Manifolds are common in oil and gas production facilities, refinery process units, power plants, and pipeline stations. They reduce the number of individual piping runs and simplify flow control by centralizing valves in a single accessible location.
Types of Piping Manifolds
Type
Function
Typical Application
Production manifold
Collects well flow from multiple wells
Oil/gas production facilities
Test manifold
Routes individual wells to test separator
Well testing and allocation
Injection manifold
Distributes injection fluid to wells
Water/gas injection systems
Steam header
Distributes steam to multiple consumers
Power plants, refineries
Instrument manifold
Multi-valve assembly for instrument isolation
Pressure transmitter hook-ups
Subsea manifold
Collects subsea well flow
Deepwater production
Pipeline header
Connects multiple pipelines at station
Pipeline terminal/station
Manifold Design Considerations
Parameter
Design Criteria
Header size
Based on total flow and velocity limit (typically 3-6 m/s for liquid, 15-25 m/s for gas)
Branch size
Based on individual flow and velocity limit
Branch spacing
Minimum 2x header OD between branch centers
Branch connection type
Tee (equal branches), weldolet/reinforced branch (reduced branches)
ASME B31.3 requires reinforcement calculations for all branch connections. The branch weakens the header by removing pipe wall material. Reinforcement (from excess header wall, branch wall, or welded pads) must compensate for this lost area.
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