Method for carbonyl synthesis by using carbon-rich natural gas
A technology for oxo synthesis and natural gas, applied in the preparation of carbon-based compounds, carbon compound catalysts, hydrogen/synthesis gas production, etc., can solve the problems of increased energy consumption, natural gas loss, environmental greenhouse gas impact, etc. The effect of exhaust emission and loss avoidance
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Embodiment 1
[0056] This embodiment provides a method for carbonylation using carbon-rich natural gas, the schematic flow chart of which is as follows figure 1 As shown, the steps include the following steps:
[0057] (1) The 1000kmol / h carbon-rich natural gas purified in the natural gas purification unit is preheated in the heat exchange unit, and then reformed in the reformer to obtain synthesis gas (hydrogen-to-carbon ratio=0.95). The pressure of the reforming reaction is 1.5Mpag, and the temperature of the reforming reaction is 900°C;
[0058] Wherein, the pressure of the purified carbon-rich natural gas is 2.0Mpag, the temperature is 40°C, and the CO 2 Molar content 50%;
[0059] (2) After the synthesis gas is purified, carry out a hydroformylation reaction with 1100 kmol / h 1-butene under the catalysis of rhodium dicarbonyl acetylacetonate, the temperature of the carbonylation reaction is 70 ° C, the pressure is 1.0 Mpag, and the product is separated and purified After obtaining 89...
Embodiment 2
[0062] This embodiment provides a method for carbonylation using carbon-rich natural gas, the schematic flow chart of which is as follows figure 2 As shown, the steps include the following steps:
[0063] (1) The 1000 kmol / h carbon-rich natural gas purified in the natural gas purification unit is preheated in the heat exchange unit, and then reformed in the reformer to obtain synthesis gas (hydrogen-to-carbon ratio=1.03). The pressure of the reforming reaction is 2.0Mpag, and the temperature of the reforming reaction is 1100°C;
[0064] Wherein, the pressure of the purified carbon-rich natural gas is 2.5Mpag, the temperature is 40°C, and the CO 2 Molar content 40%;
[0065] (2) After the synthesis gas is purified, carry out a hydroformylation reaction with 1050 kmol / h 1-butene under the catalysis of rhodium dicarbonyl acetylacetonate, the temperature of the carbonylation reaction is 75 ° C, the pressure is 1.1 Mpag, and the product is separated and purified After obtaining...
Embodiment 3
[0068] The present embodiment provides a method for utilizing carbon-rich natural gas to carry out oxo synthesis, which comprises the following steps:
[0069] (1) The 1000kmol / h carbon-rich natural gas purified in the natural gas purification unit is preheated in the heat exchange unit, and then reformed in the reformer to obtain synthesis gas (hydrogen-to-carbon ratio=1.06). The pressure of the reforming reaction is 2.5Mpag, and the temperature of the reforming reaction is 1300°C;
[0070] Wherein, the pressure of the purified carbon-rich natural gas is 3.0Mpag, the temperature is 40°C, and the CO 2 Molar content 25%;
[0071] (2) After the synthesis gas is purified, carry out a hydroformylation reaction with 1000 kmol / h 1-butene under the catalysis of rhodium dicarbonyl acetylacetonate, the temperature of the carbonylation reaction is 80 ° C, the pressure is 1.2 Mpag, and the product is separated and purified After obtaining 760kmol / h C5 aldehyde, the olefin conversion ra...
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