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Overview of Downhole Tubulars - Oil and Gas Wells banner

Overview of Downhole Tubulars - Oil and Gas Wells

Overview of Downhole Tubulars - Oil and Gas Wells banner
Live online Intermediate

Overview of Downhole Tubulars - Oil and Gas Wells

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1 enrolled
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2 hrs
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English
1717 views
Team OG
Team OGUpstream Oil & Gas Technical Professional
  • 7-day money-back guarantee
  • Session recordings included
  • Certificate of completion

Why enroll

The course will give an overview of the main categories, types and consideration for all downhole tubulars. These are extensively used in all oil and gas wells and serve different purposes, which will be covered.

What enrolled engineers say

4 verified reviews
  • May 3, 2026

    The jump from junior framing to senior tradeoffs shows up fast here; it's explicit without being preachy. In the Tubular Design Walkthrough, the collapse vs burst example using a 7‑in casing at ~9k ft stuck, especially the safety factor callouts. I liked how failure modes tie back to arch and ops, though I wasn't sold on the brief nod to obs and wished for more on closing the loop with field data. By the end I've got notes translating this into our infra repo—naming, PR checks, and a CI gate I'd add.

    Murali C. Verified
  • May 3, 2026

    Needed a clearer mental model of what’s actually inside the hole, and this filled gaps without marketing fluff. The section on casing vs tubing around the burst/collapse calc with API J55/N80 table stuck, plus the animation at 22:10. It mapped components like an arch diagram; think prod failures traced via obs, not k8s—mostly worked, though I wished for more on workover edge cases. it's answered questions I've been parking for a year while skimming well reports and PRs in the repo.

    parekh J. Verified
  • May 3, 2026

    Dense material without the fluff; it moves fast but stays readable. The Module 3 casing vs tubing section, especially the burst/collapse walk-through using API 5CT grades, stuck with me because it mirrors spec reviews I see before prod changes. I've already used that framing to sanity-check a client’s arch decisions on connections and weights, which saved a back-and-forth. Wasn't sold on the brief metallurgy pass; wished there was more on sour service failures and photos.

    sarath S. · Offshore Construction Engineer Verified

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream
  • You're a Petroleum Technology / Mechanical Engineering professional
  • You have some foundational knowledge in the subject
  • You prefer live, instructor-led training with Q&A

You should skip if

  • You're looking for an introductory overview course
  • You need a different specialisation outside Petroleum Technology
  • You need fully self-paced, on-demand content

Course details

Downhole tubulars are essential steel pipes used in oil and gas wells to ensure safe drilling, well integrity, and efficient production. They form the structural framework of a well and play a critical role throughout its lifecycle—from drilling to completion and production.

Downhole tubulars are cylindrical steel components installed inside the wellbore to maintain stability, control pressure, and provide a conduit for fluid flow. They are designed to withstand extreme downhole conditions such as high pressure, temperature, and corrosive environments.

The focus of this course will be on introducing the participant to the different oil and gas well tubulars, such as casing, tubing and drill pipes. The purposes of different types of tubulars which are available in several different grades and with various joint thread types, will be covered.

Course suitable for

Key topics covered

  • Different purposes for tubulars used extensively in the oil and gas well

  • Drill pipes and collars, Production Tubing, Production Casing, Cross-over subs, Pup Joints

  • Defining tubulars by size, weight and end connection threads

  • API steel grades for tubing and casing

  • Methods of manufacturing downhole tubulars

  • Thread types: API, non-API and Premium

Opportunities that await you!

Career opportunities

Training details

This is a live course that has a scheduled start date.

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

sarath Selvaraj
sarath Selvaraj Offshore Construction Engineer
May 3, 2026

This course nudged how I think about legacy choices, kind of like refactoring old arch without breaking prod. It frames sand control as tradeoffs instead of rules, which clicked for me coming from software and infra, especially when you’re juggling constraints that look a lot like CI gates and RPS limits. The micro-detail that stuck was the screen sizing example in the “Gravel Pack vs Frac Pack” section, where they walk through median grain size and then show how one assumption cascades into cost and ops risk—felt like reading a PR where one default sneaks into prod. I wasn’t sold on every analogy to modern completions; the k8s-style modularity pitch was mostly helpful but a bit hand-wavy in spots. Still, the beginner pacing worked, and the oilgas context mapped cleanly to how we think about legacy systems in energyutilities. I’ve already got a note to tweak some of our internal logic after this, mostly around how we document assumptions before they fossilize in the repo.

Abraham Idoko
Abraham Idoko Comrade
May 3, 2026

The course laid out a workable path through a messy topic, which helped me map fundamentals without getting lost. The Chapter 4 pipeline pressure drop example using Darcy-Weisbach and a step-by-step calc stuck, especially the unit checks. I kept mapping it to infra in prod, thinking about constraints, safety margins, and obs, so it clicked faster; it's beginner-friendly but not dumbed down. Wasn't sold on the short k8s-style control analogy in the ops section, and I wished there was more on gas processing impacts for energyutilities, but I've already applied bits in a repo note for the team.

Ebrahim Xoshnaw
Ebrahim Xoshnaw
May 3, 2026

The section headers pulled me in, and the content mostly delivered. Chapter 3’s pipeline hydraulics example, walking a pressure drop calc end to end, stuck; it clicked like budgeting RPS before a prod push, and the compressor station tradeoffs read like arch notes you’d leave on a PR. it's beginner-friendly without talking down, though I wasn't sold on how light the infra/obs tie-in was for energyutilities oilgas ops. I’ve already avoided a couple late CI-style scrambles that would've felt like debugging at 2am.

Savio Vogt
Savio Vogt
May 3, 2026

Module 4 on compressor sizing dragged a bit and repeated formulas I’d already seen. After that, it reads like field notes from someone who’s been through a few turnarounds. The section on dehydration stuck with me, especially the worked example comparing TEG vs molecular sieves and the callout on hydrate risk during cold starts. As a TeamLead, I care about team lift and cost, and this helps juniors reason about arch tradeoffs without overspending on infra. I’ve already pointed a new hire to the chapter on gathering systems and pressure drop; the RPS-style thinking maps well to ops. it’s nudged how I frame system-level troubleshooting during handoffs, with better obs questions before jumping to fixes.

COMPLETED

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Questions and Answers

A: That's the most common mistake — assuming drawing symbols are decorative. Flush joint versus LTC changes OD, drift, and contact forces. With permit-to-work stacked and no onshore support for hours, proceeding on an assumption exposes you to stuck tools and failed logging runs that can't be mitigated later.

A: That's the most common mistake — treating pressure rise as a pump problem. Friction scales sharply with ID, so a borderline drift or wrong weight pipe shows up exactly like this. Changing fluids or rates masks the symptom and loads the string closer to burst.

A: That's the most common mistake — confusing absolute internal pressure with differential. Burst is driven by delta-P across the wall. With these numbers the thin-wall equation lands just over 1.2 margin, and that’s before you start stacking test or corrosion allowances.

A: That's the most common mistake — assuming seal details are interchangeable. Dual versus single seal changes test envelopes and acceptance criteria. Letting that slide offshore turns a paperwork issue into a well integrity risk.