Method and system for producing low carbon olefins from aqueous feedstock
A low-carbon olefin and raw material technology, applied in the field of low-carbon olefin and system from water-containing raw materials, can solve the problem of low olefin yield and achieve high conversion rate and good technical effect
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Embodiment 1
[0057] The water-containing raw material (4) enters the system of the present invention and contacts with the catalyst to generate a reaction product (7) rich in carbon number less than or equal to 6 olefins, wherein the mass percentage of water in the water-containing raw material (4) is 20%; the water-containing The total mass percentage of oxygen-containing compounds in the raw material (4) is 80%, wherein the oxygen-containing compounds are acetone, methyl ethyl ketone, pentanone, methyl isoamyl ketone, methanol, ethanol, acetaldehyde, propionaldehyde; oxygen-containing compounds The mass percent content of ketone compounds in the middle is 30%; the mass percent content of aldehyde compounds in the oxygen-containing compounds is 20%.
[0058] The system comprises a first reactor (1), a second reactor (2) and a gas-liquid separator (3).
[0059] The water-containing raw material (4) is preheated to 120-200°C and then enters the first reactor (1) to contact with the first ca...
Embodiment 2
[0067] The water-containing raw material (4) enters the system of the present invention and contacts with the catalyst to generate a reaction product (7) rich in carbon number less than or equal to 6 olefins, wherein the mass percentage of water in the water-containing raw material (4) is 90%; The total mass percentage of oxygen-containing compounds in the raw material (4) is 10%, wherein the oxygen-containing compounds are acetone, butanone, pentanone, methyl isoamyl ketone; the mass percentage of ketones in the oxygen-containing compounds is 100%; Oxygenate free of aldehydes.
[0068] The system of the present invention comprises a first reactor (1), a second reactor (2) and a gas-liquid separator (3).
[0069] The water-containing raw material (4) is preheated to 120-200°C and then enters the first reactor (1) to contact with the first catalyst to obtain the first reaction product (5); the stream I (8) is preheated to 150-350°C and then enters The second reactor (2) and th...
Embodiment 3
[0077] The water-containing raw material (4) enters the system of the present invention and contacts with the catalyst to generate a reaction product (7) rich in carbon number less than or equal to 6 olefins, wherein the mass percentage of water in the water-containing raw material (4) is 70%; The total mass percentage of oxygen-containing compounds in the raw material (4) is 30%, wherein the oxygen-containing compounds are one of acetone, butanone, pentanone, methyl isoamyl ketone, methanol, ethanol, acetaldehyde, and propionaldehyde or more; the mass percent content of ketone compounds in the oxygen-containing compound is 95%; the mass percent content of the aldehyde compound in the oxygen-containing compound is 5%.
[0078] The system of the present invention comprises a first reactor (1), a second reactor (2) and a gas-liquid separator (3).
[0079] The water-containing raw material (4) is preheated to 120-200°C and then enters the first reactor (1) to contact with the fir...
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