Dave Ramirez
Senior Mechanical Engineer
Houston, TX
Over a decade of experience as a Senior Mechanical Engineer at a major independent oil and gas exploration and production company. A proud Houston native raised in the Energy Corridor, grew up surrounded by the city’s booming energy sector. Bachelor of Science in Mechanical Engineering from Texas A&M University in 2009 and later obtained Professional Engineer (P.E.) license in Texas. Responsible for the design, reliability, and integrity of critical mechanical equipment across offshore platforms, onshore production facilities, and pipeline compressor stations. Expertise includes rotating equipment (pumps, compressors, and gas turbines), pressure vessels, heat exchangers, and piping systems operating in high-pressure, high-temperature, and sour service environments. Focusing on failure analysis investigations, implements predictive maintenance programs using vibration analysis and condition monitoring, and drives reliability improvements that have reduced unplanned downtime by 25% over the past three years. Well-versed in API, ASME, and ISO standards and play a key role in capital projects, facility upgrades, and root cause analyses following major equipment incidents. Known for my practical, field-oriented approach and my ability to collaborate effectively with operations, drilling, and HSE teams in fast-paced environments. An active member of the American Society of Mechanical Engineers (ASME) and the Society of Petroleum Engineers (SPE).
Mechanical
Oil and Gas
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15 years
P.E.
Profile is not yet complete
Profile is not yet complete
In our condensate stabilizer train, every time ops bumped the demulsifier, our E-205 shell-and-tube went from clean to molasses in a week. We chased velocity, baffle leakage, metallurgy, even blamed crude blend. Turned out the fix was polymerizing in hot zones and plating the tubes.We rigged a cheap side-stream with a 40 µm strainer and a beaker-on-a-hot-plate test at process film temps to see if the dose browned. Moved the injection lance downstream of the hot bundle, cut rate 30%, and used DP...
I'm the mech guy babysitting an MDEA sweetening unit that foams at the worst times. When contactor DP climbs and the regenerator level chatters, our compressors start singing. Vendor wants to sell a cloud-tuned antifoam skid. I’d rather keep control in the rack room.What’s worked: clamp hydrocarbon slip, swap carbon when lean color darkens, drain coalescers daily, and a very low continuous antifoam trickle through a rotameter. I use hot-lean shaker-bottle tests and tie dose to contactor DP...