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Category  >>  Operational Questions  >>  What are the steps in conducting well stimulation?
OPERATIONAL QUESTIONS
Updated : September 17, 2025

What are the steps in conducting well stimulation?

Published By Rigzone

At-a-Glance

Conduct well stimulation via a closed-loop workflow: candidate and diagnostics ? treatment design and execution plan ? HSE and equipment readiness ? step-rate/minifrac or injectivity test ? main treatment (pad/breakdown ? placement ? flush) ? controlled cleanup/flowback ? post-job evaluation and surveillance.

I. Objective Definition and Key KPIs

Assumptions (estimated): onshore vertical or moderately deviated oil/gas well; reservoir depth 2,000–3,000 m; stimulation type selected based on rock type (matrix acid for carbonates, HF/Mud acid for sandstones; hydraulic fracturing for tight formations).

  • I.1 Objectives
    • 1.1 Reduce skin and increase inflow; connect more reservoir volume.
    • 1.2 Restore or exceed pre-damage productivity; mitigate near-wellbore damage or create conductive fractures.
  • I.2 Core KPIs
    • 1.3 ?Skin (pre vs post), ?PI or ?IPR; production uplift (?q), water/gas cut stabilization.
    • 1.4 Treatment placement efficiency (e.g., proppant placed vs scheduled, diversion success), screen-out rate.
    • 1.5 Surface treating pressure conformance; NPT; execution time adherence; HSE (TRIR=0).
    • 1.6 $/incremental bbl (or $/Mscf) added; EUR uplift; emissions intensity during pumping.
    • 1.7 Integrity: no frac hit/offset communication, no sustained annulus pressure.
  • I.3 Relevant Equations (performance and design)
    • 1.8 Radial flow with skin (field units): $$q_o=\frac{k h}{141.2\,\mu_o B_o}\cdot\frac{(p_e-p_{wf})}{\ln(r_e/r_w)+s}$$
    • 1.9 Skin benefit (rate ratio for same drawdown): $$\frac{q_{post}}{q_{pre}}=\frac{\ln(r_e/r_w)+s_{pre}}{\ln(r_e/r_w)+s_{post}}$$
    • 1.10 Step-rate/frac gradient: $$G_f=\frac{\Delta P}{\Delta D}$$ where ?P is pressure increment at onset of fracture and ?D is depth.
    • 1.11 Fracture net pressure: $$P_{net}=P_{bh}-P_{pore}-\sigma_{min}$$
    • 1.12 Fracture conductivity (dimensionless): $$C_f^D=\frac{k_f w_f}{k x_f}$$
    • 1.13 Pump horsepower (field): $$HP=\frac{Q\;(\mathrm{bpm})\times \Delta P\;(\mathrm{psi})}{40.8\;\eta}$$

II. Critical Parameters and Target Ranges

Parameter Typical targets/notes (estimated) KPI linkage
Rock type Carbonate ? matrix/acid frac (HCl-based); Sandstone ? mud acid (HF/HCl) or hydraulic fracturing. Technique selection accuracy
Bottomhole temperature 60–160 °C dictates acid kinetics, breakers, stabilizers. Reaction control, retained perm
Pressure/MAASP Respect casing, wellhead, packer ratings; set MASP with 10–20% safety margin. Integrity, HSE
Frac gradient, smin From DFIT/step-rate: 0.8–1.2 psi/ft (18–27 kPa/m) typical; constrain to avoid out-of-zone growth. Placement, offset protection
Pump rate Matrix: 0.5–5 bpm; HF: 25–80 bpm (vertical), 60–120 bpm (horizontal) as allowed by friction/MASP. Stimulation efficiency
Acid system Carbonate: 7.5–28% HCl; Sandstone: 3–12% HCl + 0.5–3% HF (mud acid), preflush/overflush. Skin reduction, compatibility
Proppant 20/40–40/70 sand or LWP/CWP; 0.5–5 ppg ramp; total 30–400 klb depending on target SRV. Conductivity, EUR
Diversion Ball sealers, degradable particulates, foams, staged perforations. Cluster efficiency
Fluids Linear/XL gel, slickwater; breakers, biocides, clay stabilizers, scale/corrosion inhibitors. Retained perm, flowback QoQ
Flowback strategy Choke-managed drawdown; sand management thresholds; early-time cleanup chemistry. Proppant retention, cleanup time

III. Step-by-Step Procedure / Workflow / Checklist

III.A Candidate Selection and Diagnostics

  • 3.1 Compile data: logs, core, PVT, offset stim jobs, completions, production trends, pressure history.
  • 3.2 Diagnose damage or need for fractures: skin from buildup/mini-DST; identify mechanisms (scale, fines, emulsion, water block, clay swelling, asphaltenes).
  • 3.3 Select stimulation type:
    • 3.3.1 Matrix acidizing for near-wellbore damage in permeable rocks.
    • 3.3.2 Acid fracturing in carbonates when conductivity via etching is desired.
    • 3.3.3 Hydraulic fracturing in tight/ultratight formations to create SRV.
  • 3.4 Lab/compatibility tests: brine/acid compatibility, precipitation checks, crude–acid emulsion tendencies, proppant pack damage, corrosion coupons.
  • 3.5 Objectives/KPIs set: targeted ?skin (e.g., -6 to -10), ?q (e.g., +30–200%), execution window, screen-out risk =5%.

III.B Design and Engineering

  • 3.6 Pressure window: confirm pore pressure, smin, caprock strength, MASP/MAASP; define max allowable treating pressure (ATP).
  • 3.7 Perforation strategy: shot density, phasing, limited-entry sizing; ensure perforation friction 200–500 psi for even distribution.
  • 3.8 Fluid system: choose base fluid and additives for temperature and damage control; set breaker loading to achieve <15 cP at BH temp by end of job.
  • 3.9 Diversion plan: stages and diverter loading; for carbonates, alternating acid–diverter cycles; for multi-cluster fracs, limited entry + degradables.
  • 3.10 Pump schedule:
    • 3.10.1 Matrix acid: preflush (HCl or solvent), main acid (HCl or mud acid), overflush; volumes 50–300 gal/ft depending on damage and rock (estimated).
    • 3.10.2 Hydraulic frac: pad ? slurry ramp (proppant concentration) ? tail-in ? flush; ensure proppant transport (velocity > settling), sandface rate above critical.
  • 3.11 Power/hydraulics check: compute required HP using $$HP=\frac{Q\times \Delta P}{40.8\,\eta}$$ and verify pump spread capacity and friction pressure.
  • 3.12 Integrity and barrier plan: BOP/packers tested, CT fatigue life, pressure tests (1.1× ATP), leak-off tests as applicable.
  • 3.13 AFE, logistics, inventory: acids, additives, proppant, water/brine quality; waste and returns handling plan.

III.C Pre-Job Testing and Readiness

  • 3.14 Pre-job HAZID/HAZOP; SIMOPS plan; permit to work; emergency response.
  • 3.15 Step-rate test or injectivity test: determine closure/frac initiation; estimate $$G_f=\frac{\Delta P}{\Delta D}$$ and set treating pressure limits.
  • 3.16 Mini-frac/DFIT (for HF): acquire ISIP, closure pressure, leak-off coefficient; calibrate model.
  • 3.17 Mixing QA/QC: density, pH, viscosity, gel hydration, crosslink delay, friction reducer efficacy; sample retention for lab check.
  • 3.18 Wellbore prep: cleanout, scale removal, solvent washes as needed; confirm perforation status and isolation (packer/plug/straddle).

III.D Execution (Pumping Operations)

  • 3.19 Ramp to test rate; verify surface/bottomhole pressure response vs model; hold below ATP/MASP.
  • 3.20 Breakdown/Pad:
    • 3.20.1 Matrix: Typically avoid fracturing; if pressure trends indicate fracture onset, reduce rate or divert.
    • 3.20.2 HF: Establish fracture with pad; confirm ISIP and net pressure trend $$(P_{net}=P_{bh}-P_{pore}-\sigma_{min})$$.
  • 3.21 Main Placement:
    • 3.21.1 Acid: Execute preflush ? main acid ? divert cycles as designed; monitor rate/pressure; adjust acid strength or diverter on-the-fly for conformance.
    • 3.21.2 Proppant: Increase concentration per schedule; monitor sand rate, blender tub level, density; avoid sudden rate cuts that risk screen-out.
  • 3.22 Flush/Displacement: Pump overflush (acid) or flush (HF) to clear tubulars; ensure proppant off-bottom and inside fracture.
  • 3.23 Shut-in (if applicable): Observe pressure fall-off for closure (HF) or reaction time (acid systems).

III.E Cleanup, Flowback, and Normalization

  • 3.24 Flowback under controlled choke; target drawdown to prevent fines/proppant backproduction; ramp per well integrity envelopes.
  • 3.25 Sand management: install desander/sand traps; keep sand rates below threshold (e.g., =0.1 lb/MMscf or =50 ppm by mass) to protect facilities.
  • 3.26 Chemistry returns: track iron content, pH, breakers, surfactants; adjust cleanup chemistry if emulsions or sludge observed.
  • 3.27 Stabilize and hand over to production with surveillance plan.

III.F Post-Job Evaluation

  • 3.28 Compare actual vs design: pad% variance, proppant placed, acid volumes, pressure match, screen-out events.
  • 3.29 Estimate post-job skin from buildup or rate-transient; compute ?PI and ?q versus plan using: $$q=\frac{k h}{141.2\,\mu B}\cdot\frac{(p_e-p_{wf})}{\ln(r_e/r_w)+s}$$
  • 3.30 Decide on remedial actions (e.g., additional diversion stage, refrac candidate flag).

IV. Risk & Mitigation (HSE, Reliability, Redundancy)

  • 4.1 Screen-out / bridging
    • 4.1.1 Mitigation: Maintain sandface velocity; staged proppant ramp; viscosity/FR optimization; include contingency flush and rate increase protocol.
  • 4.2 Out-of-zone growth / frac hits
    • 4.2.1 Mitigation: Real-time pressure matching; adjust rate/viscosity; reduce net pressure; observe offset pressure via DFIT gauges if available; set frac fence via perforation strategy.
  • 4.3 Corrosion and precipitation
    • 4.3.1 Mitigation: Inhibitors per temperature; iron control; preflush/overflush to manage aluminosilicate/fluoride systems; monitor coupons.
  • 4.4 H2S/CO2 exposure
    • 4.4.1 Mitigation: Sour service PPE, scavengers, appropriate metallurgy, gas monitoring; emergency blowdown plan.
  • 4.5 Well integrity
    • 4.5.1 Mitigation: Verified pressure tests, two-barrier policy, temperature/pressure derating considered, packer setting check, vibration and torque control on CT.
  • 4.6 Environmental/emissions
    • 4.6.1 Mitigation: Minimize flaring; optimize pump fleet utilization; low-emission power options when feasible; chemical containment and spill prevention.
  • 4.7 SIMOPS/conflict
    • 4.7.1 Mitigation: Permit-to-work, radio channels, exclusion zones, crane lifts plan, hose management; stop-work authority affirmed.

V. Optimization Levers (Execution and Design)

  • 5.1 Diagnostics-first: DFIT/mini-frac, step-rate, and fiber/pressure monitoring to calibrate model; update net pressure and closure on-the-fly.
  • 5.2 Diversion effectiveness: Use pressure response to confirm diversion; if no step-up, increase diverter or switch method (particulate ? chemical).
  • 5.3 Limited entry tuning: Adjust perforation friction 200–500 psi for cluster balance; validate via injection allocation (spinner or tracers).
  • 5.4 Fluid economy: Optimize FR and gel load to minimum needed for transport; employ breakers tailored to BH temperature to reduce residual damage.
  • 5.5 Drawdown management: Choke schedule to protect proppant pack and prevent fines mobilization; target early-time dP/dt limits.
  • 5.6 Chemical tailoring: For sandstones, preflush with HCl or solvent; carefully meter HF strength to avoid secondary precipitates; for carbonates, staged HCl with inhibitors and diverters for deeper wormholing.
  • 5.7 Execution analytics: Real-time pressure-rate match curves; track deviations >10% and trigger decision tree (rate, viscosity, stage length).
  • 5.8 Logistics/maintenance: Hot redundancy on critical pumps/blenders; hose pressure ratings margin =15%; pre-job function tests reduce NPT.

VI. Verification & Monitoring Plan

  • 6.1 Pre-job baselines
    • 6.1.1 PI/IPR, skin from buildup, PLT if available, water/gas cut, solids/salt content.
    • 6.1.2 Integrity logs/pressure tests; emissions/power baseline for OPEX/emissions KPI.
  • 6.2 During job
    • 6.2.1 High-frequency rate/pressure/density/chem dosages; blender tub levels; sand concentration.
    • 6.2.2 Event tags: breakdown, ISIP, screen-out onset, diversion pressure steps, stage end times.
  • 6.3 Immediate post-job
    • 6.3.1 Fall-off analysis for closure and leak-off coefficients; compare with model.
    • 6.3.2 Fluid returns sampling (iron, pH, residual FR/gel, oil–water emulsion index).
  • 6.4 Flowback/early production
    • 6.4.1 Daily production test; choke, WHP, THP, sand rate, GOR/WOR; calculate early-time cleanup efficiency.
    • 6.4.2 If available: tracers or PLT to confirm stage/cluster contribution.
  • 6.5 30–90 day evaluation
    • 6.5.1 Pressure transient or rate-transient analysis to quantify ?skin and fracture properties; update type curves.
    • 6.5.2 KPI scorecard: ?q, ?PI, cost/added barrel, screen-out rate, emissions per stage, lessons learned.

Disclaimer: The information provided here is for informational and educational purposes only. These insights are intended as general guides and may not reflect your specific circumstances. Salary figures are approximate and can vary by region, employer, and individual experience. Career, educational, and industry guidance offered here should not replace consultation with qualified professionals, employers, or educational institutions. Nothing presented should be interpreted as legal, financial, or investment advice, nor as a recommendation for commodity or securities trading. Always seek advice from appropriate professionals before making career, educational, or financial decisions.

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