Process for formaldehyde manufacture
View Patent ↗A process for the production of formaldehyde from methanol comprising the steps of: feeding to a reactor a feed stream comprising the methanol and an oxygen-containing gas; reacting the methanol in the gas phase with the oxygen-containing gas in the reactor in the presence of a catalyst comprising oxides of iron and molybdenum; and recovering a formaldehyde reactor outlet stream from the reactor, the formaldehyde reactor outlet stream comprising formaldehyde and carbon monoxide. The catalyst comprises copper in an amount of at least 0.025 wt %, or at least 0.05 wt %, of the catalyst and in that the molar ratio of carbon monoxide to formaldehyde in the formaldehyde reactor outlet stream is at least 5% less than the molar ratio of carbon monoxide to formaldehyde in the formaldehyde reactor outlet stream in the same process using a catalyst containing essentially no copper.
1 . A process for the production of formaldehyde from methanol comprising the steps of:
feeding to a reactor a feed stream comprising the methanol and an oxygen-containing gas;
reacting the methanol in the gas phase with the oxygen-containing gas in the reactor in the presence of a catalyst comprising oxides of iron and molybdenum and copper in an amount of at least 0.025 wt % of the catalyst; and
recovering a formaldehyde reactor outlet stream from the reactor, the formaldehyde reactor outlet stream comprising formaldehyde and carbon monoxide,
wherein the CO loss is reduced such that the molar ratio of carbon monoxide to formaldehyde in the formaldehyde reactor outlet stream is at least 0.25% less than the molar ratio of carbon monoxide to formaldehyde in the formaldehyde reactor outlet stream in the same process using a catalyst containing essentially no copper.
2 . A process for the production of formaldehyde from methanol comprising the steps of:
feeding to a reactor a feed stream comprising the methanol and an oxygen-containing gas;
reacting the methanol in the gas phase with the oxygen-containing gas in the reactor in the presence of a catalyst comprising oxides of iron and molybdenum; and
recovering a formaldehyde reactor outlet stream comprising formaldehyde and carbon monoxide from the reactor;
wherein the catalyst comprises copper in an amount of at least 0.025 wt % of the catalyst.
3 . A process for the production of formaldehyde from methanol comprising the steps of:
feeding to a reactor a feed stream comprising the methanol and an oxygen-containing gas;
reacting the methanol in the gas phase with the oxygen-containing gas in the reactor in the presence of a catalyst comprising oxides of iron and molybdenum and copper in an amount of at least 0.025 wt % of the catalyst; and
recovering a formaldehyde reactor outlet stream from the reactor, the formaldehyde reactor outlet stream comprising formaldehyde and carbon monoxide,
wherein the methyl formate loss is reduced such that the molar ratio of methyl formate to formaldehyde in the formaldehyde reactor outlet stream is at least 0.01% less than the molar ratio of methyl formate to formaldehyde in the formaldehyde reactor outlet stream in the same process using a catalyst containing essentially no copper.
4 . The process according to claim 1 , wherein the catalyst comprises copper in an amount of at least 0.05 wt % of the catalyst.
5 . The process according to claim 1 , wherein the reactor is operated at an inlet pressure of at least 1 barg.
6 . The process according to claim 1 , wherein said oxygen-containing gas is air.
7 . The process according to claim 1 , wherein the catalyst has been calcined at a temperature of not more than 525° C.
8 . The process according to claim 7 , wherein the catalyst has been calcined at a temperature of at least 425° C.
9 . The process according to claim 2 , wherein the catalyst comprises copper in an amount of at least 0.05 wt % of the catalyst.
10 . The process according to claim 2 , wherein the reactor is operated at an inlet pressure of at least 1 barg.
11 . The process according to claim 2 , wherein said oxygen-containing gas is air.
12 . The process according to claim 2 , wherein the catalyst has been calcined at a temperature of not more than 525° C.
13 . The process according to claim 11 , wherein the catalyst has been calcined at a temperature of at least 425° C.
14 . The process according to claim 3 , wherein the catalyst comprises copper in an amount of at least 0.05 wt % of the catalyst.
15 . The process according to claim 3 , wherein the reactor is operated at an inlet pressure of at least 1 barg.
16 . The process according to claim 3 , wherein said oxygen-containing gas is air.
17 . The process according to claim 3 , wherein the catalyst has been calcined at a temperature of not more than 525° C.
18 . The process according to claim 16 , wherein the catalyst has been calcined at a temperature of at least 425° C.