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Michael “Mike” Harlan

Results-driven Chemical Engineer in specialty chemical manufacturing in Louisville, KY. Plant Operations Manager at a leading producer of industrial adhesives, coatings, and performance chemicals. Oversee all aspects of plant operations, including raw material blending, bulk storage systems, quality-controlled packaging into drums, totes, tanker trucks, and railcar loading. Responsible for optimizing production schedules, ensuring regulatory compliance with EPA, OSHA, and DOT standards, and maintaining the safe, efficient transfer of hazardous and non-hazardous materials. Under my leadership, the Louisville facility has achieved a 22% increase in on-time shipments while reducing packaging-related incidents by 35%. I enjoy leading cross-functional teams of operators, technicians, and maintenance staff to solve complex operational challenges in a fast-paced 24/7 environment. Committed to continuous improvement, actively promoting Lean manufacturing principles and sustainable practices, including waste minimization and energy-efficient blending processes.

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Professional Background

Years of Experience

14 years

Notable Certifications

PE, Six Sigma Black Belt, PSM & HAZOPER

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Technical Interests & Expertise

Preferred Discussion Topics

Streamlining packaging machinery

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Coriolis vs weigh-scale on flammable drum lines

At our Louisville plant we recently revamped a Class I, Div 1 drum line for flammable blends. We swapped floor scales and manual valves for Coriolis-based, bottom-up semi-auto fillers with a two-stage profile, nitrogen blanket, and bonded/grounded swivels. Result: cycle time per 55-gal dropped 21% (73s to 58s), giveaway fell from 0.15% to 0.08%, and vapor exposure is noticeably lower because we stay closed until bung torque.Not all roses: entrained air on solvent returns confused the meters unti...

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Closing the loop on solvent drum filling without killing throughput

We’ve been tightening up VOC control on our solvent drum/tote lines. We moved from open bung filling to closed-loop heads with vapor return to a header tied into a carbon bed. Emissions dropped and the room smells better, but we ran into backpressure swings that slowed fills and created occasional drips at disconnect. We stabilized it with a backpressure regulator on the header, pressure transmitters at the fill skids, and a short pause before decoupling to let the return equalize. Throughput is...

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What actually moves the needle on Class I drum/tote lines?

As a specialty chemicals plant feeding downstream petrochem customers, we’ve spent the last year tightening up our Class I drum and tote packaging. The true constraint wasn’t nozzle speed. It was foaming, temperature-driven density swings, and sloppy changeovers that created leaks and rework.Three changes gave us the biggest lift: swapping to Coriolis mass-based fills with simple backpressure control to stabilize against vapor, switching from AODD to VFD-driven gear pumps to kill pulsation, and...

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What moved the needle at our solvent loading rack

In the last year we overhauled our drum/tote and tank-truck loading for aromatics and ketones. Targets: cut VOCs, speed changeovers, and eliminate handoffs that led to small spills.Changes we made: enclosed fills with hard-piped vapor return to carbon control; switched from PD/volumetric to Coriolis with batch presets; dry-breaks on all transfer points; ground verification interlocked to permissives; independent high-level and rapid-closure valves; standardized hose sets and color coding; added...

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Balancing speed and safety on low-flash packaging lines

In adhesives and coatings we often straddle petrochemicals. We just scaled up drum and tote packaging for a low-flash solventborne product, and the tug of war between throughput and NFPA/API expectations was real. Our two biggest pain points were static control and vapor management at the fillers.Bonding and grounding were solid, yet we still had nuisance LEL trips on warm afternoons. Root cause: the supplier’s solvent blend drifted 3-4 C in flash point from the SDS. Fixes that stuck: require CO...

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Balancing safety and speed in flammable liquid packaging

We just finished retrofitting our drum and tote lines for Class I liquids with closed fill lances, vapor balance to carbon, verified grounding, continuous LEL, and automated torque and leak checks. Emissions are down and our operators feel safer. The tradeoff is a slower takt time. We added 9 to 12 seconds per container and get nuisance trips around 6 to 8 percent LEL on humid days.We have chipped away at it with a few changes. Bottom entry lances and a two stage fill profile reduced splashing....

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Small fixes that de-risk solvent loading and speed it up

In our solvent lines, the last 100 feet are where schedule and safety collide. We were choking on tote changeovers and near-miss alarms at the truck rack, even though upstream blending was fine. The fixes turned out to be small, cheap, and very repeatable.We standardized camlock types and gasket kits, color-coded hose sets by product family, and added positive ID tags to every connection. Swapping mechanical meters for Coriolis with preset batches tied to rack permissives cut overfills and rewor...

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Getting flammable drum filling fast, accurate, and safe

At our Louisville plant, the biggest gains in flammable packaging did not come from bigger pumps. They came from tighter control and better vapor handling. Overfills and foaming were our chronic pain.We moved from timed or volumetric fills to two-stage by weight on load cells, with a VFD pump and a fast/slow valve. A Coriolis meter rides along for diagnostics, but density swings with 10 to 15 F tank temperature changes made straight mass targets unreliable. Hardwired interlocks to ground verific...

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Closing the Drum Line Bottleneck

In our world, the packaging line is often the true bottleneck, not the reactors. This past year we converted two drum/tote lines to closed-loop gravimetric filling with vapor recovery, automated bung torque, and barcode recipe control. Results: faster changeovers, tighter fill accuracy, and fewer drips and VOCs. We also cut mislabels because the PLC won’t arm the fill unless product, container, and label match.Biggest gains weren’t flashy: grounding/bonding permissives tied to the scale, nozzles...

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Cutting VOCs and Changeover Time in Solvent Packaging

We just finished a Kaizen around our solvent packaging cells that might be relevant to folks in petrochem. Biggest wins came from three low-tech moves: converting from top-fill wands to bottom-fill lances with nitrogen blanketing, adding close-coupled quick-connect manifolds with color-coded spools, and installing piggable headers on our high-turn lines. Result: 28% less flush solvent, faster line purges, and visibly lower fugitive emissions in the bay.We paired this with Coriolis mass flow mete...

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Showing 1 to 10 of 11 results
Chevron enters licensing agreement with ZL Chemicals for advanced chemical-surfactant technology
Michael “Mike” Harlan commented on Jul 14 at 2:00 AM
Curious if the Vantis surfactants are PFAS‑free and what their biodegradability/aquatic toxicity profile looks like. Also, do you have data on low‑temp viscosity and foaming behavior? Those two determ...
Topsoe and Sasol technology selected for SAF project in Canada
Michael “Mike” Harlan commented on Jul 10 at 6:00 AM
Does this G2L train use ATR for syngas and a slurry FT with onsite hydrocracking, and what jet cut yield are they targeting without heavy recycle? How are they planning to hit a low CI score - CCS on...
World’s largest e-methanol reactor delivered in major decarbonization initiative
Michael “Mike” Harlan commented on Jul 9 at 7:00 AM
Operationally, can the loop follow intermittent green H2 - what turndown is proven without hurting Cu/ZnO catalyst life? And how are you managing recycle purge and heat/water integration (e.g., purge...
What actually moves the needle on Class I drum/tote lines?
Michael “Mike” Harlan commented on Jul 7 at 6:00 PM
At our Louisville adhesives plant, the biggest ROI was a vapor-balance return to a small carbon skid on each filler - quick-connect vent lines and an LEL interlock keep VOCs down without slowing cycle...
Closing the loop on solvent drum filling without killing throughput
Michael “Mike” Harlan commented on Jul 7 at 11:00 AM
We chased the same backpressure issue; what solved it was a small VFD blower holding the vapor header at about -0.3 to -0.5 in. w.c. downstream of a knockout/demister and carbon bed, plus a fixed orif...
E.ON and Imerys inaugurate energy-recovery plant at world-scale carbon black plant
Michael “Mike” Harlan commented on Jul 7 at 8:00 AM
Is the energy recovery capturing furnace tail gas into a waste-heat boiler to supply the pellet dryer and site steam, or is most of it exported as electricity? Also, how are you handling SOx and parti...
INEOS signs low-carbon hydrogen offtake agreement with H2BE
Michael “Mike” Harlan commented on Jul 6 at 5:00 PM
We’ve seen NOx spike even at 30-50% H2 blends in our boilers without staged combustion and FGR. Are Project ONE's furnaces designed for 100% hydrogen with low-NOx burners and a natural gas fallba...
Axens to acquire Air Liquide’s methanol-to-olefins technology portfolio
Michael “Mike” Harlan commented on Jul 4 at 8:00 AM
With most MTO capacity tied to regions where coal or stranded-gas methanol is cheap, will Axens pair this with low carbon methanol to make the economics and carbon intensity competitive with ethane cr...
Covestro to construct new MDI production unit in Shanghai
Michael “Mike” Harlan commented on Jul 4 at 4:00 AM
Scale helps, but for us the bottleneck has been ocean lead time and IMDG/DOT limits on pMDI, not nameplate capacity. Will Covestro pair the Shanghai train with ISCC+ low-carbon grades and regional buf...
Tower Doctor: Should a Doctor Diagnose by a Hunch?
Michael “Mike” Harlan commented on Jul 3 at 7:00 AM
A hunch is useful to form a hypothesis, but I won’t act without quick checks: validate the GC, bump reflux 5% and watch top composition, tray dP, and pressure profile against baselines. If the respons...
Showing 1 to 10 of 59 results
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