Reaction process involving capillary condensation within a microporous catalyst
Described herein is a catalytic reaction process including introducing one or more gas-phase reactants into a reactor comprising a microporous catalyst having a pore size less than or equal to 2 nm and adjusting the temperature and/or the pressure of the reactor such that one or more of the gas-phase reactants condense within the micropores of the catalyst thereby causing the catalytic reaction to take place in a liquid phase. Additionally, a process for engineering defects on a carboxylate-based metal organic framework (MOF) catalyst is described. The process includes providing a carboxylate-based MOF catalyst; and heating the carboxylate-based MOF catalyst in an inert gas atmosphere at temperatures between about 150° C. and about 900° C.
1. A catalytic reaction process comprising
providing a reactor comprising a microporous catalyst having a defined pore size distribution with a pore diameter ≤2 nm, thereby allowing a controlled pore-filling, wherein the reactor operates at a temperature in a range of about −30° C. to about 100° C. and at a pressure in a range of about 0.1 MPa and about 10 MPa,
heating the microporous catalyst in an inert gas atmosphere at a temperature between about 150° C. and about 900° C., wherein the microporous catalyst comprises a carboxylate-based metal-organic framework (MOF) catalyst,
introducing one or more gas-phase reactants into the reactor,
adjusting the temperature and/or the pressure of the reactor such that one or more of the gas-phase reactants condense to form a liquid phase fraction within the micropores of the catalyst, wherein the liquid phase fraction in the micropores is controlled to achieve a mixed liquid/gas phase within the micropores such that the catalytic reaction takes place in a liquid phase.
2. The process of claim 1 , wherein in the inert gas comprises N 2 .
3. The process of claim 1 , wherein the catalytic reaction comprises C—C coupling reactions or chain-growth reactions, ethylene epoxidation, ethylene hydrochlorination, CO hydrogenation reactions, or CO 2 hydrogenation reactions.
4. A process for converting ethylene into its associated oligomer, the process comprising
providing a reactor comprising a microporous catalyst having a pore size ≤2 nm, wherein the reactor operates at a temperature between about −30° C. and about 200° C. and at a pressure between about 0.1 MPa and about 10 MPa
heating the microporous catalyst in an inert gas atmosphere at a temperature between about 150° C. and about 900° C., wherein the microporous catalyst comprises a metal-organic framework (MOF) catalyst,
introducing a gas-phase ethylene reactant into the reactor, and
adjusting the temperature and/or the pressure of the reactor such that at least a portion of the gas-phase ethylene reactant condenses within the micropores of the catalyst thereby causing the catalytic reaction to take place in a liquid phase.
5. The process of claim 4 , wherein the microporous catalyst comprises a carboxylate-based MOF catalyst.
6. The process of claim 5 , wherein in the inert gas comprises N 2 .
7. The process of claim 4 , wherein the catalyst includes a Ruthenium (RU) based MOF.
8. A process for converting a C 2 -C 4 alkene into its associated oligomer, the process comprising
providing a reactor comprising a microporous catalyst having a pore size <2 nm, wherein the reactor operates at a temperature between about −30° C. and about 200° C. and at a pressure between about 0.1 MPa and about 10 MPa,
heating the microporous catalyst in an inert gas atmosphere at a temperature between about 150° C. and about 900° C., wherein the microporous catalyst comprises a carboxylate-based metal-organic framework (MOF) catalyst,
introducing a gas-phase C 2 -C 4 alkene reactant into the reactor, and
adjusting the temperature and/or the pressure of the reactor such that at least a portion of the gas-phase C 2 -C 4 alkene reactant condenses within the micropores of the catalyst thereby causing the catalytic reaction to take place in a liquid phase.
9. The process of claim 8 , wherein in the inert gas comprises N 2 .
10. The process of claim 8 , wherein the microporous catalyst comprises a metal organic framework (MOF), zeolites, zeotypes, covalent organic frameworks (COF), porous organic polymers, porous molecular solids, porous carbons, or other porous catalysts containing silica, organosilica, silicoaluminate, aluminophosphate, titania, zirconia, and/or ceria.
11. The process of claim 10 , wherein the MOF catalyst comprises metals from alkali metals, alkali earth metals, transition metals, rare earth metals or other metals.
12. The process of claim 10 , wherein the MOF catalyst comprises Mg, V, Cr, Mo, Zr, Hf, La, Zr, Mn, Fe, Co, Cu, Ni, Zn, Ru, Al, Ga, or mixtures thereof.
13. The process of claim 8 , wherein the C 2 -C 4 alkene comprises ethylene.
14. The process of claim 8 , wherein the reactor operates at a temperature between about 0° C. and 100° C.
15. The process of claim 8 , wherein the reactor operates at a pressure between about 3.0 MPa and 4.5 MPa.
16. The process of claim 8 , wherein the reactor operates at a pressure between about 3.5 MPa and 4.5 MPa.
17. The process of claim 8 , wherein the C 2 -C 4 alkene has a saturation pressure Psat at the operating temperature, and wherein the reactor is operated at a pressure P such that a relative saturation pressure for the reactor is P/P sat is >0.4.
18. The process of claim 7 , wherein the reactor operates at a temperature between about 0° C. and about 60° C. and at a pressure between about 3.3 MPa and about 4.2 MPa.
19. The process of claim 7 , wherein after heating the RU-based MOF, the RU based MOF includes at least one catalytically active open metal site.
20. The process of claim 7 , wherein the inert gas includes nitrogen, wherein the temperature is between 200° C.-300° C., wherein the RU-based MOF includes at least one catalytically active open metal site after being heated.