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Chapter 2 23<br />

appealing perspectives of this method on CUSs modification/introduction, this method is<br />

expected to receive much attention in next years. This kind of modification of MOFs are<br />

also involved in this dissertation. Further details will come in Chapter 4 and 5.<br />

2.3.4 Application of MOFs<br />

What have been addressed above show rather a broad picture demonstrating that MOFs<br />

are attractive porous materials with a huge diversity of structures, functionalities, and<br />

facile modification. All these make MOFs very promising for a range of applications<br />

(Figure 2.15), [147] especially in gas storage, selective adsorption and separation.<br />

Hydrogen and methane are good candidates for on-board fuel. A tank loaded with porous<br />

absorbent allows gas to be stored at much lower pressure in comparison with the<br />

identical tank without an adsorbent. Due to the high porosity and well-defined structures,<br />

MOFs has gained significant attention being a new class of adsorbents. A lot of MOFs have<br />

been evaluated for gas storage such as hydrogen and methane, [24, 26] which provides a<br />

safer and more economical gas storage method. For example, MOF-5 has shown a rapid<br />

and fully-reversible H2 storage density (66 g L -1 at 77 K, 100 bar), [148] which is very close<br />

to the value observed for liquid hydrogen (71 g L -1 at 20.4 K, 1 bar). Later, it was found<br />

that most of the MOFs like MOF-5 demonstrate poor performance at 298 K due to rather<br />

weak interactions between H2 and the framework. However, remarkable enhancement of<br />

H2 adsorption enthalpy can be achieved by designing MOFs with CUSs, [65, 70, 89]<br />

catenation/interpenetration [149] or MOFs with heavy transition metals (e.g. Pd) which can<br />

afford spillover effect for hydrogen storage. [150] For instance, respectively designed<br />

Mn3[(Mn4Cl)3(BTT)8]2 bearing CUSs exhibits H2 uptake of 1.49 total wt% and 12.1 g L -1 at<br />

298 K and 90 bar, [89] what is 77% greater than that of compressed H2 under the same<br />

conditions. Furthermore, HKUST-1 and Ni2(dobdc) have also demonstrated high total<br />

volumetric methane uptakes at 35 bar (225 and 235 v/v, respectively). [26] Significantly,<br />

PCN-14 (Cu2(adip) (adip 4- = 5,5’-(9,10-anthracenediyl)di-isophthalate) containing Cu-<br />

CUSs is also one of the best reported so far MOFs for methane storage (230 v/v, 290K, 35<br />

bar). Note, that 35 bar is the maximum pressure achievable by most inexpensive singlestage<br />

compressors, [151] which is also a widely used standard pressure for evaluating<br />

adsorbents for adsorbed natural gas storage. Both rigid and flexible MOFs as well as MOF<br />

membranes can be utilized as adsorbents for selective gas adsorption on the basis of

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