Catalyst system used in low pressure methanol carbonyl synthesizing acetic acid
A catalytic system, oxo synthesis technology, applied in the direction of organic compound/hydride/coordination complex catalyst, physical/chemical process catalyst, carbon monoxide reaction to prepare carboxylic acid, etc., can solve pollution, concentration increase, containing methyl acetate and Increase in methyl iodide and other issues, to achieve the effect of high quality, less by-products, high activity and selectivity
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Embodiment 1
[0036] In the catalyst system, the reaction solution consists of: 70.5wt% acetic acid, 1wt% methyl acetate, 12wt% methyl iodide, 14wt% water, Fe0.0025wt%, Ni0.0024wt%, Cr0.0050wt%, Mo0.0100wt%, I - 2.5wt%, Rh0.04wt%.
[0037] Carry out experiments according to the embodiment, and keep the temperature in the decanter 8 at about 40° C., and keep the temperature in the decanter 9 less than 45° C. Keep the flow rate of logistics 41 at 100kg / h, and keep the flow rate of logistics 42 at 100kg / h. The catalyst composition, the composition of stream 12, the density of stream 15, the concentration of stream 21, the composition of stream 25, and the composition of stream 30 were tested. And obtain product 25 127kg, waste acid 30 0.2kg. What table 1 records is the material flow and process condition of embodiment 1.
[0038] Embodiment 1 is as a kind of contrast of the present invention, and decanter 9 is not used as decanter.
[0039] name
Embodiment 2
[0041] The reaction solution in the catalyst system consists of: 59.8wt% acetic acid, 1.94wt% methyl acetate, 10.37wt% methyl iodide, 7.17wt% water, K + 0.5000wt%, Li + 0.3700wt%, Fe 0.1357wt%, Ni 0.0798wt%, Cr 0.0916wt%, I - 10.83wt%, Rh 0.0650wt%.
[0042] Carry out experiments according to the embodiment, and keep the temperature in the decanter 8 at about 36° C., and keep the temperature in the decanter 9 less than 45° C. Keep the flow rate of logistics 41 at 100kg / h, and keep the flow rate of logistics 42 at 75kg / h. The catalyst composition, the composition of stream 12, the density of stream 15, the concentration of stream 21, the composition of stream 25, and the composition of stream 30 were tested. And obtain product 25 179.5kg, spent acid 30 0.23kg. What table 2 records is the material flow and process condition of embodiment 2.
[0043] name
Embodiment 3
[0045] The reaction solution in the catalyst system consists of: 64.9wt% acetic acid, 3.0wt% methyl acetate, 14.0wt% methyl iodide, 8.4wt% water, 0.0341wt% propionic acid, K + 0.4000wt%, Li + 0.3600wt%, Fe 0.1551wt%, Ni 0.1027wt%, Cr 0.1085wt%, Mo 0.0708wt%, I - 9.5wt%, Rh 0.0740wt%.
[0046] Carry out experiments according to the embodiment, and keep the temperature in the decanter 8 at about 32° C., and keep the temperature in the decanter 9 less than 45° C. Keep the flow rate of logistics 41 at 90kg / h, and keep the flow rate of logistics 42 at 50kg / h. The catalyst composition, the composition of stream 12, the density of stream 15, the concentration of stream 21, the composition of stream 25, and the composition of stream 30 were tested. And obtain product 25225.8kg, waste acid 300.25kg. What table 3 records is the material flow and process condition of embodiment 3.
[0047] name
PUM
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