Patent classifications
B01J31/16
Metal organic frameworks and methods of making and using same
Metal Organic Framework (MOF) materials and methods of making MOF materials. The methods include grinding of mixtures of metal hydroxide(s) and ligand(s). The MOF materials may have at least two different ligands. The MOF materials may have open metal sites. The MOF materials can be used in gas storage applications.
Topical skin closure compositions and systems
Novel compositions and systems for closure of wounds are disclosed. The compositions provide devices of improved flexibility and elasticity and are readily applied to wound sites or over wound closure devices. The present invention is also directed to a novel platinum catalyst for use in such compositions. The catalyst provides for rapid curing on topical surfaces such as skin and bonds to such surfaces in about 2-5 minutes.
Nanoparticles of CO complexes of zero-valent metals that can be used as hydrosilylation and dehydrogenative silylation catalysts
Nanoparticles that can be used as hydrosilylation and dehydrogenative silylation catalysts. The nanoparticles have at least one transition metal with an oxidation state of 0, chosen from the metals of columns 8, 9 and 10 of the periodic table, and at least one carbonyl ligand, preferably a silicide.
4,4′-bipyridyl-ethylene MOFs of lead, zinc, or cadmium
Metal-organic frameworks (MOFs) may have Zn(II), Pb(II), and/or Cd(II) as a central metal ion; a 4,4′-bipyridylethylene (bpe) ligand as a first ligand; and fumaric acid (fum) and/or oxalic acid (ox) as a second ligand, wherein the 4,4′-bipyridylethylene ligands are stacked in the MOF, and wherein a distance between two consecutive 4,4′-bipyridylethylene ligands is less than 5 Å. Cycloadditions, particularly photoinduced [2+2] cycloadditions may be catalyzed by such MOFs, and/or the conversion of photoinduced [2+2] cycloadditions in inventive MOFs may be increased by mechanical force, such as by grinding.
Catalyst for water splitting
Methods for producing a carbon-free, PGM-free support for PGM catalyst. The catalytic material comprises PGM metals disposed on a carbon-free support which is catalytic but free of PGM.
AN IMPROVED PROCESS FOR PHOTOCATALYTIC HYDROCARBOXYLATION OF METHANOL WITH CO2 TO PRODUCE ACETIC ACID
The present invention discloses a photocatalytic process and methodology for the preparation of acetic acid by a hydrocarboxylation reaction of methanol using carbon dioxide under visible light irradiation. Importantly, the reaction occurred under ambient temperature and pressure condition using a readily available household LED lamp in the presence of a transition metal based molecular photocatalyst, homogeneous as well as supported to semiconductor support and a CO.sub.2-philic solvent without adding any external electron and proton donors.
PROPYLENE OXIDE PRODUCTION APPARATUS AND PROPYLENE OXIDE PRODUCTION METHOD
Provided is a propylene oxide production apparatus including a switching mechanism that is capable of switching a state of each reactor between an operating state where reaction raw materials are supplied and an epoxidation reaction is performed and a non-operating state where the supply of the reaction raw materials is shut off. The propylene oxide production apparatus is capable of changing a reactor in the non-operating state one by one, and performs switching in such a way that only reactors in the operating state are connected fluidically in series or in parallel, thereby enabling supplying the reaction raw materials to the reactors in the operating state. A sampling mechanism is also provided that samples part of the reaction mixture from each discharge line that is connected to each reactor.
PROPYLENE OXIDE PRODUCTION APPARATUS AND PROPYLENE OXIDE PRODUCTION METHOD
Provided is a propylene oxide production apparatus including a switching mechanism that is capable of switching a state of each reactor between an operating state where reaction raw materials are supplied and an epoxidation reaction is performed and a non-operating state where the supply of the reaction raw materials is shut off. The propylene oxide production apparatus is capable of changing a reactor in the non-operating state one by one, and performs switching in such a way that only reactors in the operating state are connected fluidically in series or in parallel, thereby enabling supplying the reaction raw materials to the reactors in the operating state. A sampling mechanism is also provided that samples part of the reaction mixture from each discharge line that is connected to each reactor.
METHOD FOR SYNTHESIZING 2D ULTRATHIN ZIF-67 WITH HIERARCHICAL POROUS STRUCTURE
The disclosure is related to the field of preparation of nanometer materials, and, in particular, to a method for synthesizing a 2D ultrathin zeolitic imidazolate framework-67 (ZIF-67) with a hierarchical porous structure, the method converting ZIF-67 from nanoparticles into 2D ultrathin nanosheets with a hierarchical porous structure by controlling a dropping amount of water and the reaction time. With the method, the 2D ultrathin ZIF-67 with a hierarchical porous structure can be made from readily available starting materials in a one pot synthesis. The method is feasible on industrial scale and has both economic and environmental benefits due to the simple process and low cost.
INHIBITORS OF HYDROSILYLATION CATALYSTS
A composition containing the following components: (a) a hydrosilylation catalyst comprising a metal-ligand complex, and (b) an inhibitor of the catalyst, wherein the inhibitor differs from the ligand of the metal-ligand complex and is represented by formula (I):
X—CHR—CO—Y (I),
wherein —X represents —NO.sub.2, —S(═O)R, or R.sup.c.sub.2R.sup.aC—CO—; Y represents 2-furyl, —S(═O)R, —CN, —NO.sub.2, or —CR.sup.b.sub.xR.sup.d.sub.3-x; R.sup.a and R.sup.b is independently selected from the group consisting of —O—R, —O—CO—R, —CO—O—R, 2-furyl, —S(═O)R, —CN, —NO.sub.2, —F, —Cl, and —Br; each of R is independently selected from the group consisting of —H, optionally fluorinated C.sub.1-C.sub.8-alkyl, —F, —Cl, and —Br; each of R.sup.c and each of R.sup.d is independently selected from the group consisting of —H, optionally fluorinated C.sub.1-C.sub.8-alkyl, —F, —Cl, and —Br; and x is 0 or 1.