Chemical Engineer Resume 2026 - process design, simulation and safety sample free

Антон Литвинов
Published: 03.10.2026 Updated: 03.10.2026

A chemical engineer resume has to answer a question the job title does not: which chemical engineer are you. A refinery hiring a process engineer and a biologics plant hiring a tech transfer engineer are reading for completely different evidence, and a resume written to cover both covers neither. The hiring manager is looking for three things in the first fifteen seconds - what you designed or operated and at what scale, which calculations you actually own rather than check, and whether you have worked inside a Process Safety Management program or only read about one. Scale is the part candidates leave out most often. A distillation column you specified at 20,000 barrels a day and a column you ran in a pilot skid are both real engineering, but they are not the same job, and a manager who cannot tell which one you did will assume the smaller. Put units, throughput, pressure and temperature ranges, and the service on the page. Then put the licensure track where it can be read: ABET degree, FE exam passed, EIT designation, PE Chemical if you hold it, with the state and license number in plain text. The rest of this page is how to build those three themes out, with a full sample resume at the end.

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Chemical engineer resume sample

The order a process engineering manager reads in: discipline and industry lane first, licensure and FE or PE status second, design and simulation work with scale third, process safety fourth, and plant results last because they are the part that is hardest to fake.

Industry lane declared immediately

Refining and petrochemicals, pharma and biotech, specialty chemicals, or food and beverage. Each has its own standards, its own regulators and its own vocabulary. Name yours in the headline and the summary so the reader stops guessing.

Design work with real scale

Column diameter and tray count, exchanger duty and area, pump head and flow, reactor volume, throughput in the units the plant uses. A design claim with no magnitude attached reads as coursework.

Process safety as a named program

OSHA Process Safety Management under 29 CFR 1910.119 has fourteen elements, and a candidate who has owned any of them says which. HAZOP participation is common, HAZOP facilitation is rarer and worth stating separately.

ATS friendly

Single column, standard headings, and the software spelled exactly as postings spell it - Aspen Plus, Aspen HYSYS, AutoCAD, MATLAB. Write out Professional Engineer alongside PE and Engineer in Training alongside EIT, because keyword matching is string matching.

Sample resume text

Use it as a reference: keep the structure and wording, put in your own facts and numbers.

Daniel Reyes

Process Engineer (Chemical) - PE
Baton Rouge, LA
daniel.reyes.pe@example.com
(225) 555-0164
linkedin.com/in/example

Profile

Process Engineer with 6 years in continuous specialty chemicals, Baton Rouge LA. Own heat transfer and separations for a 180,000 tonne a year intermediates unit: 42-tray atmospheric column, three shell-and-tube trains, a thermal oxidizer and two centrifugal pump systems. Built and maintain the Aspen Plus model of record for the unit, validated to within 3% on overhead composition against DCS data. Completed a pinch study that cut reboiler steam demand by 14%. Licensed Professional Engineer (PE), Chemical, Louisiana PE #41287. Facilitated 4 HAZOPs and own two PSM elements, mechanical integrity and management of change.

Experience

Senior Process Engineer03/2022 - present

Delta Reach Chemicals, Baton Rouge, LA

  • Process owner for the separations and heat transfer section of a 180,000 tonne a year continuous intermediates plant, covering a 42-tray atmospheric column, three shell-and-tube exchanger trains and the associated pump and reflux systems
  • Rebuilt the unit Aspen Plus model, validated it against six months of DCS data to within 3% on overhead composition, and made it the model of record used for all unit case studies
  • Ran a pinch analysis that justified a feed-effluent exchanger and reduced reboiler steam demand by 14%, confirmed over three months of post-installation operation
  • Facilitated four HAZOPs on a $7.4M debottleneck project, closed 61 recommendations through management of change, and led the pre-startup safety review
  • Resized 23 pressure relief devices to API 520 and API 521 during a relief system reconciliation, and corrected two undersized cases found in the legacy documentation
  • Diagnosed intermittent column flooding as entrainment from a fouled feed preheater rather than a tray problem, avoiding an unnecessary tray replacement in the turnaround scope
Process Engineer07/2019 - 02/2022

Harrowgate Specialty Materials, Beaumont, TX

  • Supported two batch reaction trains and a vacuum dryer, writing and revising 14 operating procedures and running the management of change queue for the area
  • Scaled a new esterification product from a 20 L bench vessel through a 400 L pilot reactor to a 12,000 L production train, including heat removal and agitation checks at each step
  • Built the unit mass balance in Aspen Plus and used it to identify a 6% solvent loss to the vent scrubber, recovered by a condenser change
  • Participated in six what-if PHAs and three HAZOPs as the process subject matter expert, and completed a dust hazard analysis on the powder handling area
  • Ran capability studies on two critical quality attributes and brought both from Cpk below 1.0 to above 1.33 through control loop retuning and a feed sequence change
Process Engineering Co-op05/2018 - 12/2018

Vantris Refining Services, Lake Charles, LA

  • Reconciled instrument and lab data for a hydrotreater unit and rebuilt the daily heat and material balance spreadsheet used by the shift engineers
  • Marked up 38 P&ID sheets against field verification walkdowns and logged the discrepancies for drawing revision

Education

Louisiana State University2015 - 2019

BS Chemical Engineering, ABET-accredited program

Skills

Mass and energy balances, steady state and dynamicAspen Plus and Aspen HYSYS modeling and validationP&ID and PFD development, line and control valve sizingDistillation design and troubleshootingHeat exchanger specification, rating and pinch analysisPump and compressor selection, NPSH and hydraulicsPressure relief and flare sizing to API 520 and API 521OSHA PSM 29 CFR 1910.119, HAZOP facilitation, LOPA and SILDCS operation, control loop tuning, statistical process controlAutoCAD, MATLAB and Python for process data analysis

Licensure and Certifications

  • Licensed Professional Engineer (PE), Chemical - Louisiana PE #41287, 2024
  • Fundamentals of Engineering (FE) exam, Chemical - passed 2019; Engineer in Training (EIT), Louisiana
  • HAZOP Leader training - 2022
  • LOPA and SIL determination course - 2023
  • Six Sigma Green Belt - 2021
  • OSHA Process Safety Management refresher - annual since 2019
  • Member, American Institute of Chemical Engineers (AIChE)

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What you get

  • A complete chemical engineer resume sample
  • 3 PDF templates
  • How to write process design work with scale, units and service
  • 6 mistakes that get chemical engineering resumes screened out
Profile

Chemical engineer profile summary

Four lines, no more. Years of experience, the industry lane, the process area you know best, your licensure status, and one or two outcomes with numbers. The reader is deciding whether to spend another thirty seconds on your experience section, and the thing that buys that thirty seconds is specificity about what you have run or designed.

Name the unit operations rather than the job title. A manager who needs someone who understands fractionation, fired heaters and hydrotreating will respond to those words; they will not respond to responsible for process improvement initiatives. If you have crossed between batch and continuous operation, say so explicitly, because that transition is harder than it looks on paper and hiring managers know it.

WeakResults-driven chemical engineer with strong analytical skills and experience in process optimization. Proven track record of improving efficiency and working effectively in cross-functional teams. Seeking a challenging role with a growing company.
StrongProcess Engineer, 6 years in continuous specialty chemicals, Baton Rouge LA. Own the heat transfer and distillation side of a 180,000 tonne a year intermediates plant: 42-tray atmospheric column, three shell-and-tube trains and a thermal oxidizer. Built and maintain the Aspen Plus model used for the unit's heat and material balance, and completed a pinch study that cut steam demand on the reboiler loop by 14%. Licensed Professional Engineer (PE), Chemical, Louisiana PE #41287. Facilitated four HAZOPs and own two PSM elements: mechanical integrity and management of change.
Tip
Write the simulation tool and what you did with the model in the same sentence. Built, validated against plant data and maintained is a different skill from opened an existing model, and only the first one survives a technical interview.
Skills

Chemical engineer skills for a resume

Keep this a plain list, not a graphic with filled bars - the bars are images and carry no text to be matched. Group by calculation, simulation, safety and plant systems, and name every software package the way job postings write it.

Hard skills

  • Mass and energy balances, steady state and dynamic, hand-calculated and reconciled against plant data
  • Process simulation in Aspen Plus and Aspen HYSYS, including property method selection, column convergence and sensitivity studies
  • Process flow diagram and P&ID development and markup, line sizing, hydraulics and control valve sizing
  • Distillation design and troubleshooting: tray and packed columns, reflux ratio, efficiency, flooding and weeping diagnosis
  • Heat exchanger specification and rating, shell-and-tube and plate, fouling allowance, and pinch analysis for heat integration
  • Pump, compressor and blower selection, NPSH checks, system curves and cavitation troubleshooting
  • Pressure relief and flare system sizing to API 520, API 521 and ASME Boiler and Pressure Vessel Code Section VIII requirements
  • OSHA Process Safety Management under 29 CFR 1910.119: process hazard analysis, mechanical integrity, management of change, pre-startup safety review, operating procedures
  • HAZOP and what-if PHA participation and facilitation, LOPA studies, SIL determination and safety instrumented function definition
  • Scale-up from bench to pilot to production, batch and continuous, DCS operation and basic regulatory control tuning, statistical process control and capability studies

Soft skills

  • Explaining a process constraint to operators in the control room without talking down to them
  • Standing behind a calculation when a schedule-driven conversation wants a different answer
  • Writing a deviation or incident narrative that is honest enough to be useful in the investigation
  • Facilitating a HAZOP where two experienced people disagree about a credible scenario
  • Handing a change over to maintenance and operations so it survives after you leave the area
  • Knowing when a model is good enough and when a field measurement is needed instead
  • Working a turnaround or startup through night shifts without quality of decision dropping
  • Saying no to a non-conforming change that has not been through management of change
  • Teaching a technician enough of the why that they catch the next problem themselves
  • Keeping the lab, process and quality groups aligned during a tech transfer
Experience

How to write chemical engineering experience

Formula: the unit and its scale, the calculation or design you owned, the tool you used, and what changed in production, yield, energy or safety terms. Supported process improvement projects is the job description read back. Reduced reboiler steam by 14% on a 42-tray column after a pinch study, verified over three months of plant data is engineering.

Separate the three kinds of work managers hire for, because they are evaluated differently. Design and capital project work: basis of design, equipment specification, vendor bid review, HAZOP, commissioning. Plant and sustaining work: troubleshooting, debottlenecking, yield and reliability, operating procedure revisions. Safety and compliance work: PHA cycles, relief valve studies, PSM element ownership, environmental reporting. If you have done all three, give each its own bullets rather than mixing them.

Weak- Used simulation software to model processes and worked with the team to optimize plant operations and improve safety.
Strong- Rebuilt the unit Aspen Plus model for the intermediates column train, validated it against six months of DCS data to within 3% on overhead composition, and used it to run a pinch analysis that justified a feed-effluent exchanger and cut reboiler steam demand by 14%, confirmed over three months of post-installation operation.
What to include
Unit and throughput - process area and service - what you calculated or specified - software named as postings name it - PSM elements you owned - PHA cycles facilitated or participated in - capital value of projects you supported - yield, energy, reliability or rate change with the period it was measured over.
Education

Education, licensure and certifications

A bachelor's degree in chemical engineering from an ABET-accredited program is the normal prerequisite, and it matters enough to write the accreditation out when your school is not nationally recognizable. The licensure path is the same across disciplines: pass the Fundamentals of Engineering exam administered by NCEES, which in most states lets you use the Engineer in Training or Engineer Intern designation, accumulate the qualifying experience your state board requires - typically four years under a licensed Professional Engineer - then sit the PE Chemical exam. The license itself is issued by a state board, not nationally, so write the state and the number. If you are licensed in more than one state, say which, and if you maintain an NCEES Record for comity applications, that is worth a line because it tells a multi-state employer you are cheap to add in a new jurisdiction.

  • BS or MS Chemical Engineering, ABET-accredited program, with graduation year and GPA if you are within a few years of graduating
  • Fundamentals of Engineering (FE) exam, Chemical module, with the year passed, and your Engineer in Training (EIT) or Engineer Intern certificate number if your state issues one
  • Licensed Professional Engineer (PE), Chemical - state and license number, in a plain text line, plus any comity licenses
  • NCEES Record maintained, if you have one, for multi-state licensure
  • OSHA Process Safety Management training, HAZOP leader or PHA facilitation training, and any LOPA or SIL course with the provider
  • Six Sigma Green Belt or Black Belt, or a formal statistical process control course, with the year
  • AIChE membership and Center for Chemical Process Safety course work, ISA instrumentation courses, or cGMP training if you work in pharma
  • Specific software training you can prove: Aspen Plus or HYSYS courses, DCS vendor training, or a named CFD or FEA tool
Careful
Do not put proprietary process conditions, recipes, catalyst formulations or yields that are not public on a resume. Describe the service and the scale generically - a hydrotreater, a continuous esterification, a 2,000 L fed-batch fermentation - and keep the numbers you quote to things like your own project outcomes rather than licensed process data.
No experience

Entry level chemical engineer resume with no industry experience

A new graduate competes on three things: the FE exam, the design and lab work that most resembles plant work, and any co-op or internship time, however short. Pass the FE before you apply if you possibly can - it is the single clearest signal that you intend to be licensed, and it moves you past candidates who have the same degree and nothing else.

Then raise the senior design project to the level of a real job entry. It is usually the only place a new graduate has done a full mass and energy balance, sized equipment, costed a plant and defended the result. Write it with the feed and product, the capacity, the unit operations, the simulation tool, and the economic conclusion. Unit operations lab counts too, provided you say what you measured and on what rig: tray efficiency on a bubble-cap column, overall heat transfer coefficient on a double-pipe exchanger, residence time distribution in a CSTR.

  • FE exam Chemical passed, with the year, and EIT certificate if your state issues one, placed near the top
  • Senior or capstone design project written as an entry: feed and product, design capacity, unit operations, simulation tool, capital and operating cost estimate, and what you personally owned
  • Unit operations laboratory experience named by rig and measurement rather than by course number
  • Co-op, internship or undergraduate research with the plant or lab scale stated, even if the task was data reconciliation or a mass balance audit
  • Software you can genuinely use unsupervised: Aspen Plus or HYSYS, MATLAB or Python for data work, AutoCAD for P&ID markup, and Excel modeling of any depth

Ready to write your chemical engineer resume?

The builder keeps your licensure line, simulation tools and process safety experience in plain parseable text, where a hiring manager and a screening system will both find them.

Mistakes

Common mistakes

No scale anywhere on the page

Designed a distillation column could mean a 60-tray refinery fractionator or a lab-scale rig. Diameter, tray count, feed rate, operating pressure and the service turn the same sentence into evidence. Without magnitude, the reader defaults to assuming the smallest plausible version.

A resume written for every industry at once

Refining, pharma, specialty chemicals and food have different regulators, different standards and different hiring criteria. A summary that tries to cover all of them signals that you have not committed to any, and gives the reader nothing to match against the posting.

Process safety mentioned as an attitude

Safety conscious is not a qualification. Named PSM elements, PHA cycles, relief valve studies to API 520 and 521, LOPA work and SIL determination are. If you facilitated rather than attended, say facilitated - it is a different skill and it is scarcer.

Simulation listed as a logo, not a competence

Aspen Plus in a skills graphic tells the reader nothing about whether you can select a property method, converge a column or defend the model against plant data. Put the tool inside a bullet that says what you built with it.

Confidential process data on the resume

Catalyst formulations, proprietary yields, unpublished operating conditions and customer names do not belong on a resume. It reads as a confidentiality risk to the next employer, which is exactly the opposite of the impression you want.

A two-column or graphic layout

Chemical engineering roles are often screened automatically before a human sees anything. Two-column layouts get read across the gutter, skills charts are images with no text, and a headline inside a header graphic is invisible. Single column, standard headings, consistent MM/YYYY dates.

Takeaways

Takeaways

Remember

  • Declare the industry lane in the headline
  • Every design claim carries scale and service
  • FE, EIT, PE Chemical with state and number in plain text
  • Name PSM elements and PHA role, not safety as a value
  • Simulation tools inside bullets that say what you built
  • Single column, standard headings, no confidential process data
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FAQ

Frequently asked questions

For most industrial process engineering roles, no - a great many chemical engineers in refining, chemicals and pharma never become licensed, because the industrial exemption in many states covers work done for an employer's own facilities. The license matters when you offer engineering services to the public, sign and seal documents, work in consulting or forensic practice, or hold a role where a state board or a client requires it. Even where it is not required, PE Chemical is read as a seriousness signal, and the FE exam alone is worth passing early because eligibility rules get harder to satisfy the longer you wait.
Say what you did with the model, not that you have the software. Built a model from a PFD and converged it, selected and justified a property method for a non-ideal system, validated against plant data to a stated tolerance, ran a sensitivity or case study that supported a decision, or maintained the model of record for a unit. All of those are different competence levels, and a technical interviewer will find out which one you are within a few questions, so state the real one.
Evidence that you have worked inside a Process Safety Management program rather than near one. The strongest version names elements of 29 CFR 1910.119 you owned or contributed to - process hazard analysis, mechanical integrity, management of change, pre-startup safety review, operating procedures, contractor safety - and says how many PHA or HAZOP cycles you have been through and in what role. Relief system work sized to API 520 and API 521, LOPA studies and SIL determination are all specifics worth their own lines. If you work with combustible powders, dust hazard analysis belongs here too.
The title should match the posting, because keyword matching is literal, but the content largely overlaps. Process engineer postings lean harder on plant sustaining work, troubleshooting, debottlenecking and operating discipline. Chemical engineer and process design engineer postings lean toward basis of design, equipment specification, simulation and capital projects. Keep one master resume with both sets of bullets and lead with the half that matches the posting.
Lead with the engineering fundamentals that transfer and be honest about the ones that do not. Mass and energy balances, heat transfer, fluid mechanics, relief sizing, P&ID literacy and PSM thinking travel across industries. What does not travel automatically is the regulatory frame - cGMP, validation and tech transfer on one side; refining unit knowledge, API standards practice and continuous operating discipline on the other. Name the transferable work first, acknowledge the gap plainly, and point at any course work or standards familiarity you have in the target industry.
FE exam status, then the capstone design project written like a job. The design project is usually the only place a graduate has carried a full mass and energy balance, sized equipment, estimated capital and operating cost and defended the result against questioning, which is a reasonable preview of early-career work. Write the feed and product, the design capacity, the unit operations, the simulation tool and your specific scope within the team. Unit operations lab work comes next, described by rig and measurement.
One page for the first few years, two pages once you have real project and plant history worth describing. Two pages is normal and expected for a mid-career process engineer with capital projects, PHA history and multiple units behind them, and cramming that onto one page by deleting the scale numbers is a bad trade. Three pages is only reasonable in consulting or research contexts where a project or publication list is genuinely part of the credential.
Yes - the full sample above, and all the templates on this page. You can assemble your own resume from any of them in the builder for free and see the result; downloading the finished PDF is paid, by subscription or a one-time payment. The templates keep a single-column structure and plain text headings, which matters because engineering applications are routinely parsed by software before anyone reads them.
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