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$100 To Be Won This Week by Nigel1: 5:08pm On Jul 29, 2015
QUIZ OF THE WEEK 

Dear Nlanders,

Congrats to Enwose! Last week's winner of $35!

Answer only few questions for a chance to win this week's prize of $100!

Visit http://fedpforum.epcmengineers.com now!


Twitter: @FEDPForum
Facebook: FEDP Forum
Re: $100 To Be Won This Week by weedy: 5:10pm On Jul 29, 2015
Good am in
Re: $100 To Be Won This Week by Nigel1: 7:51pm On Jul 29, 2015
1. Re-arrange the following in Order of start-to-end for an Oil and Gas Brownfield Facilities Project
a. Process Flow Diagram
b. Preliminary Block Flow Diagram
c. Management of Change Risk Assessment
d. Constructability Review
e. Field Data gathering and measurements
f. Pre-Construction Risk Assessment
g. Piping and Instrumentation Diagram-IFC


2. Arrange the following in sequence: Earliest-to-Latest
a. Front End Engineering Design
b. Feasibility Study
c. Start-Up/Operations
d. Procurement of Long Lead Items
e. Detailed Engineering Design
f. Commissioning
g. Construction/Fabrication


3. What is the name of the document that is developed to guide the process of a HAZOP Study in terms of Scope, Timing, Venue, Methodology, Boundaries, Participants, etc.?


4. Which of the following is NOT a PARAMETER in a typical Guide-Word HAZOP study
a. FLOW
b. TEMPERATURE
c. HEIGHT
d. PRESSURE
e. DENSITY
f. VISCOSITY
g. SPEED


5. Can a regular 90 DEG ELBOW be used in the construction of a main pipeline segment (Not in Pig Launcher or Pig Receiver areas). YES/NO. Give reasons to support your answer.


6. During the operation of a newly installed 3-Phase Oil, Gas, Water separator connected to a knock-out vessel and flare, persistent high level and liquid carryover to flare was observed. As an engineer, identify at least 5 potential CAUSES that could result in this deviation.


7. A new Marginal field Operator is located 250m away from an existing Natural Gas Pipeline. The gas pressure in the pipeline is 30 Barg. The Marginal field is mostly non-associated gas but they have one dual completed well with a combined tested capacity of 3,000 BOPD, GOR of 1200 SCF/Barrel, FTHP 1,650 Psig, FLP 700 Psig. What surface production configuration would you advise for adoption to minimize or possibly eliminate compression power and costs to enable timely injection of gas sales through the existing pipeline i.e. minimize flaring and generate early revenue? Support your answer with a sketch. This question carries 60% of the total quiz score.


ONLY 100% Correct Answer wins the Star prize. Highest Score for all entries, but below 100% wins only 50% of Star Prize.

To submit answers Visit http://fedpforum.epcmengineers.com 

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