CARBON SORBENT-AZOBENZENE HYBRIDS FOR CARBON CAPTURE AND METHODS OF PRODUCING AND/OR USING SAID HYBRIDS
20250065300 ยท 2025-02-27
Inventors
Cpc classification
B01J20/3204
PERFORMING OPERATIONS; TRANSPORTING
B01J20/3253
PERFORMING OPERATIONS; TRANSPORTING
B01D53/02
PERFORMING OPERATIONS; TRANSPORTING
B01J20/3217
PERFORMING OPERATIONS; TRANSPORTING
B01D2253/25
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J20/20
PERFORMING OPERATIONS; TRANSPORTING
B01J20/32
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Modified carbon-based sorbents configured for improved carbon capture, methods for increasing CO.sub.2 capture potential of modified carbon-based sorbents, and methods for improving noncovalent interactions of modified carbon-based sorbents with CO.sub.2, N.sub.2, and H.sub.2 are disclosed herein. The modified carbon-based sorbents have porous carbon surfaces and/or mesoporous carbon surfaces comprising one or more in-plane sites having at least one first nitrogen functionality and one or more out-of-plane sites having at least one second nitrogen functionality, wherein the at least one first nitrogen functionality is a different nitrogen functionality than the at least one second nitrogen functionality. The methods comprise contacting the modified carbon-based sorbents to gaseous streams containing CO.sub.2.
Claims
1. A carbon-based sorbent configured for improved carbon capture, the carbon-based sorbent comprising: at least one modified carbon-based sorbent comprising porous carbon surfaces and/or mesoporous carbon surfaces configured to improve selective CO.sub.2 adsorption, wherein the porous carbon surfaces and/or the mesoporous carbon surfaces comprise one or more in-plane sites having at least one first nitrogen functionality and one or more out-of-plane sites having at least one second nitrogen functionality, and the at least one first nitrogen functionality is a different nitrogen functionality than the at least one second nitrogen functionality.
2. The carbon-based sorbent of claim 1, wherein the one or more in-plane sites is/are one or more nitrogen doping sites.
3. The carbon-based sorbent of claim 2, wherein the one or more in-plane sites is/are one or more graphitic-N sites, one or more pyrrolic-N sites, one or more pyridinic-N sites, one or more pyridine-N sites, or a combination thereof.
4. The carbon-based sorbent of claim 2, wherein the one or more out-of-plane sites is/are one or more azobenzene-N sites.
5. The carbon-based sorbent of claim 1, wherein the one or more in-plane sites are at least one graphitic-N site, at least one pyrrolic-N site, at least one pyridinic-N site, and at least one pyridine-N site, and the one or more out-of-plane sites are one or more azobenzene-N sites.
6. The carbon-based sorbent of claim 1, wherein the at least one modified carbon-based sorbent is a carbon sorbent-azobenzene hybrid.
7. The carbon-based sorbent of claim 6, wherein the carbon sorbent azobenzene hybrid is a N-doped-carbon sorbent-azobenzene hybrid.
8. A method for increasing CO.sub.2 capture potential of at least one modified carbon-based sorbent, the method comprising: covalently functionalizing at least one carbon lattice of a carbon-based sorbent comprising porous carbon surfaces and/or mesoporous carbon surfaces; incorporating one or more in-plane CO.sub.2 philic groups and one or more out-of-plane CO.sub.2 philic groups into the carbon-based sorbent; and incorporating one or more out-of-carbon lattice plane nitrogen functionalities into the carbon-based sorbent to produce the at least one modified carbon-based sorbent.
9. The method of claim 1, wherein the at least one modified carbon-based sorbent is a carbon sorbent-azobenzene hybrid.
10. The method of claim 9, wherein the carbon sorbent azobenzene hybrid is a N-doped-carbon sorbent-azobenzene hybrid.
11. The method of claim 8, wherein the one or more in-plane CO.sub.2 philic groups comprise nitrogen doping groups.
12. The method of claim 11, wherein the nitrogen doping groups are one or more graphitic-based groups, one or more pyrrolic-based groups, one or more pyridinic-based groups, one or more pyridine-based sites, or a combination thereof.
13. The method of claim 11, wherein the one or more out-of-plane CO.sub.2 philic groups is/are one or more azobenzene-based groups.
14. The method of claim 8, wherein the one or more in-plane CO.sub.2 philic groups are at least one graphitic-N group, at least one pyrrolic-N group, at least one pyridinic-N group, and at least one pyridine-N group, and the one or more out-of-plane CO.sub.2 philic groups are one or more azobenzene-N groups.
15. The method of claim 8, further comprising: improving selective CO.sub.2 adsorption by simultaneously activating the one or more in-plane CO.sub.2 philic groups and the one or more out-of-plane CO.sub.2 philic groups.
16. A method for improving noncovalent interactions of a modified carbon-based sorbent with CO.sub.2, N.sub.2, and H.sub.2, the method comprising: providing the modified carbon-based sorbent comprising porous carbon surfaces and/or mesoporous carbon surfaces; and simultaneously activating one or more in-plane sites and one or more out-of-plane sites of the porous carbon surfaces and/or the mesoporous carbon surfaces, wherein the one or more in-plane sites have at least one first nitrogen functionality that is a different nitrogen functionality than at least one second nitrogen functionality of the one or more out-of-plane sites.
17. The method of claim 16, further comprising: selectively capturing CO.sub.2 with the modified carbon-based sorbent during syngas processing, post-combustion processing, or pre-combustion processing.
18. The method of claim 16, wherein the modified carbon-based sorbent is a carbon sorbent-azobenzene hybrid or a N-doped-carbon sorbet-azobenzene hybrid.
19. The method of claim 16, wherein the one or more in-plane sites is/are nitrogen doping sites and the one or more out-of-plane sites is/are azobenzene-N sites.
20. The method of claim 16, further comprising: contacting the modified carbon-based sorbent to at least one gaseous stream comprising CO.sub.2 therein.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0026] The present disclosure is best understood from the following detailed description when read with the accompanying figures. It is emphasized that, in accordance with the standard practice in the industry, various features are not drawn to scale. In fact, the dimensions of the various features may be arbitrarily increased or reduced for clarity of discussion.
[0027]
[0028]
[0029]
[0030]
[0031]
DETAILED DESCRIPTION
[0032] Illustrative examples of the subject matter claimed below will now be disclosed. In the interest of clarity, not all features of an actual implementation are described in this specification. It will be appreciated that in the development of any such actual implementation, numerous implementation-specific decisions may be made to achieve the developers' specific goals, such as compliance with system-related and business-related constraints, which will vary from one implementation to another. Moreover, it will be appreciated that such a development effort, even if complex and time-consuming, would be a routine undertaking for those of ordinary skill in the art having the benefit of this disclosure.
[0033] Further, as used herein, the article a is intended to have its ordinary meaning in the patent arts, namely one or more. Herein, the term about when applied to a value generally means within the tolerance range of the equipment used to produce the value, or in some examples, means plus or minus 10%, or plus or minus 5%, or plus or minus 1%, unless otherwise expressly specified. Further, herein the term substantially as used herein means a majority, or almost all, or all, or an amount with a range of about 51% to about 100%, for example. Moreover, examples herein are intended to be illustrative only and are presented for discussion purposes and not by way of limitation.
[0034] The present disclosure is directed to and relates to one or more carbon sorbent-azobenzene (hereinafter CS-AZO) hybrids (hereinafter CS-AZO hybrids) for carbon capture, one or more methods of producing or providing the CS-AZO hybrids, and one or more methods of using the CS-AZO hybrids to capture carbon. The CS-AZO hybrids include, comprise, or consist of at least one enhanced surface chemistry (hereinafter the surface chemistry) that surprisingly achieves improved carbon capture and/or CO.sub.2 adsorption. In some embodiments, the at least one enhanced surface chemistry is configured for selective CO.sub.2 absorption and/or capture in porous carbon surfaces, mesoporous carbon surfaces, or a combination thereof. Further, the CS-AZO hybrids may utilize, have, comprise, or consist of one or more porous carbon surfaces and/or one or more mesoporous carbon surfaces with one or more varied nitrogen functionalities including one or more in-plane nitrogen doping sites, one or more in-plane azo groups, and/or one or more out-of-plane azo groups. Embodiments of the surface chemistry disclosed herein may engage in or facilitate selective CO.sub.2 adsorption and/or the one or more N doping sites may include, for example, one or more graphitic groups, one or more pyrrolic groups, one or more pyridinic groups, one or more pyridine groups, or a combination thereof. In at least one embodiment, the methods disclosed herein may utilize the CS-AZO hybrids to benefit or improve at least one of syngas processing, post-combustion CO.sub.2 capture, pre-combustion CO.sub.2 capture, or a combination thereof. Moreover, the surface chemistry disclosed herein may simultaneously provide one or more in-plane sites and/or one or more out-of-plane sites with one or more different nitrogen functionalities including the one or more N doping sites and one or more azo groups. In at least one embodiment, the one or more different nitrogen functionalities may be, comprise, or consist of at least one graphitic group, at least one pyrrolic group, at least one pyridinic group, at least one pyridine group, or a combination thereof.
[0035] The enhanced surface chemistry, disclosed herein, of porous carbon, mesoporous carbon, or both porous and mesoporous carbon for boosting selective CO.sub.2 adsorption occurs when both in-plane sites and out-of-plane sites, each providing different nitrogen functionalities, are simultaneously activated in some embodiments. In embodiments, the in-plane sites serve as or provide nitrogen doping sites (i.e., graphitic, pyrrolic, pyridinic and/or pyridine groups) and the out-of-plane sites are targeted to be or provide one or more azo groups. Two sorbents in this modified carbon sorbent class may include, in some embodiments: (i)CS-AZO; and (ii)N-doped-carbon sorbent-azobenzene (hereinafter N-CS-AZO). Additionally, some embodiments of the enhanced surface chemistry may benefit from an electron transfer scheme for synthesis of CS-AZO hybrids. The resulting surface chemistry engineering approach enables one or more molecular level adjustments of electron distributions and surface polarities, thereby optimizing one or more noncovalent interactions of one or more modified carbon sorbent surfaces with gases, such as, for example, CO.sub.2, N.sub.2, H.sub.2, or a combination thereof.
[0036] In one or more embodiments, one or more diazonium chemistries may produce, provide, and/or manufacture one or more nitrogen rich porous carbon adsorbents. The enhanced surface chemistry of the porous carbon and/or the mesoporous carbon for boosting and/or improving the selective CO.sub.2 adsorption may be selected and/or achieved when the one or more diazonium chemistries are utilized and/or reacted. With simultaneous activation of both the in-plane sites and the out-of-plane sites, each of the sites may provide the one or more different nitrogen functionalities. For example, the in-plane sites may produce, provide, or serving as the nitrogen doping sites (i.e., graphitic, pyrrolic, pyridinic and pyridine) and the out-of-plane sites may produce, provide, or are targeted to be the azo groups. In some embodiments, two sorbents in this modified carbon sorbent class are: (i)CS-AZO; and (ii)N-CS-AZO as shown in
[0037] In some embodiments, at least one carbon matrix of adsorbents disclosed herein have enhanced and/or improved CO.sub.2 selectivity. Two strategies disclosed herein improve the selectivity for CO.sub.2 in carbon sorbents, wherein the first strategy comprises dispersing one or more aqueous amines in the carbon matrix and the second strategy comprises doping or incorporating of nitrogen into the carbon lattice/carbon surface/graphene lattice. For example, one or more nitrogen doping schemes may be based on nitrogen functionalities (i.e., pyridinic, pyrrolic, and graphitic groups) and are classified as N-containing heterocycles. One or more synthesis routes are used to incorporate the nitrogen into the carbon matrix, wherein the one or more synthesis routes may comprise treating pristine carbon sorbent with ammonia at temperatures ranging from 200 to 800 C. or deliberate selecting nitrogen containing carbon precursors, such a melamine. However, some carbon sorbents may suffer from weak in-plane physisorption of CO.sub.2 with the nitrogen donor which may limit their selectivity. Thus, tailoring the carbon surface chemistry to maximize the synergistic effect of local dipole-IT and dipole-quadrupole interactions on carbon and different nitrogen functionalities is required. The limitation of nitrogen doping schemes may be address by incorporating different CO.sub.2-philic groups into the sorbent frameworks, wherein carbon sorbents may be based on (i) at least one pristine carbon surface and (ii) one or more N-containing carbon heterocycles.
[0038]
[0039]
[0040]
[0041] In one or more embodiments, at least one electron transfer diazonium chemistry may be utilized and/or reacted for synthesis of one or more CS-AZO hybrids. The at least one electron transfer diazonium chemistry may be initiated by placing at least one carbon sorbent in a reactor with an aqueous solution of 0.5 to 2 weight percent anionic surfactant. Diazonium salt is injected in a reactor vessel which is heated (45 to 50 C.) and stirred. The reaction involves electron-transfer from the carbon lattice to the diazo moiety, which leads to cleavage of dinitrogen and generation of one or more aryl radicals. The one or more aryl radicals bind to the surface of carbon sorbent via one or more covalent bonds. Anionic surfactant, such as, for example, a diazonium ion is cationic, and hence the anionic surfactant may significantly increase the ability of the surfactant layer to stabilize the diazonium ion near the carbon sorbent surface.
[0042] In some embodiments, N.sub.2 and CO.sub.2 molecularly binds with the diazo bridge in post-combustion mixtures as shown in
[0043]
[0044] In one or more embodiments, one or more CCUS technologies may include, incorporate, and/or utilize the CS-AZO hybrids disclosed herein for the CO.sub.2 capture, CO.sub.2 utilization, CO.sub.2 storage, or a mixture thereof. The CS-AZO hybrids disclosed herein may be, have, achieve, exhibit, and/or provide improved higher CO.sub.2 absorption efficiencies, improved higher loading capacities, or a combination thereof. As a result, the CS-AZO hybrids disclosed herein may be included, incorporated, and/or utilized in one or more industrial scale applications to capture CO.sub.2 from, for example, one or more natural gas extractions, one or more gas refineries, and/or one or more exhaust gases produced by one or more fossil fuel-fired power generations. In some embodiments, methods disclosed herein may utilize the CS-AZO hybrids to remove CO.sub.2 from one or more gaseous streams, such as, for example, a flue gas, a natural gas, a hydrogen gas, a synthesis gas, one or more waste gas streams, or a combination thereof. In an embodiment, these methods may utilize the CS-AZO hybrids disclosed herein to contact at least one gaseous stream and/or capture CO.sub.2 of the at least one gaseous stream.
[0045] The foregoing description, for purposes of explanation, used specific nomenclature to provide a thorough understanding of the disclosure. However, it will be apparent to one skilled in the art that the specific details are not required in order to practice the systems and methods described herein. The foregoing descriptions of specific examples are presented for purposes of illustration and description. They are not intended to be exhaustive of or to limit this disclosure to the precise forms described. Obviously, many modifications and variations are possible in view of the above teachings. The examples are shown and described in order to best explain the principles of this disclosure and practical applications, to thereby enable others skilled in the art to best utilize this disclosure and various examples with various modifications as are suited to the particular use contemplated. It is intended that the scope of this disclosure be defined by the claims and their equivalents below.