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Multiphase flow line and Trunk line Basic Hydraulics and Flow Assurance banner
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Multiphase flow line and Trunk line Basic Hydraulics and Flow Assurance

Multiphase flow line and Trunk line Basic Hydraulics and Flow Assurance banner
Preview this course
Self-paced Beginner

Multiphase flow line and Trunk line Basic Hydraulics and Flow Assurance

4(286)
9 enrolled
1609 views
₹ 999
106 min
Anytime
English
1609 views
Sanjay Chakraborty
Sanjay Chakraborty
  • 7-day money-back guarantee
  • Lifetime access
  • Certificate of completion

Why enroll

Participants should join this course to gain a strong practical understanding of how fluids behave and travel from the wellhead to the plant inlet separator—knowledge essential for anyone working in upstream or midstream oil and gas operations. The course bridges theory with real field challenges, enabling learners to perform basic hydraulic calculations, interpret multiphase flow patterns, and anticipate flow-assurance risks such as slugging, wax, and hydrates. By attending, participants will enhance their problem-solving skills, improve design and troubleshooting capability, and build confidence in evaluating flowline and trunkline performance in real operating environments.

What enrolled engineers say

13 verified reviews
  • Feb 25, 2026

    The topics looked familiar, but the depth surprised me. Coming from an oil and gas operations role, multiphase flow regimes and basic pressure loss calculations are things dealt with regularly, but the course tied them together better from wellhead through flowline and trunk line. The sections on slugging behavior and hydrate formation were especially relevant to a brownfield tie-in project recently handled, where unstable flow kept tripping the inlet separator.One challenge was working through the simplified hydraulics without immediately leaning on software. Estimating frictional losses and elevation effects by hand took some effort, especially when visualizing how liquid loading builds up in low spots. That said, the struggle was useful. A practical takeaway was learning how to do quick back-of-the-envelope checks to validate OLGA results before accepting them in a design review.Coverage of wax deposition and basic mitigation options also filled a knowledge gap, particularly for long trunk lines with declining temperatures. The examples felt close to real field conditions rather than textbook cases. Overall, the content felt aligned with practical engineering demands.

    Suryavel S. · PROCESS ENGINEER Verified
  • Feb 25, 2026

    This course turned out to be more technical than I anticipated. The sections on multiphase flow regimes and frictional pressure drop in oil & gas flowlines went beyond textbook sketches and actually tied back to how trunk lines behave under changing GOR and water cut. Coverage of hydrates and wax deposition was especially useful, since those issues tend to sit at the intersection of hydraulics and operations rather than pure design. One challenge was reconciling the simplified hydraulic calculations with what’s typically seen in the field. Steady‑state assumptions work for screening, but edge cases like terrain-induced slugging or cold restart scenarios clearly need transient thinking, which is closer to current industry practice in larger energy utilities pipeline networks. That gap was acknowledged, which I appreciated. A practical takeaway was the structured way to sanity-check pressure losses and liquid loading before jumping into a simulator. That approach is similar to what’s done in chemical and pharmaceutical utility systems—do a first-pass hand calc to catch bad inputs early. Overall, the course helped connect wellhead conditions to inlet separator performance at a system level. It definitely strengthened my technical clarity.

    Suryavel S. Verified
  • Feb 25, 2026

    This course turned out to be more technical than I anticipated. The sections on multiphase flow behavior in oil and gas flowlines and trunk lines went beyond theory and actually reflected what shows up in upstream operations. The discussion on flow regimes, especially slugging near low points and risers, matched issues seen in brownfield assets where geometry was never ideal. Hydraulics coverage on frictional pressure loss and elevation effects was basic, but grounded enough to sanity-check results against what commercial simulators usually spit out. One challenge was working through transient behavior without relying on OLGA-style tools. Manually reasoning through liquid loading and restart scenarios took some effort, particularly around hydrate risk during shutdowns. Still, that exercise highlighted edge cases that are often hidden when everything is automated. A practical takeaway was a clearer method for estimating pressure margins along a trunk line and understanding how small temperature drops can trigger wax or hydrate problems. Compared with common industry practice, this reinforces doing first-pass calculations before jumping into software. The system-level implications for energy utilities tie-ins and inlet separation were useful context. I can see this being useful in long-term project work.

    Phaneendra S. Verified

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream
  • You're a Flow Assurance / Petroleum Technology professional
  • You want to build skills in Engineering & Design
  • You prefer self-paced learning you can revisit

You should skip if

  • You need a different specialisation outside Flow Assurance
  • You need live interaction with an instructor

Course details

Course Objective:

This course aims to equip learners with a foundational understanding of how fluids travel from the wellhead to the plant inlet separator, focusing on the essential principles of hydraulics and flow assurance. Participants will learn to interpret flow behaviour in wellhead and pipeline systems, perform basic hydraulic calculations, and evaluate pressure losses, liquid loading, and multiphase flow characteristics. The course also introduces key flow-assurance challenges such as slugging, wax deposition, hydrates, and sand production, along with mitigation strategies. By the end, learners will be able to analyze and troubleshoot flowline and trunkline performance confidently using practical engineering approaches.

Subject Description:

This course provides a comprehensive overview of the fluid journey from the wellhead to the inlet separator of an oil and gas processing facility. It explains the fundamentals of wellhead systems, flowlines, trunklines, and inlet separation, emphasizing how pressure, temperature, and multiphase flow dynamics influence system performance. Learners will explore basic hydraulic concepts including frictional pressure drop, elevation effects, and flow regimes, supported by simplified calculations. The subject also covers essential flow-assurance topics such as paraffin, hydrates, corrosion, and transient behaviour. Practical examples and field-based insights ensure relevance for engineers involved in upstream and midstream production operations.

Course suitable for

Key topics covered

  • Introduction

  • Basic hydraulics and flow assurance

  • Beggs and Brill and Oil gas correlation

  • Slugs ?

  • Why Slugs form?

  • Why Slugs matter?

  • Corrosion

  • Onset Pressure

Course content

The course is readily available, allowing learners to start and complete it at their own pace.

3 lectures1 hr 46 min
  1. Course Overview & Introduction
    9 min
  2. Basic Hydraulic and Flow Assurance
    67 min
  3. Slug Key Characteristics & Decision tree structure
    30 min

Opportunities that await you!

Skills & tools you'll gain

Engineering & Design

Career opportunities

Course Attachments

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Why people choose EveryEng

Industry-aligned courses, expert training, hands-on learning, recognized certifications, and job opportunities-all in a flexible and supportive environment.

What learners say about this course

Shaikh Shahbaz
Shaikh Shahbaz
Feb 25, 2026

Initially, I wasn’t sure what to expect from this course. Coming from a working role on brownfield oil and gas projects, the basics are familiar, but the way the role of a process engineer was tied to real plant decisions helped fill a gap I didn’t realize I had. Topics like PFD and P&ID development, separator sizing, and crude dehydration were explained in a way that connects directly to day‑to‑day engineering work. There was also useful context around utilities in energy facilities, especially steam and cooling water systems, which often get overlooked early in design. One challenge was keeping up with the transition from high‑level concepts to practical constraints like operability and safety reviews. The sections touching on HAZOP inputs and how process engineers support them took a bit of effort to digest, but they reflected real project pressure. A practical takeaway was a clearer approach to doing material and energy balances before jumping into simulation tools like HYSYS, which is something that can save time on live projects. Overall, the course helped connect oil and gas process fundamentals with how decisions are actually made on site. It definitely strengthened my technical clarity.

ramesh pangalwar
ramesh pangalwar
Feb 25, 2026

Coming into this course, I had some prior exposure to the subject. Most of my background was in chemical/pharmaceutical plants, so the oil and gas context helped connect a few missing dots. The sections on three-phase separation and dehydration were especially useful, and the way PFDs and P&IDs are used differently in upstream facilities made sense of drawings I’ve seen on projects but never fully owned. Utilities coverage around fuel gas, steam, and cooling water tied nicely into energy/utilities work I’ve done on compressor stations. One challenge was keeping track of where the process engineer’s responsibility stops and operations or mechanical picks up, particularly around API standards and HAZOP inputs. That boundary isn’t always clear in real projects, and it took a bit of effort to map the course examples to actual site constraints. A practical takeaway was a clearer checklist for early project phases: basic mass balance, separator sizing assumptions, and utility tie-ins before detailed design. That’s already been applied on a small debottlenecking study at work. Overall, the material filled a real knowledge gap without oversimplifying. The content felt aligned with practical engineering demands.

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Mohamed Sathamushen
Feb 25, 2026

This course turned out to be more technical than I anticipated. For a beginner-to-intermediate level, it went beyond job titles and actually touched the mechanics of oil and gas facilities, especially around separation trains, basic material balances, and how utilities like steam, cooling water, and power distribution tie into process design. The discussion on PFDs versus P&IDs reflected real industry practice, including where early-stage assumptions tend to break under debottlenecking or brownfield constraints. One challenge was reconciling the simplified examples with edge cases seen offshore, such as transient slugging or utility upsets that ripple across multiple units. That part could have used a bit more emphasis on dynamic behavior, but the limitation was acknowledged. Comparing this with chemical/pharmaceutical facilities was useful—continuous oil and gas operations demand a different mindset than batch-oriented pharma systems, particularly around control philosophy and operability. A practical takeaway was a structured way to think about a process engineer’s role during FEED, especially asking the right questions before HAZOP rather than treating it as a checkbox. System-level implications were discussed realistically, including how utilities often become the hidden bottleneck. It definitely strengthened my technical clarity.

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Puja Kawale
Feb 25, 2026

This course turned out to be more technical than I anticipated. For a beginner-to-intermediate level, it went beyond job titles and actually touched the mechanics of oil and gas facilities, especially around separation trains, basic material balances, and how utilities like steam, cooling water, and power distribution tie into process design. The discussion on PFDs versus P&IDs reflected real industry practice, including where early-stage assumptions tend to break under debottlenecking or brownfield constraints. One challenge was reconciling the simplified examples with edge cases seen offshore, such as transient slugging or utility upsets that ripple across multiple units. That part could have used a bit more emphasis on dynamic behavior, but the limitation was acknowledged. Comparing this with chemical/pharmaceutical facilities was useful—continuous oil and gas operations demand a different mindset than batch-oriented pharma systems, particularly around control philosophy and operability. A practical takeaway was a structured way to think about a process engineer’s role during FEED, especially asking the right questions before HAZOP rather than treating it as a checkbox. System-level implications were discussed realistically, including how utilities often become the hidden bottleneck. It definitely strengthened my technical clarity.

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Questions and Answers

A: The discriminator here is the P&ID convention boundary. At P&ID level, a solid line typically marks process hydrocarbon service without embedding flow regime assumptions; phase behavior is handled in line list notes and design documents, not the symbol itself. Treating it as single-phase or liquid-continuous would import an assumption that doesn't belong on this drawing layer.

A: The hard boundary is erosion onset, not regulatory coverage. API 14E exists to limit metal loss driven by particle impact and droplet impingement in multiphase flow; it's a screening tool, not a slugging control or a legal shield under COMAH.

A: The threshold is free water presence. Bulk removal first limits liquid holdup, and drying to a defined dewpoint before hydrocarbons avoids hydrate conditions; reversing the order traps water and builds slug volume.

A: The tipping point is holdup, not friction. At lower velocities, liquid accumulates in low spots, raising hydrostatic head and upstream pressure; terrain slugging assessment comes before aggressive valve moves or chemical shots.