Catalysts containing a support and a metal oxide, and reactors and methods of using the catalysts in a carbonylation reaction, such as alcohol carbonylation and ester carbonylation, are described herein. The support is typically chemically inert and has a high surface area. The metal oxide typically contains a transition metal or a mixture of metals, such as rhenium, aluminum, tungsten, molybdenum, or a combination thereof. Typically, the metal oxide is mainly atomically dispersed on the surface of the support, as indicated by STEM. For example, at least 10% of the metal oxide is atomically dispersed on the surface of the support. The method includes (i) exposing a mixture of one or more alcohols or one or more esters and carbon monoxide to the catalyst. Typically, the one or more alcohols or one or more esters and carbon monoxide are in a gas phase.

Catalysts containing a support and a metal oxide, and reactors and methods of using the catalysts in a carbonylation reaction, such as alcohol carbonylation and ester carbonylation, are described herein. The support is typically chemically inert and has a high surface area. The metal oxide typically contains a transition metal or a mixture of metals, such as rhenium, aluminum, tungsten, molybdenum, or a combination thereof. Typically, the metal oxide is mainly atomically dispersed on the surface of the support, as indicated by STEM. For example, at least 10% of the metal oxide is atomically dispersed on the surface of the support. The method includes (i) exposing a mixture of one or more alcohols or one or more esters and carbon monoxide to the catalyst. Typically, the one or more alcohols or one or more esters and carbon monoxide are in a gas phase.

Catalysts containing a support and a metal oxide, and reactors and methods of using the catalysts in a carbonylation reaction, such as alcohol carbonylation and ester carbonylation, are described herein. The support is typically chemically inert and has a high surface area. The metal oxide typically contains a transition metal or a mixture of metals, such as rhenium, aluminum, tungsten, molybdenum, or a combination thereof. Typically, the metal oxide is mainly atomically dispersed on the surface of the support, as indicated by STEM. For example, at least 10% of the metal oxide is atomically dispersed on the surface of the support. The method includes (i) exposing a mixture of one or more alcohols or one or more esters and carbon monoxide to the catalyst. Typically, the one or more alcohols or one or more esters and carbon monoxide are in a gas phase.

A system and method for removing acetaldehyde from an acetic acid system, including providing a solution from the acetic acid system, the stream having methyl iodide and acetaldehyde, and contacting the solution with a polymer-bound polyol.

A system and method for removing acetaldehyde from an acetic acid system, including providing a solution from the acetic acid system, the stream having methyl iodide and acetaldehyde, and contacting the solution with a polymer-bound polyol.

Provided is a process for the preparation of certain 1,4-bicyclo[2.2.2]octane derivatives. The new synthetic procedure involves treating 1,4-dimethylene cyclohexane with an oxidizing agent in the presence of a transition metal catalyst to afford an oxo-substituted bicyclo[2.2.2]octane species. This intermediate structure can then be further derivatized. The processes of this disclosure thus affords a novel and simplified means for the commercial production of a wide variety of bicyclo[2.2.2]octane derivatives.

Provided is a process for the preparation of certain 1,4-bicyclo[2.2.2]octane derivatives. The new synthetic procedure involves treating 1,4-dimethylene cyclohexane with an oxidizing agent in the presence of a transition metal catalyst to afford an oxo-substituted bicyclo[2.2.2]octane species. This intermediate structure can then be further derivatized. The processes of this disclosure thus affords a novel and simplified means for the commercial production of a wide variety of bicyclo[2.2.2]octane derivatives.

Provided is a process for the preparation of certain 1,4-bicyclo[2.2.2]octane derivatives. The new synthetic procedure involves treating 1,4-dimethylene cyclohexane with an oxidizing agent in the presence of a transition metal catalyst to afford an oxo-substituted bicyclo[2.2.2]octane species. This intermediate structure can then be further derivatized. The processes of this disclosure thus affords a novel and simplified means for the commercial production of a wide variety of bicyclo[2.2.2]octane derivatives.

The present invention concerns a method of production for carbon monoxide using a derivative of formic acid, in particular an alkyl formate. It also concerns a method chosen from among, the method of production of methanol, the method of production of acetic acid (Monsanto and Cativa methods), the method of hydroformylation of olefins (oxo and aldox method, the method of production of hydrocarbons (Fischer-Tropsch method), or the method of carbonylation of nickel (Mond method), comprising a step of production of carbon monoxide using an alkyl formate of formula (I) by the method according to the invention. It further concerns a “CO pump” or “CO liquid storage” method comprising a step of production of carbon monoxide using an alkyl formate of formula (I) according to the method of the invention.

The present invention concerns a method of production for carbon monoxide using a derivative of formic acid, in particular an alkyl formate. It also concerns a method chosen from among, the method of production of methanol, the method of production of acetic acid (Monsanto and Cativa methods), the method of hydroformylation of olefins (oxo and aldox method, the method of production of hydrocarbons (Fischer-Tropsch method), or the method of carbonylation of nickel (Mond method), comprising a step of production of carbon monoxide using an alkyl formate of formula (I) by the method according to the invention. It further concerns a “CO pump” or “CO liquid storage” method comprising a step of production of carbon monoxide using an alkyl formate of formula (I) according to the method of the invention.