An overview of associated gas – its processing and treatment
Module 1
Summary description of module�
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Objectives
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Basic concepts
Gas produced as a byproduct of crude oil production. Associated gas reserves are typically developed to produce crude oil, which pays for field development costs. Reserves typically produce at peak levels for a few years before declining.[1]
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Major concerns
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Major concerns (continued)
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Gas processing plant block diagram
Figure 1. Gas Plant – Process Description
CEMS: SO2 Mass Emissions
H2S & SO2
High H2S
Gas Composition
Possible H2O Quality Measurement
Custody Transfer: Dew Point, H2S, Heating Value
LPG QC
Low H2S
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Gas sweetening – amine absorption
Figure 2. Natural gas treating process. Adapted from Instrument Technician
Regenerate using heat input from a reboiler
Bubble cap trays: refer to glycol dehy. flow diagram
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Natural gas dehydration – adsorption technique
Figure 3. Adsorption Dehydration Two-Tower vs Three-Tower System
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Natural gas dehydration – glycol absorption technique
Figure 4. Dehydration With Glycol (Smith, 2013)
Remove the water
Heat exchanger
Regenerate the glycol
Lean glycol
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LPG recovery
Figure 5. Fractionation train. Adapted from Instrument Technician ILM, Gas Analyzers – Part A, 310304cA, (2016)
Consider a GC with a multi-stream configuration
It’s all about boiling points and temp. control
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Sulfur recovery
Figure 6. Natural Gas Processing Plant. Adapted from Hauer, Randy (2013). Claus Sulfur Recovery [PowerPoint Slides]
Sulfur Block
Flare stack with a small flame: things are going well today
CEMS sample point: about 40m
Sweetening & Dehy.
LPG Recovery
The reaction furnace – incomplete combustion by intent
Figure 7. Natural Gas Processing Plant. Adapted from Hauer, Randy (2013). Claus Sulfur Recovery [PowerPoint Slides]
925 °C – 1300 °C
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Figure 8. Natural Gas Processing Plant. Adapted from Hauer, Randy (2013). Claus Sulfur Recovery [PowerPoint Slides]
H2S and SO2 Vapours
swept away to the incinerator
Molten sulfur
Measure for explosive levels of H2S
H2S measurement for feedforward
H2S and SO2 measurement for feedback trim or cascade
Figure 9. Natural Gas Processing Plant. Adapted from Hauer, Randy (2013). Claus Sulfur Recovery [PowerPoint Slides]
No SO2 breakthrough allowed – bad news for absorber
Low H2S <300 ppm = optimum absorber performance
Low H2S @ AT5 = low emissions
Why do we bother recovering sulfur?
Keep It Clean
Figure 10 Stacked (Apergis, 2019)
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Most energy-demanding industries
Several examples will be given as handouts.
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Energy-demanding industries will result in major CO2-containing waste streams
Several examples will be given as handouts.
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Major methane-containing waste streams
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Pollution mitigation strategies or waste stream minimization
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Key take-aways
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References
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