Cellulous nanofiber aerogels-based bio unit for sequestering flow back CO2 after hydraulic fracturing operations
Devices, methods, and systems for carbon dioxide (CO 2 ) sequestration using a cellulose nanofiber (CNF) aerogel, having a monolithic structure. The monolithic structure includes an aerogel matrix, a plurality of crosslinked CNFs, and a plurality of cellulose nanocrystal acetone (a-CNC) suspension particles, where the plurality of crosslinked CNFs and the plurality of a-CNC suspension particles are dispersed throughout the aerogel matrix. Systems and methods for CO 2 sequestration include locating a CO 2 producing process, separating, using a first membrane system, a feed stream into a mixed solid and liquid stream and a first gas stream and separating, using a second membrane system, the first gas stream to produce a second gas stream and a CO 2 rich stream. Systems and methods further include directing the CO 2 rich stream to a cellulose nanofiber (CNF) aerogel unit and adsorbing CO 2 from the CO 2 rich stream.
1. A method for carbon dioxide (CO 2 ) sequestration, comprising:
locating a CO 2 producing process, wherein the CO 2 producing process produces a feed stream;
separating, using a first membrane system, the feed stream into a mixed solid and liquid stream and a first gas stream;
separating, using a second membrane system, the first gas stream to produce a second gas stream and a CO 2 rich stream comprising CO 2 ;
directing the CO 2 rich stream to a cellulose nanofiber (CNF) aerogel unit, comprising,
a CNF aerogel, comprising a monolithic structure, wherein the monolithic structure comprises;
an aerogel matrix,
a plurality of crosslinked CNFs, and
a plurality of cellulose nanocrystal acetone (a-CNC) suspension particles,
wherein the plurality of crosslinked CNFs and the plurality of a-CNC suspension particles are dispersed throughout the aerogel matrix; and
adsorbing, using the CNF aerogel unit, the CO 2 from the CO 2 rich stream.
2. The method of claim 1 , wherein the CO 2 producing process comprises a hydraulic fracturing process, and wherein the hydraulic fracturing process produces the feed stream by fracturing treatment employing a CO 2 foam.
3. The method of claim 1 further comprising determining, by calculating a reduced adsorption capacity, when the CNF aerogel unit is saturated with the CO 2 :
Adsorption capacity=[(Co−Ce)/ m ]×V (Equation 4)
wherein adsorption capacity has units of mg/g, Co is an initial concentration of adsorbate in ppm, Ce is an equilibrium concentration of adsorbate, m is a mass of the adsorbent, and V is a volume of solution containing adsorbate injected into the CNF aerogel unit.
4. The method of claim 3 , further comprising replacing the CNF aerogel unit when it is saturated with CO 2 .