How much does a control and valve installers and repairers make?

The median control and valve installers and repairers salary in the United States is $74,340 per year ($35.74/hour). Salaries range from $45,910 (10th percentile) to $112,500 (90th percentile). There are 48,240 control and valve installers and repairers jobs in the U.S. Source: Bureau of Labor Statistics OEWS.

Which state pays control and valve installers and repairerss the most?

The highest paying state for control and valve installers and repairerss is Rhode Island at $110,900 median salary.

Is control and valve installers and repairers a good career?

Control and Valve Installers and Repairers employment is projected to grow 1.3% from 2024 to 2034 (slower than average). There are approximately 3,900 job openings per year. Typical education required: High school diploma or equivalent.

What interview questions are asked for control and valve installers and repairers roles?

Common control and valve installers and repairers interview questions include: "Walk me through a control-valve rebuild — Fisher easy-e globe valve on a critical-service loop.", "Describe your approach to PSV testing under the NBIC VR-stamp program.", "Describe a safety incident or near-miss you handled.". Interview format at top employers ranges from behavioral panels (STAR method) to technical case rounds — for example Petroleum Refining Majors (ExxonMobil, Chevron, Marathon Petroleum, Valero, Phillips 66, HF Sinclair, PBF Energy, Delek US) typically uses 3-5 rounds over 4-8 weeks.

What certifications should control and valve installers and repairerss get?

Top-ROI certifications for control and valve installers and repairerss: ISA CCST (Certified Control Systems Technician) Level I / II / III ($500 per level exam + $300-500 prep material; 60-90 hr study; ISA member $150-300 annual dues); ISA CAP (Certified Automation Professional) ($500 exam + $400-800 prep); API 570 (Piping Inspector) + API 510 (Pressure Vessel) + API 653 (Aboveground Storage Tank) ($1,200-2,500 per exam + $500-1,500 prep material; 100-160 hr study each).

How do you negotiate a control and valve installers and repairers salary?

Anchor on documented market data (BLS median $74,340, p75 $97,120), specific outcomes you've delivered, and the specific band for your years of experience. Given 8 years across I&E Apprentice, Journeyman I&E Tech, and Valve Tech II at Marathon Petroleum Galveston Bay Refinery — ISA CCST Level II + API 570 Piping Inspector + Emerson Fisher DVC / Control Valve certified + TÜ...

Control and Valve Installers and Repairers Salary

Q: What is the career ladder for control and valve installers and repairerss?

The typical control and valve installers and repairers career ladder: I&E Apprentice / Instrumentation Helper / Valve Shop Tech I (0-4 yrs, $48-62k hourly + $1.50-3.50/hr shift diff + OT + full benefits + USW / UA / IBEW pension where applicable) → Journeyman I&E Tech / Valve Tech II (3-8 yrs, $65-88k hourly + shift diff + $10-20k OT + full benefits + USW / UA / IBEW pension where applicable) → Sr I&E Tech / Shop Foreman / PSV Certified Technician (8-16 yrs, $85-115k hourly or salaried + shift diff + $15-25k OT + $6-12k bonus + LTIP at Fortune-500) → Instrumentation Supervisor / Reliability Engineer / Corporate I&E SME (15-25 yrs, $115-175k+ salaried + 10-15% bonus + LTIP + $18-35k RSU refresh + full benefits at Fortune-500).

Bureau of Labor Statistics title: Control and Valve Installers and Repairers, Except Mechanical Door

The median control and valve installers and repairers salary in the United States is $74,340 per year ($35.74/hour). Salaries range from $45,910 at the entry level to $112,500+ for the top 10% of earners. There are 48,240 control and valve installers and repairers jobs nationwide. Employment is projected to grow 1.3% through 2034.

Last updated: June 2026 · Source: U.S. Bureau of Labor Statistics

Median Salary

$74,340

per year

Hourly Rate

$35.74

per hour

Employment

48,240

jobs in the U.S.

Salary Distribution

10th percentile

$45,910

25th percentile

$54,950

Median

$74,340

75th percentile

$97,120

90th percentile

$112,500

Job Growth (2024-2034)

+1.3%

Slower than average

Annual Openings

3,900

jobs/year (growth + replacements)

Education Required

High school diploma or equivalent

Training Needed

Moderate-term on-the-job training

Control and Valve Installers and Repairers Career Guide

Interview questions, resume templates, and a career ladder written specifically for control and valve installers and repairerss.

Control and valve installers and repairers (BLS SOC 49-9012) service the industrial control valves, safety valves, actuators, positioners, and instrumentation loops that regulate flow, pressure, level, and temperature across refineries, chemical plants, pharmaceutical manufacturing, power generation, and pipeline systems. Typical seats: valve-shop technicians at OEM service centers (Emerson Fisher, Flowserve, Metso Neles, Samson, Baker Hughes Masoneilan, Cameron Valves, CIRCOR, Weir Minerals); refinery + petrochemical instrument-and-valve techs at ExxonMobil, Chevron, Marathon Petroleum, Valero, Phillips 66, Shell, BP; chemical-plant instrument techs at Dow, LyondellBasell, INEOS, BASF, Eastman, Celanese; pharma / API manufacturing at Merck, Pfizer, Lilly, Amgen, Regeneron under 21 CFR Part 210/211 GMP; power generation at Duke Energy, Southern Company, NextEra, TVA; pipeline / midstream at Kinder Morgan, Enterprise Products, Enbridge, Williams. Instruments in daily use — smart-valve positioners (Emerson FieldVue DVC6200 with HART / Foundation Fieldbus / Profibus / WirelessHART), pressure safety valves (Anderson Greenwood, Consolidated, Crosby), control valves (Fisher easy-e, Flowserve Valtek, Metso Neles ball and butterfly), pneumatic and electric actuators (Rotork, Bettis, Limitorque, Auma), transmitters (Rosemount 3051 pressure, Rosemount 5300 radar, Micro Motion Coriolis), calibrators (Beamex MC6, Fluke 754, GE Druck DPI 620). Credentials — ISA (International Society of Automation) CCST (Certified Control Systems Technician) Levels I / II / III; ISA CAP (Certified Automation Professional); API 570 (Piping Inspector), API 510 (Pressure Vessel), API 653 (Aboveground Storage Tank); NBIC (National Board Inspection Code) authorized inspector for pressure safety valve certification; API RP 576 (Pressure-Relieving Devices) for PSV shop testing. BLS reports 48,240 employed with a median of $74,340, p10 ~$46,000, p90 $112,000+. Entry apprentice / helper $48-62k; established journeyman I&E / valve tech $65-88k; Sr tech / shop foreman $85-115k; specialty pressure-safety-valve certified technician + supervisor $105-145k+ at PSM-covered refineries and chemical plants. The single biggest earnings lever is stacking ISA CCST Level II or III + API 570 + NBIC PSV authorization and moving into a Sr I&E tech / shop foreman seat at an OSHA PSM 29 CFR 1910.119 covered refinery, chemical plant, or midstream facility where turnaround overtime + call premium routinely push total earnings to $135-175k+.

Core Skills Hiring Managers Screen For

Control valve service — Fisher, Flowserve, Metso Neles, Samson, Masoneilan

Field disassembly, inspection, and rebuild of globe / cage / ball / butterfly / rotary control valves. Trim replacement (plug, seat, cage, stem) with anti-galling stem-thread lubrication and torque-to-spec on packing gland. Air-set / bench-set on pneumatic actuators to match spring range. Leak class verification per FCI 70-2 / ANSI B16.104 (Class II shutoff at 0.5% of rated Cv, Class IV at 0.01%, Class V at 5 × 10^-4 mL/min per inch of orifice diameter × psi differential, Class VI bubble-tight for emergency isolation). Emerson Fisher easy-e / EZ / Vee-Ball, Flowserve Valtek Mark One / MaxFlo, Metso Neles top-entry ball, Samson 3241 globe, Baker Hughes Masoneilan 21000 / 41005 platforms. Trim-material selection (17-4 PH SS, stellite hardfacing, tungsten carbide) per fluid service.

Smart-valve positioner calibration (HART, Foundation Fieldbus, Profibus PA, WirelessHART)

Emerson FieldVue DVC6200 auto-calibration + manual travel-limit setup + partial-stroke test (PST) configuration for SIS-tagged valves per IEC 61511. Foundation Fieldbus configuration of the positioner function block (AO block, PID block linkage). HART Communicator (475 / 375 / 5150) diagnostics — device variable read, self-test, ValveLink diagnostic upload for signature analysis (dead band, stroke asymmetry, air-mass consumption trend). Profibus PA and WirelessHART network integration; understand IEEE 802.15.4 mesh topology for WirelessHART. Positioner-signature analysis is the emerging PdM discipline for valve reliability — signature deviation predicts stem-packing wear, seat degradation, actuator diaphragm rupture.

Pressure safety valve (PSV) testing + certification per API RP 576 and NBIC NB-23

Bench-testing PSVs at the valve shop with pop-testing rig — set pressure verification within ±3% (spring loaded) or ±1% (pilot operated), blowdown verification, seat leakage per API 527 (bubble test at 90% of set pressure). Nozzle / disc / spring inspection and rebuild. Backpressure calculation for balanced-bellows PSVs. NBIC (National Board Inspection Code) NB-23 Part 3 requirements for PSV repair — VR stamp authorization from the National Board, repair traceability documentation, certified capacity re-rating. API RP 576 test intervals — 5-year default for most refinery / chemical service, 3-year for corrosive / fouling service, 10-year for clean-service. Field trevi-testing where the PSV cannot be removed to shop (limited to specific service conditions). Documentation per PSM Element 8 Mechanical Integrity.

Pneumatic and electric actuator service (Rotork, Bettis, Limitorque, Auma)

Spring-diaphragm and piston pneumatic actuators — diaphragm inspection, spring range verification, air-supply plumbing (0-10 / 3-15 / 6-30 psig ranges), volume booster + positioner integration. Rotary electric actuators (Rotork IQ / IQT / CVA, Limitorque MX / QX, Auma SA / SAR / SQ, Bettis EHO / EM) — motor / gearbox lubrication, torque and travel limit switch setup, position transmitter (potentiometer or absolute encoder) calibration. Solenoid valves (ASCO, Rexroth, SMC) — pilot solenoid, tripping-relay logic, redundant-configuration on SIS valves. Fail-safe direction verification (fail-open FO vs fail-closed FC vs fail-in-last-position FLP) per the valve tag and P&ID.

Loop calibration — transmitter to control valve end-to-end

5-point loop calibration (0%, 25%, 50%, 75%, 100%) using Beamex MC6 or Fluke 754 documenting calibrators. Trace signal from field transmitter (Rosemount 3051 pressure, Rosemount 5300 radar level, Micro Motion Coriolis flow, Rosemount 848T RTD temperature) through the DCS / PLC (Honeywell Experion, Emerson DeltaV, Yokogawa CENTUM, Rockwell ControlLogix) to the valve positioner and back via position feedback. Verify controller PID action + scaling + engineering units + valve direction. HART-loop-check with signal simulation at the transmitter and readback at the DCS console. Loop-cal certification traceable to NIST via ANSI/NCSL Z540.3.

OSHA PSM 29 CFR 1910.119 + Mechanical Integrity discipline

PSM covered facilities require documented mechanical-integrity program (Element 8) — inspection intervals, test procedures, deficiency-tracking, work-order documentation via SAP PM / IBM Maximo / Infor EAM. Control valve and PSV work is safety-critical at PSM covered facilities; deficiencies must be corrected before returning to service. Management of Change (MOC — Element 10) required for any valve trim change, spring range change, or set pressure adjustment. Pre-Startup Safety Review (PSSR — Element 7) after turnaround valve work. Incident Investigation (Element 11) on any PSV lift, valve failure, or release event. Contractor training (Element 6) required for third-party valve-shop personnel entering the facility. LOTO per 29 CFR 1910.147 for every valve service — mechanical + electrical + pressure + thermal isolation with verification.

SIS (Safety Instrumented System) valve service per IEC 61511 + partial-stroke testing

SIS-tagged valves (typically fail-safe ESD block valves, blowdown valves, HIPPS valves) require IEC 61511 discipline — proof-test at required interval (typically 12-24 months) per Safety Integrity Level (SIL 1-4). Partial-Stroke Test (PST) via smart positioner (Emerson FieldVue DVC6200 SIS variant) at 10-25% stroke without process disruption; documented per SIS Safety Manual. Full-stroke functional-safety test at scheduled turnaround. TÜV / exida Certified Functional Safety Engineer or Technician (FS Eng / FS Tech) credential is preferred at SIS-heavy refineries and chemical plants (typically Sabic, INEOS, BASF, Merck fine chemicals, LyondellBasell).

Valve-shop work + turnaround planning

Turnaround (T/A) valve work — refinery / chemical plant unit shutdowns every 3-6 years generate 6-14 weeks of intensive valve-shop and field-valve work. Coordinate with T/A planning on scope of valves to be pulled, shop-repair timeline, PSV re-certification schedule, spare-valve inventory (typical refinery holds 25-40% spare inventory on critical service). Track parts (trim kits, packing sets, gaskets, springs, diaphragms) against OEM lead times (typically 4-16 weeks for critical trim). Manage the valve-tracker database (asset tag / physical location / last inspection date / next inspection due). Coordinate with third-party valve-service contractors (VR Anderson, MST — Machine Support Technology, Valve Repair Services).

How to Become a Control and Valve Installers and Repairers

1
Complete a high school diploma or GED plus vocational or military electronics / instrumentation training
HS diploma + strong math / mechanical aptitude. Military electronics / instrumentation training (Navy Fire Controlman, Air Force Electronic Systems Security Assessment, Army 25U Signal Support, Coast Guard ET) is a strong entry credential. Community-college instrumentation programs at Lee College (Baytown, TX), San Jacinto (Pasadena, TX), Alvin Community College (TX), Baton Rouge Community College, WVU Parkersburg, Delta College (MI) offer 12-24 month certificates or AAS Process Technology / Instrumentation Technology programs — $4-15k tuition, Pell Grant eligible.
2
Enter a state-registered instrument-and-electrical (I&E) apprenticeship or vendor training program
4-year I&E apprenticeship at UA (United Association of Plumbers and Pipefitters) Local, IBEW (International Brotherhood of Electrical Workers) Local, or a state-registered I&E program. Alternate — Emerson / Flowserve / Metso Neles service-center apprenticeships at $22-30/hr during the 3-4 year program. Refinery / chemical-plant I&E apprenticeships (ExxonMobil Baytown, Chevron Pascagoula, Dow Freeport, LyondellBasell La Porte, Merck Elkton) — typically 4-year programs paying $28-42/hr during apprenticeship + full benefits.
3
Start as I&E Apprentice / Instrumentation Helper / Valve Shop Tech I at $48-62k + shift diff + benefits
First seat — assist journeyman I&E techs on valve service, PSV testing, loop calibration, and field instrument troubleshooting. Learn the valve-shop workflow (disassembly, inspection, part-ordering, reassembly, bench-testing, documentation). Learn refinery / chemical plant PSM discipline. Shift differential $1.50-3.50/hr; overtime 1.5x above 40 hrs; USW / UA / IBEW pension eligibility at legacy plants.
4
Complete ISA CCST Level I + API 570 (Piping Inspector) or vendor certifications
ISA CCST (Certified Control Systems Technician) Level I — the recognized US control-systems credential; $500 exam + $300-500 prep material; 60-90 hr study. API 570 Piping Inspector — $1,200-2,500 exam + prep; requires 1-5 years qualifying experience depending on education. Vendor certifications — Emerson Fisher DVC / control valve certification, Flowserve Valve School, Metso Neles service certification. NBIC PSV Authorization for VR-stamp PSV repair — typically employer-sponsored through the shop's NBIC-authorized program.
5
Advance to Journeyman I&E Tech / Valve Tech II at $65-88k + shift diff + OT + LTIP eligibility
3-6 years in seat. Own end-to-end valve service — field diagnosis, LOTO, disassembly, shop-repair coordination, reassembly, calibration, return-to-service PSSR sign-off. Handle PSV testing at the shop under the NBIC VR-stamp program. Own smart-positioner calibration + PST configuration on SIS-tagged valves. Complete ISA CCST Level II + API 570 stack. Union plants at this rung typically clear $85-105k with OT + shift diff.
6
Layer on TÜV / exida FS Engineer + ISA CAP + NBIC advanced authorization
TÜV Rheinland / TÜV SÜD / exida CFSE (Certified Functional Safety Expert) — required at SIS-heavy chemical, oil-and-gas, refining, and pharma sites; $3,500-6,500 course + exam; 5 days; typically employer-paid. ISA CAP (Certified Automation Professional) — the recognized US automation credential; $500 exam + prep. NBIC NB-23 R-stamp or VR-stamp authorization program — required for shop-based PSV and pressure-vessel repair with NBIC certification. API 510 (Pressure Vessel Inspector) + API 653 (Aboveground Storage Tank Inspector) for tank-and-vessel-facing techs.
7
Advance to Sr I&E Tech / Shop Foreman at $85-115k + shift diff + OT + LTIP + bonus
8-15 years in seat. Own the plant's valve reliability program — PdM route with positioner-signature analysis, PSV test schedule, turnaround valve-scope planning, critical-spare inventory. Direct 4-8 I&E techs at the shop or field level. Interface with the Reliability Engineer and Process Engineer on chronic-failure valves and MOC on control-valve trim changes. Some plants layer this as a bargaining-unit Lead Tech classification; others move this seat into salaried Assistant Shift Supervisor.
8
Advance to Instrumentation Supervisor / Reliability Engineer / Corporate I&E SME at $115-175k+ + bonus + LTIP + RSU
12-25 years in seat. Own the site's instrumentation-and-controls function or the corporate valve / instrumentation reliability program. Direct-manage 10-25 I&E techs. Own capital-project planning for control-valve replacements and DCS migrations. Corporate SME roles at ExxonMobil, Chevron, Marathon Petroleum, Dow, LyondellBasell, Merck support 3-15 plants on best-practice valve reliability, SIS proof-testing, and turnaround planning. Some senior techs move into Emerson / Flowserve / Metso Neles applications-engineer or field-service-engineer roles at $115-165k + travel + benefits.

Career Progression

I&E Apprentice / Instrumentation Helper / Valve Shop Tech I

0-4 yrs$48-62k hourly + $1.50-3.50/hr shift diff + OT + full benefits + USW / UA / IBEW pension where applicable

•Assist journeyman I&E techs on valve service, PSV testing, loop calibration, and field instrument troubleshooting
•Own basic PM execution — grease actuator gearboxes, verify air-supply plumbing, replace air-set filters + regulators
•Complete plant CMMS work-order documentation with parts consumption and labor hours
•Complete LOTO / NFPA 70E / HAZWOPER / confined-space training in first 90 days

Next: Apprentice → Journeyman I&E Tech at 3-6 years with ISA CCST Level I + API 570.

Journeyman I&E Tech / Valve Tech II

3-8 yrs$65-88k hourly + shift diff + $10-20k OT + full benefits + USW / UA / IBEW pension where applicable

•Own end-to-end valve service — field diagnosis, LOTO, disassembly, shop-repair, reassembly, calibration, return-to-service
•Handle PSV testing at the shop under the NBIC VR-stamp program
•Own smart-positioner calibration + partial-stroke test configuration on SIS-tagged valves
•Handle loop calibration with Beamex MC6 or Fluke 754 documenting calibrators, traceable to NIST

Next: Sr I&E Tech / Shop Foreman at 8-15 years with ISA CCST Level II/III + TÜV FS Tech.

Sr I&E Tech / Shop Foreman / PSV Certified Technician

8-16 yrs$85-115k hourly or salaried + shift diff + $15-25k OT + $6-12k bonus + LTIP at Fortune-500

•Own the plant's valve reliability program — PdM route with positioner-signature analysis, PSV test schedule, turnaround valve-scope planning
•Direct 4-8 I&E techs at the shop or field level; own shift-level valve-service throughput
•Interface with the Reliability Engineer and Process Engineer on chronic-failure valves and MOC on control-valve trim changes
•Own critical-spare inventory (typical refinery holds 25-40% spare inventory on critical service)

Next: Instrumentation Supervisor / Corporate I&E SME at 15-25 years.

Instrumentation Supervisor / Reliability Engineer / Corporate I&E SME

15-25 yrs$115-175k+ salaried + 10-15% bonus + LTIP + $18-35k RSU refresh + full benefits at Fortune-500

•Own the site's instrumentation-and-controls function or the corporate valve / instrumentation reliability program
•Direct-manage 10-25 I&E techs; own hiring, performance reviews, and career-development for the team
•Own capital-project planning for control-valve replacements and DCS migrations
•Corporate SME variant — support 3-15 plants on best-practice valve reliability, SIS proof-testing, and turnaround planning

Next: I&E Manager / Sr Reliability Manager at 22+ years.

I&E Manager / Sr Reliability Manager / Chief Engineer

22+ yrs$155-235k+ salaried + 15-22% bonus + LTIP + $35-65k RSU refresh + full executive-adjacent benefits

•Own the enterprise instrumentation-and-controls function at a Fortune-500 refinery / chemical / pharma / power employer
•Direct-manage 3-8 Instrumentation Supervisors covering 8-30 plants
•Own the enterprise valve / PSV reliability strategy and the SIS lifecycle management program under IEC 61511
•Represent the enterprise externally at ISA, API, NBIC, and TÜV / exida functional-safety committee work

Interview Questions & Answers

5 free questions below. Career Kit unlocks 12 total plus resume bullets for every level.

Q1. Walk me through a control-valve rebuild — Fisher easy-e globe valve on a critical-service loop.technical

Structured. (1) LOTO — verify hydraulic / pneumatic / process isolation with double-block-and-bleed on high-hazard service; verify positive isolation with pressure-decay test. Apply personal locks per plant procedure. (2) Actuator removal — depressurize air supply, disconnect positioner instrument tubing, remove actuator-to-yoke bolts. (3) Bonnet removal — remove packing gland studs, retract stem, remove bonnet with lifting eyebolts. (4) Trim removal — remove plug, cage, seat ring, and stem assembly; inspect trim components for erosion / cavitation damage / galling. (5) Trim rebuild — replace worn components with OEM parts (Fisher 17-4 PH SS plug and stem, stellite-hardfaced seat ring, tungsten-carbide guide bushings for erosive service); replace packing set (typically PTFE V-ring for low temp, graphite / spiral-wound for high temp), gaskets, and bonnet spiral-wound gasket. (6) Reassembly — torque bonnet studs to spec per FCI 70-2 / OEM manual (typical 180-240 ft-lb on 2-inch valve), install packing, tighten packing gland to leak-test spec. (7) Actuator reinstall — align actuator to yoke, torque bolts, connect positioner + air supply. (8) Bench air-set — verify actuator spring range against nameplate. (9) Field commissioning — 5-point stroke check (0%, 25%, 50%, 75%, 100%) with positioner readback vs DCS command; verify leak class per FCI 70-2 (Class IV for shutoff, Class V for critical). (10) PSSR sign-off before return to service; document in CMMS with parts consumption and calibration certificate. Interviewers screen for candidates who name specific trim materials, specific FCI leak classes, and specific torque values.

Q2. Describe your approach to PSV testing under the NBIC VR-stamp program.technical

Structured. (1) NBIC (National Board Inspection Code) NB-23 Part 3 requirements for PSV repair — the shop must hold VR-stamp authorization from the National Board with documented procedures, qualified inspectors, and traceability. (2) Pre-test inspection — verify PSV tag information (set pressure, size, orifice designation, service classification, last test date). Visual inspection for corrosion, damage, and prior repair history. (3) Disassembly — remove bonnet, disc, spring, nozzle. Inspect seat / disc for wear, corrosion, or damage requiring machining or replacement. Inspect spring for corrosion and set-pressure drift. (4) Rebuild — replace seat / disc / spring per manufacturer parts specification. Lap seat / disc for bubble-tight seat leakage per API 527. (5) Bench pop-testing — test PSV on the shop pop-test rig with certified pressure gauge (traceable to NIST); verify set pressure within ±3% (spring-loaded) or ±1% (pilot-operated); verify blowdown (typical 7-10% for gas service); verify seat leakage at 90% of set pressure per API 527 bubble test. (6) Certification — apply VR stamp on the PSV nameplate; complete Form R-1 (Repair Report) with the National Board; retain shop records for the required retention period. (7) Field installation — verify orientation, verify no soft-seat contact damage during installation, verify piping stress on the inlet + outlet is within API 520 recommended limits. (8) Post-installation PSSR sign-off at PSM covered facilities per Element 7. Interviewers at shop foreman and Sr I&E Tech rounds screen for candidates who understand the NBIC VR-stamp discipline and the API 527 bubble-test methodology.

Q3. Describe a safety incident or near-miss you handled.behavioral

STAR. Situation: Journeyman I&E Tech at a Marathon Petroleum Galveston Bay Refinery working a scheduled turnaround on the Reformer PSV bank. Task: identify and report a near-miss during PSV removal. Action: (1) noticed on shift-turnover that the prior-shift crew had removed a PSV from a hydrocarbon service without executing the required nitrogen purge — the process line was still full of hydrocarbon; (2) executed emergency response — evacuated the immediate area, notified the shift supervisor within 5 min, coordinated with the PSM Compliance Officer; (3) verified with the Operations Console Operator that the process line was isolated at the block valves upstream and downstream; (4) coordinated a controlled nitrogen purge of the affected line before proceeding with PSV re-installation; (5) documented the near-miss in the plant's incident-tracking system per PSM Element 11 (Incident Investigation). Result: (a) near-miss triggered a root-cause meeting the next morning; the finding was that the prior-shift crew had bypassed the site's PSV-removal procedure because 'we always do it that way'; (b) the site updated the PSV-removal procedure to require a signed nitrogen-purge verification form before any PSV removal on hydrocarbon service; (c) the prior-shift crew was retrained on the site PSV procedure. Interviewers screen for candidates who own the near-miss report and follow through — a candidate who normalizes procedure bypass is a disqualifier at any credible refinery / chemical / pharma employer.

Q4. Why control valves / instrumentation rather than general electrical or mechanical trades?culture

Honest answer that resonates. 'I like the intellectual work — control-valve service sits at the intersection of mechanical (valve trim, actuator, packing), electrical (positioner, transmitter, DCS loop), pneumatic / hydraulic (air supply, actuator diaphragm, control line), and safety (SIS proof-testing, PSV certification). The differentiator is understanding all four well enough to diagnose a chronic loop-oscillation without swapping components. Pay is real — Journeyman I&E Tech at a Gulf Coast refinery with ISA CCST Level II + API 570 clears $85-108k with shift diff and OT, and the Sr I&E Tech / Shop Foreman track opens $115-145k. The trade is on-call rotation and turnaround overtime — that's fair. Long-term I want to move into a Sr I&E Tech seat at a PSM covered refinery or chemical plant, and I'm currently 2 of 3 into the ISA CCST Level II exam prep + API 570 exam application.' Interviewers screen for candidates who chose the specialty deliberately and understand the multi-disciplinary technology stack.

Q5. Where do you see your career in 5 years?closer

Show the fork clearly. Two tracks — bargaining-unit Sr I&E Tech (Sr Tech → Lead I&E → Shop Foreman with USW / UA / IBEW pension and full healthcare) or salaried Instrumentation Supervisor / Corporate I&E SME (Supervisor → Sr Reliability Engineer → I&E Manager at $135-215k+ with LTIP and RSU vesting). Say which you're leaning toward. Name the certifications you're building — ISA CCST Level I → II → III, ISA CAP, API 570 / 510 / 653, NBIC VR-stamp PSV authorization, TÜV / exida FS Tech / FS Eng. Name the target employer tier — ExxonMobil, Chevron, Marathon Petroleum, Valero, Phillips 66, Dow, LyondellBasell, Merck, Lilly, Emerson / Flowserve / Metso Neles field-service-engineer role. Interviewers screen for candidates who've thought through the specific path and pay ladder.

Resume Template — Journeyman I&E Tech / Valve Tech II (3-8 yrs)

Copy these bullets into your resume as a starting point. Career Kit includes bullets for every level of the ladder.

Journeyman I&E Tech / Valve Tech II (3-8 yrs)

▸Journeyman I&E Tech at Marathon Petroleum Galveston Bay Refinery on the Reformer + Isomerization units; own valve service, PSV testing, and loop calibration across 480 control valves and 240 PSVs.
▸Delivered a 24% reduction in unplanned control-valve downtime over 18 months through structured PdM route (Emerson FieldVue positioner-signature analysis) and turnaround scope planning.
▸NBIC VR-stamp PSV certified technician; ran 148 PSV bench-tests in FY24 with zero API 527 seat-leakage failures on return-to-service.
▸ISA CCST Level II + API 570 Piping Inspector + Emerson Fisher DVC / Control Valve certified + NFPA 70E + HAZWOPER 40-hr. $88k base + $3.50/hr shift diff + $18k FY24 OT + USW pension + full benefits + 401(k) match to 8%. Total FY24 earnings $115k.

What Gets You Rejected

✗Cannot execute LOTO per 29 CFR 1910.147 with block-and-bleed on high-hazard service — automatic disqualifier at any PSM covered facility.
✗History of PSV set-pressure drift or API 527 seat-leakage failures on return-to-service — signals the tech doesn't understand the NBIC VR-stamp discipline.
✗Cannot describe FCI 70-2 leak class or specific-trim material selection — vague 'I rebuild valves' answers without material and standard specificity.
✗No ISA CCST or API 570 credentials after 4+ years of I&E tenure — signals candidate hasn't done the credentialing work.
✗History of MOC (Management of Change) violations on control-valve trim changes or PSV set-pressure adjustments — a repeat MOC violation is a termination event at any PSM covered chemical, pharma, or refinery.
✗Weak DCS / PLC loop-calibration discipline — cannot trace signal from field transmitter through DCS to valve positioner and back via position feedback.
✗Attendance-policy violations — union I&E plants have a written attendance-point system, and repeat violations bar promotion regardless of technical competence.

Salary Negotiation Levers

✓OSHA PSM facility premium — the same I&E seat at an OSHA PSM covered refinery / chemical / pharma facility pays 25-45% above the same seat at a general manufacturing plant; the premium reflects HAZWOPER, PSM familiarization, and elevated safety-training investment.
✓Union representation — USW (which absorbed PACE), UA (Plumbers and Pipefitters), IBEW, and ICWUC at many refineries and chemical plants typically deliver a 15-30% wage premium plus defined-benefit pension (still available at USW-refinery employers) or defined-contribution 401(k) with 6-10% employer match and full healthcare against non-union employers.
✓ISA CCST Level II or III + API 570 stack — adds $4-9k at Journeyman promotion and $8-15k at Sr I&E Tech promotion at Fortune-500 refinery / chemical employers.
✓TÜV / exida FS Tech or FS Eng credential — adds $8-18k at SIS-heavy oil-and-gas, chemical, or pharma sites; required at IEC 61511 SIL-2/SIL-3 systems.
✓NBIC VR-stamp PSV authorization — adds $6-12k at shop-based tech seats and unlocks the PSV specialty premium at NBIC-authorized shops.
✓Shift differential — 2nd-shift typically $1.50-3.00/hr; 3rd-shift and rotating typically $2.00-4.00/hr; weekend / continuous-operations differential often adds another $1-2/hr.
✓Turnaround OT premium — refinery and chemical turnarounds every 3-6 years generate 6-14 weeks of elevated OT ($25-55k additional earnings) for I&E techs on the turnaround crew; some sites pay a turnaround-completion bonus of $3-15k.
✓OEM field-service-engineer premium — moving from plant-side Journeyman to Emerson / Flowserve / Metso Neles field-service-engineer typically adds $18-35k with company vehicle + per-diem + travel; the trade is 40-70% travel.
✓Sign-on bonus and relocation — Marathon Petroleum, ExxonMobil, Chevron, Dow, LyondellBasell routinely pay $5-18k sign-on and $8-20k relocation for Sr I&E Tech and Shop Foreman hires from out-of-metro.
✓Tuition reimbursement — Section 127 caps at $5,250/yr federal tax-free; Fortune-500 refinery and chemical employers routinely top this up for AAS Process Technology / Instrumentation Technology and BS Chemical Engineering Technology at $10-20k/yr.

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Control and Valve Installers and Repairers Salary by State

Best Cities (cost-adjusted) →

Salary Map — Click a state for details

$49K

$111K■ No data

Top Paying States

Vertical line = national median. Click a state for full details.

State	Median	vs. National	Employment
Rhode Island	$110,900	+49.2%	110
Alaska	$109,450	+47.2%	30
Connecticut	$104,690	+40.8%	360
North Dakota	$103,580	+39.3%	270
Washington	$102,870	+38.4%	450
New York	$101,150	+36.1%	4,170
California	$100,260	+34.9%	4,310
Wyoming	$100,030	+34.6%	290
District of Columbia	$98,810	+32.9%	50
South Dakota	$98,090	+31.9%	150

Showing 1–10 of 51

Control and Valve Installers and Repairers Salary by Metro Area

Metro Area	Median	vs. National
Modesto, CA	$133,990	+80.2%
Fresno, CA	$132,360	+78.0%
Sacramento-Roseville-Folsom, CA	$131,120	+76.4%
San Francisco-Oakland-Fremont, CA	$130,800	+75.9%
San Jose-Sunnyvale-Santa Clara, CA	$115,460	+55.3%
Bridgeport-Stamford-Danbury, CT	$108,940	+46.5%
Stockton-Lodi, CA	$105,800	+42.3%
Hartford-West Hartford-East Hartford, CT	$105,450	+41.8%
San Diego-Chula Vista-Carlsbad, CA	$104,840	+41.0%
New York-Newark-Jersey City, NY-NJ	$103,780	+39.6%

Showing 1–10 of 175

Data Source: U.S. Bureau of Labor Statistics, Occupational Employment and Wage Statistics (OEWS). Data reflects the most recent annual survey.

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A control and valve installers and repairers earning $74,340/year would need 802 years to match Stephen Curry's NBA salary, or 861 yearsto match Patrick Mahomes' NFL contract.

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