Temperature swing adsorption
Pressure swing adsorption
Adsorption Nitrogen rich euent
Regeneration
Adsorption
Regeneration
Heater
N rich gas
Flue gas
Blower/ compressor
Recycle b lower
Increase temperature
Reduuce pressure
Cooler
Flue gas
CO rich gas
CO rich gas
Pressure swing adsorbents: Carbon-based adsorbents
Temperature swing adsorbents:
Rotating solid beds Amines in composite polymer/silica hollow bres
Zeolite-based adsorbents
Metal-organic frameworks (MOF) - based adsorbents Alkali metal carbonate-based adsorbents Layered double hydroxide (LDH) - based adsorbents CaO-based adsorbents
Alkali ceramic-based adsorbents
Figure 3 Temperature and pressure swing adsorption systems
Membrane-based carbon capture Membrane-based carbon capture uses semi- permeable membranes to selectively separate the CO₂ from the other gases that are present. Depending on what the other gases are, the CO₂ may pass through the membrane, or the other gases might pass through the membrane, leaving the CO₂ behind. A wide variety of membranes are available, and a few of these
contains many small pores that allow the CO₂ to accumulate in the adsorbent. Most solid adsorbent systems use multiple adsorbent beds that can be switched from adsorbing the CO₂ to regenerating the CO₂ out of the adsorbent. This regeneration can be done using a temperature or pressure change, depending on the type of adsorbent being used (see Figure 3 ).
Membrane 1
Membrane 2
Membrane 1
Membrane 2
Feed
Retentate
Retentate
Feed
Interstage compressor
Feed compressor
Feed compressor
Permeate
Permeate
Vacuum pump
Vacuum pump
Recycle
Recycle
Membrane 1
Membrane 1
Retentate
Feed
Feed
Membrane 2
Membrane 2
Feed compressor
Feed compressor
Permeate
Permeate
Vacuum pump
E-33
Compressor
Vacuum pump
Ceramic membranes Supported liquid membranes Metalic membranes
Zeolite etc. Adsorbent membranes
Polymeric membranes
Polyamide - Air Liquide Medal™ APCI Prism Membrane™ UOP Polysep™
Figure 4 Types of membranes and four typical membrane configurations
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