MaximaLabs

Helium recovery, concentrated by staging

Helium-rich gas let down through a real isentropic turboexpander, then cascaded through two cryogenic flashes as methane and nitrogen condense out.

Real isentropic turboexpander, not an assumed chillTwo cascaded cryogenic flashes concentrating heliumNitrogen rejection on the same solved flowsheet
Helium-rich gas
Turboexpander
Cooler (125 K)
Cryogenic flash 1
Cooler (105 K)
Cryogenic flash 2
Crude helium
Condensate
Nitrogen rejection
Nitrogen
Sales gas

The actual dark-mode canvas: feed gas expanded through a turboexpander, chilled and flashed twice at 125 K then 105 K so helium concentrates in the vapour while methane and nitrogen drop out as liquid.

Staging is what concentrates a trace component

Helium's K-value at these temperatures is enormous, so it stays in the vapour while everything around it condenses. Two stages in series do what one cannot: the first strips the bulk methane, the second concentrates what is left. Scope note: that near-infinite K-value is numerically awkward, and the example's own description says how it is handled.

ηs=hinhouthinhouts(real isentropic expander, work extracted)\eta_s = \frac{h_{in}-h_{out}}{h_{in}-h_{out}^{\,s}} \quad \text{(real isentropic expander, work extracted)}
KHeKN2>KCH4(why staging concentrates helium)K_{\mathrm{He}} \gg K_{\mathrm{N_2}} > K_{\mathrm{CH_4}} \quad \text{(why staging concentrates helium)}
stage 2 vapour=crude He(each flash sharpens the previous one)\text{stage } 2 \text{ vapour} = \text{crude He} \quad \text{(each flash sharpens the previous one)}

Unit ops shipped for this vertical

Turbine

Isentropic-efficiency expansion — the power-recovery counterpart to the compressor.

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Heater / cooler

Duty- or outlet-condition-specified energy-balance stage.

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Flash drum

Single-stage vapor-liquid equilibrium split at a fixed temperature/pressure.

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Separator

Flash/phase-split unit op — the foundational vapor-liquid calculation.

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Live plant integration

Stream expander outlet temperature and both flash-stage conditions from the plant's OPC-UA server into this flowsheet's twin comparison — helium recovery is set by how cold the second stage actually gets, and a drifting expander shows there first.

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Try it yourself

  • Real isentropic turboexpander, not an assumed chill
  • Two cascaded flash stages concentrating a trace component
  • Nitrogen rejection on the same solved flowsheet

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