Mundra Solar Technopark Pvt. Ltd. entrance gate — Adani Solar plant, Kutch Gujarat — Antlia Engineering Works field visit August 2025

Mundra Solar Technopark Pvt. Ltd. (Adani Solar), Kutch, Gujarat — Antlia Engineering Works field visit, 22nd August 2025

Optimising AODD Pump Performance at Adani Solar, Mundra — Field Visit Report

On 22nd August 2025, the Antlia Engineering Works team visited the Adani Solar plant at Mundra, Kutch, Gujarat to work directly with their operations team on improving AODD pump performance for critical chemical transfer — including KOH, H₂O₂, HF, HCl, and O₃. This field report documents our on-site observations and the practical solutions recommended to improve pump uptime, diaphragm life, and process output consistency.

Pump Configuration at Site

Installed Pump Models & Diaphragms

The facility uses YTS-make 1-inch AODD pumps across three materials of construction for acid and alkaline chemical transfer:

Pump Body MOCDiaphragm FittedBackup Diaphragm
PP (Polypropylene)TPO (Thermoplastic Polyolefin)
PVDF (Polyvinylidene Fluoride)TPO (Thermoplastic Polyolefin)
SS-316 (Stainless Steel)PTFE (Main diaphragm)Neoprene backup — MISSING

Operation cycles: Rinsing — 24 hours continuous  |  Acid transfer — 6–8 hours per cycle

Observation 1

PTFE Diaphragms Running Without Backup

The SS-316 pumps were running PTFE main diaphragms without neoprene backup diaphragms. Since PTFE lacks the elasticity of rubber, it flexes unevenly under cyclic air pressure — causing premature fatigue cracking and significantly shortened diaphragm life.

✓ Solution: Always pair PTFE main diaphragms with rubber (neoprene) backup diaphragms. With the correct backup installed, expected diaphragm life increases to 12–18 months.

As an immediate support measure, Antlia will supply 2 pcs PTFE + 2 pcs rubber diaphragms for the SS-316 pumps for field testing — dispatch within 10–12 days (dye-making in process).

Observation 2

Excessive Pump Mounting Tightness

Several pumps were mounted with excessively tight bolting to their support frames. Over-tightened mounting transmits the reciprocating vibration directly into the pump body and piping — creating back pressure spikes and mechanical stress that accelerates diaphragm failure.

✓ Solution: Loosen mounting nuts slightly to allow minor flex, or install rubber anti-vibration pads / legs under the pump base to absorb cyclic vibration and reduce diaphragm fatigue.
Observation 3

Significant Performance Gap — Perceived vs Actual Output

ParameterValue
Perceived output100–120 LPM
Actual measured output40–50 LPM
Output drop~50–60%

The piping system includes approximately 30–40 m horizontal + 10 m vertical + 5–7 bends, resulting in 20–25 m total head loss (~2.5 kg pressure drop). The piping also includes reducers stepping from a 1.5-inch main line to 1-inch pump connections — adding further restriction.

✓ Solution: Upgrade to 1.5-inch PVDF pumps for this application. The larger port size compensates for head and frictional losses, restoring output to near the required process rate.

Recommendation: Replace pumps on one machine (5 pumps per system) first to validate performance before full site rollout.  Watch Performance Video →
Observation 4

Air Supply Pressure Losses

AODD pumps operate at a 1:1 air-to-liquid pressure ratio — the discharge pressure can never exceed the inlet air pressure. The pressure audit revealed significant losses:

Air Pressure PointPressure (kg/cm²)
Available at compressor6 kg/cm²
Running pressure at pump5 kg/cm²
Lost to piping head & friction2.5 kg/cm²
Net effective discharge pressure~2.5 kg/cm²

With 2.5 kg lost to the piping system, the effective discharge pressure drops proportionally — directly explaining the output shortfall observed at the pump outlets.

Observation 5

Spares Availability & Uptime Impact

Delays in procuring consumables — O-rings, gaskets, U-cups, seals, valve balls, valve seats, ball cages, and diaphragms — were causing unplanned downtime at the facility.

✓ Solution: Implement a structured MOQ buffer stock plan to maintain on-site spares inventory and eliminate procurement-driven downtime.
Spare PartMOQ
O-Rings & Seals20 pcs per item
Valve Seat & Ball Cage8 pcs per item
Diaphragms10 pcs per item
Valve Balls10 pcs per item

🎯 Impact of Recommended Optimisations

Implementing the above recommendations will deliver:

  • ✓  Extended diaphragm life — from weeks to 12–18 months (PTFE + rubber backup)
  • ✓  Reduced vibration fatigue on pump bodies and piping connections
  • ✓  Restored process output — from 40–50 LPM to near-rated capacity with 1.5" pump upgrade
  • ✓  Improved uptime through structured spare parts inventory management

Need AODD pump optimisation support for your plant?

Our engineers at Antlia Engineering Works, Mumbai provide on-site visits, pump selection, and after-sales technical support across India.

Get in Touch Call +91 9819395995

Frequently Asked Questions

WHY DO PTFE DIAPHRAGMS FAIL FASTER WITHOUT A BACKUP IN AODD PUMPS?

PTFE has very low elasticity. Without a rubber backup diaphragm to support and distribute cyclic flexing stress, PTFE fatigue-cracks rapidly under reciprocating air pressure. A neoprene backup acts as a cushion and structural support — extending PTFE diaphragm life to 12–18 months.

WHY IS ACTUAL AODD PUMP OUTPUT LOWER THAN EXPECTED IN LONG PIPING RUNS?

AODD pumps operate at a 1:1 air-to-liquid pressure ratio. Long horizontal runs, vertical lifts, and pipe bends create frictional head losses that reduce net discharge pressure. At this site, approximately 2.5 kg pressure was lost to the piping system, reducing output from 100–120 LPM to only 40–50 LPM. Upgrading to a 1.5-inch pump compensates for these losses.

WHAT CAUSES AODD PUMP VIBRATION DAMAGE IN INDUSTRIAL PLANTS?

Over-tightened pump mounting transmits the reciprocating vibration directly into the frame, piping, and pump body — causing mechanical stress on diaphragms and connections. The solution is to loosen mounting hardware slightly and install rubber anti-vibration pads or legs under the pump base.

WHICH AODD PUMP MOC IS BEST FOR HF, HCL, KOH, AND H₂O₂ TRANSFER?

PVDF body with PTFE main diaphragm and neoprene backup is the recommended configuration for HF, HCl, KOH, H₂O₂, and O₃ service. PVDF offers superior resistance to fluorinated and chlorinated compounds, while PTFE provides the broadest wetted-part chemical compatibility.

HOW OFTEN SHOULD AODD PUMP SPARES BE REPLENISHED AT A HIGH-DUTY SOLAR PLANT?

For 24-hour continuous rinsing and 6–8 hour acid transfer cycles, maintain buffer stock per the MOQ plan: 20 pcs O-rings/seals, 8 pcs valve seats/ball cages, 10 pcs diaphragms, and 10 pcs valve balls per item. Review and replenish quarterly to prevent unplanned downtime.