying Raoults law, x1*Pv1+x2*Pv2=P
=> x1*Pv
PE TE 2032
Page 7
EXAM 21101713
5' (20m . .
followitlgtfas rehievrmf existing at 5735 psia and 268F contains hydrocarbon gas orthe
mposmon Assuming that the gas does NOT behave like an ideal gas, ca
PETE 2032 Homework Solutions Chapter 12 129 Six pound moles of ethane, three lbmoles of propane and one lbmole of nbutane are mixed in a closed container and the temperature is adjusted to 75oF. W
PETE 2032
Homework Solutions Chapter 12
129 Six pound moles of ethane, three lbmoles of propane and one lbmole of nbutane are mixed in a closed container and the temperature is adjusted to 75oF. Wh
12—2. Use the equations developed in Exercise 12—1 along with the
substitution of K3— for pvjip to derive an equation with which the
composition of the gas phase of a nonideal two—component
mixture ma
Properties of Black
Oils
Field Data
Chapter 9
Production Data: 2011
Deepwater Gunashli Platform, Azerbaijan
http:/www.bp.com/assets/bp_internet/globalbp/globalbp_uk_english/reports_and_publications/st
PETE 2032 Homework Solutions Chapter 5 5.6 A field in north Louisiana discovered in 1953 and developed by 1956 had an initial producing gasoil ratio of 2000 scf/STB. The stocktank liquid was "mediu
Fluid Properties — Quiz 1
NAME Aw MW")
Label the following on the above PT plot for a pure substance: a) Critical Point, b)
Triple Point, c) VaporPressure Curve, d) Melting Point Curv , e) Subli
PETE 2032 Homework Solutions Chapter 11 Second Assignment 119 Use the correlation of Fig 116 to calculate the density of a reservoir liquid at its bubble point of 1763 psia at a reservoir temperatu
PETE 2032 Homework Solutions Chapter 8 8.1 A stocktank oil has a specific gravity of 0.875. What is the density in lb/ft3?
Water has a density of 62.4 lb/ft3
o = o w = ( 0.875)( 62.4) = 54.6 lb
PETE 2032
Homework Solutions Chapter 8
81
A stocktank oil has a specific gravity of 0.875. What is the density in lb/ft3?
Water has a density of 62.4 lb/ft3
o = o w = (0.875)(62.4) = 54.6 lb
82
Wha
All work must be shown. All writing must be legible, if I can't read it, it is wrong. All work must be contained on the pages of the exam and the attached calculation sheets. No open books, no additio
9.2
an oil field with several wells has the following production history. Producing gasoil ratio is really separator gasoil ratio; stocktank gas is vented and not metered. Separator conditions are
PETE 2032 Homework Solutions Chapter 3 3.1. Calculate the molar volume of an ideal gas at 100 psia and 90oF.
pVM = RT psia. ft 3 o 10.732 (90 F + 460 o ) 3 lb  mole.o R RT = = = 59.0 ft lb  mo
CHAPTER 12
GASLIQUID EQUILIBRIA
We consider theoretical means to calculate the
hydrocarbon mixture properties, especially in the
twophase region.
Twophase region is where both phases (liquid and
va