Pulsation Control in Hi-Temp Coffee Extraction Towers

Pulsation Control in Hi-Temp Coffee Extraction Towers

Problem: The Coffee Manufacturer operates interconnected vertical extraction towers where hot water is circulated at extreme temperatures to produce coffee extract. During operation, the customer observed:

- Rapid water evaporation above 175°C resulting in air pockets inside pipelines
- Slow-reacting temperature instruments, allowing entrained air to persist
- Centrifugal pumps forced to move both air and liquid, leading to:
• Severe water hammer
• Excessive piping vibration
• Damage to plate evaporators and instrumentation
• Partially filled distribution lines on startup, requiring air displacement before flow could stabilize—intensifying water hammer

These issues disrupted extraction quality, compromised equipment life, and increased maintenance cost.

A review of the extraction tower circulation system revealed two primary contributors to the instability:

1. Air Entrapment Due to High-Temperature Evaporation
At 175°C, water rapidly vaporizes. Air and vapor bubbles accumulated in the recirculation lines and plate evaporators. Because the system’s temperature instrumentation responded slowly, air remained trapped far longer than expected—allowing pumps to ingest and compress air repeatedly.

2. Pumping System Not Designed to Handle Vapor Pockets
The 1½” centrifugal pumps recirculating extract between stages were forced to push air through evaporators and distribution lines. This caused major hydraulic consequences:

- Violent pressure spikes (water hammer)
- Resonant vibration in vertical and horizontal piping sections
- Structural stress on evaporators and associated equipment
- This unstable flow environment also threatened extract consistency and overall process quality.

Water Hammer in Wash-Water Header

Water Hammer in Wash-Water Header

Problem: A Midwest sugar processing operation needed a surge suppression solution that could:

- Absorb hydraulic shock from six 3/4" wash-water valves closing rapidly.
- Handle an estimated 300 GPM flow.
- Fit within tight piping constraints.
- Integrate with both old and new centrifugal configurations.
- Stay within the system's #150 flange / 275 PSIG pressure rating.

The team gathered detailed system information including flow estimates, pipe schedule, pressure limits, and isometric drawings. A surge control engineer reviewed the system and collaborated with the company to understand the transient conditions. A Teams call was held to walk through the piping schematic and confirm installation points.

Diesel Transfer Pump

Diesel Transfer Pump

Problem: The diesel transfer pumps on an offshore platform had never operated reliably or automatically since installation. This forced operators to transfer diesel to the electrical generators manually, resulting in significant delays and safety risks.

Chronic issues included:
• Recurring diaphragm ruptures
• Diesel leakage at the muffler
• Hose failures
• Excessive vibration in pump and piping
• Frequent instrument damage (pressure transmitters, PSVs, filter elements)
• Low and inconsistent transfer pressure
• Extremely long transfer times (6–8 hours for a 30% fill)

Root Causes Identified:
1. Pump suction pressure significantly exceeded recommended limits, producing severe water hammer effects and subjecting PTFE diaphragms to damaging pressure spikes.
2. Process air regulator pressure was set too high, further increasing pressure peaks and accelerating failures.
3. The original pump design lacked necessary stabilizing accessories to control pulsation and protect downstream components.

Bottling Line Water Hammer

Bottling Line Water Hammer

Problem: A cleaning product manufacturing facility experienced excessive pipe vibration on its bottling line due to a quick-closing valve. The rapid valve actuation was generating hydraulic shock (water hammer), compromising system stability and potentially damaging components.

Tool Manufacturing Manifold Startup Shock

Tool Manufacturing Manifold Startup Shock

Problem: An internationally known tool manufacturer located in the Pacific Northwest was experiencing severe pipe vibration in an overhead manifold system. The system delivers coolant to several production grinding machines. The coolant is delivered to the manifold by a 300 gpm centrifugal pump located in a reservoir on the plant floor. When the pump is started, a ball valve at the pump discharge is opened and fluid is pushed vertically up to the horizontal manifold. The manifold does not stay filled with liquid during idle periods so, when the pump is started the coolant flowing into the manifold must first push the air trapped in the manifold out the machine coolant nozzles before coolant reaches the machines. Since air moves more quickly out of the nozzles than liquid, when the coolant reaches the nozzles the velocity of the coolant is instantly reduced and a water hammer effect occurs creating severe pipe vibration.

Commercial Restroom Flush Water Hammer

Commercial Restroom Flush Water Hammer

Problem: Our customer moved into their new building which did not have a pressure reducing valve in the water main and the system pressure in the building was around 90 psi. The owner's office is near the men's restroom. Every time the urinal was flushed, extreme water hammer occurred. This was very aggravating to the owner and he was afraid that the water hammer might cause a pipe to rupture and flood the building.

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