Services · ESP rebuild & performance recovery
Electrostatic precipitator upgrade: measure first, then fix the real limit
An electrostatic precipitator upgrade starts with measurement — kV/mA maps per field, opacity trend, gas distribution, ash resistivity — then fixes the actual limit in order: controls, TR sets, internals, added collecting area. Skipping diagnosis wastes an outage; our bagasse design basis shows what each step is worth, from 720 down to 24 mg/Nm³ @ 6 % O₂ dry.
01 — Diagnosis before hardware
Why an electrostatic precipitator upgrade starts with a field map, not a parts list
Most underperforming ESPs are limited by one thing. Find it before the outage is booked.
The most expensive mistake in precipitator rehabilitation is fixing the symptom. A plant sees dust on the stack, assumes the collecting plates are worn out, and spends a three-week outage replacing them — only to restart at nearly the same opacity, because the real limit was skewed gas distribution or a rapping system that stopped cleaning the plates years ago. New plates collect no better than old ones if the dust is never removed from them, and no internals package fixes a field that is electrically starved. This is a core position of our boiler and emission-control services practice: no upgrade scope is priced until the failure mode is measured.
Arrow Energy Co., Ltd. therefore runs every ESP upgrade through an ordered decision tree. The unit is surveyed on load first; the survey identifies whether the precipitator is spark-limited, voltage-limited, mechanically degraded, or fundamentally undersized; and the upgrade scope is the cheapest step that removes that specific limit. Each step is verified against the same measurement basis before the next is considered.
The on-load survey covers four measurements. First, secondary voltage and current per field — the V-I map. A healthy field draws current along a curve that rises steeply above corona onset; a field pinned at high spark rate with collapsing kV is control-limited, a field at full current but low voltage suggests ripple or resistivity trouble, and a field drawing almost no current points to shorted or swinging internals. Second, opacity or outlet dust trended against boiler load, which separates continuous underperformance from rapping puffs and load excursions. Third, gas distribution, checked by port velocity traverse or model, against the usual uniformity criterion of an RMS velocity deviation within about 15 % (indicative); a distorted profile can halve effective collecting area while every electrical reading looks normal. Fourth, fly-ash resistivity, which for good collection should sit between roughly 10⁴ and 10¹¹ Ω·cm — above that window, back-corona mimics electrical faults that no controller can tune away.
02 — The ordered decision tree
Five upgrade steps, cheapest first — and what each one is indicatively worth
Escalate only when measurement says the cheaper step cannot reach the target.
Step 1 — Controls / automatic voltage control (AVC), when spark-limited. If the V-I map shows fields sparking heavily with voltage sagging well below the sparkover ceiling, the limit is control response, not hardware. A modern AVC with fast spark quench, controlled ramp recovery, back-corona detection and intermittent energisation raises the useful corona power the existing TR set can deliver. Indicatively worth a 10–25 % reduction in outlet dust, executed in days on a normal shutdown.
Step 2 — Transformer-rectifier or high-frequency power supply, when voltage-limited. A conventional 50 Hz single-phase TR delivers roughly 35–45 % voltage ripple, so the mean field voltage sits well below the peak that triggers sparkover. A high-frequency switch-mode supply cuts ripple below 1 %, holding the field 2–5 kV closer to sparkover continuously — and since migration velocity rises roughly with the square of field strength, this is indicatively worth 15–30 % lower outlet dust on fields that were genuinely voltage-limited. See electrostatic precipitator design for how field voltage enters the sizing equations.
Step 3 — Internals renewal, when mechanically degraded. Broken or swinging discharge electrodes, plates out of alignment beyond roughly ±5 mm on a 300–400 mm duct (indicative), seized rapper drives and eroded gas distribution screens all show up as electrical instability with a mechanical cause. The remedy is targeted: re-align, replace failed electrodes, rebuild rapping, restore distribution screens — not blanket plate replacement. Renewal returns the field to its design curve; it does not exceed it.
Step 4 — More collecting area, when fundamentally undersized. If the unit is electrically healthy, mechanically true, and still over the limit, only area helps: an added field (casing extension) or an upstream Electrocyclone pre-collector removing 85–95 % of the inlet load before the ESP, in 60–65 % of the plot an equivalent ESP stage would need and at 120–140 kW absorbed power. The design basis below shows the scale of what staged collection buys.
Step 5 — Full retrofit. When casing corrosion, foundation constraints or a step-change in the emission limit make incremental work uneconomic, a new precipitator is built to current duty — usually around the existing foundations, with tie-ins prefabricated to compress the outage.
03 — Scope
Scope of the ESP upgrade service
What Arrow executes, and what stays with the plant.
| Scope item | Included | Excluded / by others |
|---|---|---|
| On-load diagnostic survey (V-I maps, opacity trend, gas distribution, resistivity) | Included — 3–5 days on load (indicative) | — |
| AVC / controller supply, installation, tuning | Included | Plant DCS modifications beyond agreed signal interface |
| TR set / high-frequency power supply replacement | Included, incl. HV cabling to the bushing | Upstream MV switchgear and plant LV distribution |
| Internals: discharge/collecting electrodes, rapping, gas distribution screens, insulators | Included — supply, alignment, installation | — |
| Casing extension / added field / Electrocyclone pre-collector | Included — design, fabrication (Samut Sakhon), erection | Civil foundations and piling (Arrow provides loading data) |
| Before/after isokinetic performance test | Included — EPA M5 / ISO 9096, one stated basis | Regulatory stack-test filing, unless agreed as an option |
| Ash handling below hoppers, scaffolding, cranage | Per project split, stated in the proposal | Boiler-side combustion tuning (available as a separate boiler energy audit) |
04 — Method & verification
Method, standards and the before/after test protocol
One measurement basis, stated in the contract, used twice.
Upgrade sizing uses the same physics as new design: Deutsch-Anderson (η = 1 − exp(−w·A/Q)) to frame the area–efficiency trade, corrected by Matts-Öhnfeldt with k ≈ 0.5 because real polydisperse ash (design-basis inlet d₅₀ 21 µm) never behaves like a single migration velocity. Electrical work follows IEC practice for HV equipment; mechanical tolerances follow Arrow fabrication standards with alignment records per field.
Performance is proven on one basis only. Before the outage, an isokinetic traverse to EPA Method 5 or ISO 9096 establishes the baseline in mg/Nm³, corrected to the stated reference O₂ — 6 % O₂ dry for biomass — dry basis, within a defined boiler load window (typically 90–100 % MCR) and with soot-blowing state recorded. After the work, the identical protocol runs at the same ports and load window. Numbers quoted on different O₂ corrections or different loads are not comparable, and we do not sign test reports that mix bases. Guaranteed figures are stated per project after the technical assessment, on that stated basis.
How long does an electrostatic precipitator upgrade take?
Indicatively: the diagnostic survey takes 3–5 days on load with no shutdown. A controls or AVC upgrade fits 3–7 outage days; TR or high-frequency power supply replacement 5–10 days; internals renewal 2–4 weeks depending on fields opened; a casing extension or Electrocyclone pre-collector is erected largely pre-outage, with tie-in windows of 2–4 weeks.
The schedule discipline is pre-assembly: for area additions, structural steel, casing modules and the pre-collector are erected beside the running unit, so the outage consumes only duct tie-ins, electrical connection and commissioning. Long-lead items — TR sets, electrodes, insulators — are secured against the outage date, and critical consumables are held as ESP and boiler spare parts stock so a failed insulator found on opening does not extend the shutdown.
Why not just replace the collecting plates?
Because plates are rarely the limit. If rapping is dead, new plates foul in weeks; if gas distribution is skewed, part of any plate area — old or new — sees almost no gas; if the field is voltage-starved, clean plates collect little. Replacing plates without a field map risks spending a full outage for single-digit improvement. Measure first; replace metal only when metal is the problem.
05 — Deliverables
What the plant receives
Documents that survive the handover, not just hardware.
- Diagnostic survey report: per-field V-I curves, spark-rate logs, opacity/load correlation, gas-distribution result, resistivity assessment, and the ranked failure-mode conclusion.
- Upgrade proposal with the decision-tree position stated: which step, why the cheaper steps were ruled out, and the indicative outlet-dust range on a stated basis.
- Baseline isokinetic test report (EPA M5 / ISO 9096, mg/Nm³ @ stated O₂ dry, load window recorded).
- As-built documentation: alignment records per field, electrode and rapping installation records, TR/AVC settings and protection parameters.
- Post-upgrade performance test report on the identical basis, with before/after comparison table.
- Recommended spares list and settings backup for controllers and power supplies.
Where the survey shows the precipitator is not the constraint at all — a boiler carrying char over at high excess air can double the inlet load — we say so, and the corrective scope shifts upstream. Related reference classes: sugar mill Thailand 170 t/h bagasse · biomass power Thailand 250 t/h · sugar mill Colombia 230 t/h.
FAQ
Engineering questions, answered
What is the first step in an electrostatic precipitator upgrade?
Measurement, not replacement. A 3–5 day on-load survey maps secondary kV and mA per field, spark rate, opacity trend against load, and gas distribution; ash resistivity is checked against the 10⁴–10¹¹ Ω·cm working window. The failure mode — spark-limited, voltage-limited, mechanical, or undersized — decides which upgrade step actually pays.
When is an ESP controls or AVC upgrade enough?
When fields are spark-limited: kV/mA maps show voltage collapsing at high spark rates while internals are mechanically sound. A modern automatic voltage controller with fast quench and ramp recovery raises useful corona power within the existing TR rating. Indicatively this recovers 10–25 % of outlet dust; it fits a short shutdown of days, not weeks.
What does a high-frequency transformer rectifier upgrade do for an ESP?
A high-frequency TR reduces ripple from roughly 35–45 % at 50 Hz to under 1 %, so mean field voltage runs 2–5 kV closer to sparkover. Because collection scales with field strength, indicatively 15–30 % lower outlet dust follows on voltage-limited fields. It reuses the existing casing and internals, so outage time stays short.
When does an ESP need more collecting area rather than repairs?
When the unit is fundamentally undersized: fields run clean, near sparkover, mechanically true — and outlet dust still exceeds the permit. Then only added specific collecting area or an upstream pre-collector helps. An Electrocyclone stage removing 85–95 % of inlet load ahead of the ESP is often cheaper than casing extension inside a congested plot.
How is ESP upgrade performance verified before and after?
By isokinetic dust sampling to EPA Method 5 or ISO 9096 at the same ports, corrected to the same reference — for biomass typically mg/Nm³ @ 6 % O₂ dry — within an agreed load window, before and after the outage. Guaranteed figures are stated per project after the technical assessment, on that stated basis.
Send us your plant data
Fuel, boiler capacity, gas flow, current emission and the limit you must meet. An Arrow engineer replies with a technical assessment basis — not a brochure.