The present invention provides a method for preparing acrylic acid and methyl acrylate. The method comprises passing the feed gas containing dimethoxymethane and carbon monoxide through a solid acid catalyst to generate acrylic acid and methyl acrylate with a high conversion rate and selectivity at a reaction temperature in a range from 180 to 400 and a reaction pressure in a range from 0.1 MPa to 15.0 MPa, the mass space velocity of dimethoxymethane in the feed gas is in a range from 0.05 h.sup.−1 to 10.0 h.sup.−1, and the volume percentage of dimethoxymethane in the feed gas is in a range from 0.1% to 95%.

The present invention provides a method for preparing acrylic acid and methyl acrylate. The method comprises passing the feed gas containing dimethoxymethane and carbon monoxide through a solid acid catalyst to generate acrylic acid and methyl acrylate with a high conversion rate and selectivity at a reaction temperature in a range from 180 to 400 and a reaction pressure in a range from 0.1 MPa to 15.0 MPa, the mass space velocity of dimethoxymethane in the feed gas is in a range from 0.05 h.sup.−1 to 10.0 h.sup.−1, and the volume percentage of dimethoxymethane in the feed gas is in a range from 0.1% to 95%.

The present invention provides a method for preparing acrylic acid and methyl acrylate. The method comprises passing the feed gas containing dimethoxymethane and carbon monoxide through a solid acid catalyst to generate acrylic acid and methyl acrylate with a high conversion rate and selectivity at a reaction temperature in a range from 180 to 400 and a reaction pressure in a range from 0.1 MPa to 15.0 MPa, the mass space velocity of dimethoxymethane in the feed gas is in a range from 0.05 h.sup.−1 to 10.0 h.sup.−1, and the volume percentage of dimethoxymethane in the feed gas is in a range from 0.1% to 95%.

A process for the production of methyl acetate by carbonylating at a temperature of 250 to 350° C., in the presence of a zeolite catalyst, a feed comprising dimethyl ether, a gas comprising carbon monoxide and hydrogen at a molar ratio of hydrogen to carbon monoxide of at least 1, methyl acetate and one or more compounds containing a hydroxyl functional group.

A process for the production of methyl acetate by carbonylating at a temperature of 250 to 350° C., in the presence of a zeolite catalyst, a feed comprising dimethyl ether, a gas comprising carbon monoxide and hydrogen at a molar ratio of hydrogen to carbon monoxide of at least 1, methyl acetate and one or more compounds containing a hydroxyl functional group.

A process for the production of methyl acetate by carbonylating at a temperature of 250 to 350° C., in the presence of a zeolite catalyst, a feed comprising dimethyl ether, a gas comprising carbon monoxide and hydrogen at a molar ratio of hydrogen to carbon monoxide of at least 1, methyl acetate and one or more compounds containing a hydroxyl functional group.

A method of preparing β-hydroxycarboxylic acid ester comprises mixing an alkylene oxide, a monohydric alcohol and a composite catalyst, and performing a carbonylation esterification reaction in a carbon monoxide atmosphere to obtain the β-hydroxycarboxylic acid ester. The composite catalyst comprises a main catalyst, a cocatalyst and a reducing agent. the main catalyst is at least one of a cobalt salt, cobalt oxide and cobalt hydroxide. The cocatalyst is a nitrogen-containing heterocyclic compound. The reducing agent is a base metal. The method is an atomic reaction type process, does not produce three wastes, and has high conversion rate. It is a green environmental protection process. The composite catalyst used does not contain Co.sub.2(CO).sub.8. The raw materials and catalyst used are all cheap and easily available. The composite catalyst can be used repeatedly at a lower cost, and is suitable for industrial applications.

A method of preparing β-hydroxycarboxylic acid ester comprises mixing an alkylene oxide, a monohydric alcohol and a composite catalyst, and performing a carbonylation esterification reaction in a carbon monoxide atmosphere to obtain the β-hydroxycarboxylic acid ester. The composite catalyst comprises a main catalyst, a cocatalyst and a reducing agent. the main catalyst is at least one of a cobalt salt, cobalt oxide and cobalt hydroxide. The cocatalyst is a nitrogen-containing heterocyclic compound. The reducing agent is a base metal. The method is an atomic reaction type process, does not produce three wastes, and has high conversion rate. It is a green environmental protection process. The composite catalyst used does not contain Co.sub.2(CO).sub.8. The raw materials and catalyst used are all cheap and easily available. The composite catalyst can be used repeatedly at a lower cost, and is suitable for industrial applications.

A method of preparing β-hydroxycarboxylic acid ester comprises mixing an alkylene oxide, a monohydric alcohol and a composite catalyst, and performing a carbonylation esterification reaction in a carbon monoxide atmosphere to obtain the β-hydroxycarboxylic acid ester. The composite catalyst comprises a main catalyst, a cocatalyst and a reducing agent. the main catalyst is at least one of a cobalt salt, cobalt oxide and cobalt hydroxide. The cocatalyst is a nitrogen-containing heterocyclic compound. The reducing agent is a base metal. The method is an atomic reaction type process, does not produce three wastes, and has high conversion rate. It is a green environmental protection process. The composite catalyst used does not contain Co.sub.2(CO).sub.8. The raw materials and catalyst used are all cheap and easily available. The composite catalyst can be used repeatedly at a lower cost, and is suitable for industrial applications.

The present invention provides a method for preparing acrylic acid and methyl acrylate. The method comprises passing the feed gas containing dimethoxymethane and carbon monoxide through a solid acid catalyst to generate acrylic acid and methyl acrylate with a high conversion rate and selectivity at a reaction temperature in a range from 180 to 400 and a reaction pressure in a range from 0.1 MPa to 15.0 MPa, the mass space velocity of dimethoxymethane in the feed gas is in a range from 0.05 h.sup.−1 to 10.0 h.sup.−1, and the volume percentage of dimethoxymethane in the feed gas is in a range from 0.1% to 95%.