2134-29-4Relevant articles and documents
Synthesis method of 3-hydroxypropionaldehyde
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Paragraph 0075; 0076; 0077, (2020/05/14)
The invention relates to a synthesis method of 3-hydroxypropionaldehyde, which mainly solves the problem of difficulty in separation of a catalyst of a homogeneous system in the prior art. The synthesis method of 3-hydroxypropionaldehyde comprises the following steps: i, adding a cobalt catalyst and a cocatalyst into a solvent, and heating for pretreatment in a synthesis gas atmosphere; and ii, after the catalyst pretreatment is finished, cooling, releasing the pressure, adding ethylene oxide and synthesis gas, and reacting to obtain the 3-hydroxypropionaldehyde, so that the technical problemis better solved, and the method can be applied to industrial production of the 3-hydroxypropionaldehyde.
Method for preparing 3-hydroxypropionaldehyde by hydrating acrolein
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Paragraph 0050-0059, (2020/12/31)
The invention relates to a method for preparing 3-hydroxy propionaldehyde by hydrating acrolein. The acrolein is homogeneously catalyzed under the action of a N-heterocyclic carboxylic acid ionic liquid to prepare 3-hydroxy propionaldehyde, wherein the hydration reaction liquid is subjected to aqueous two-phase extraction to recover the ionic liquid catalyst for cyclic utilization. According to the invention, the method is simple to operate and stable in process, the catalyst has very high reaction activity and very good selectivity, and the problems of separation of a homogeneous catalyst andinstability and easy deactivation of a solid catalyst in the hydration process are effectively solved.
Catalytic glycerol hydrogenolysis to 1,3-propanediol in a gas-solid fluidized bed
Edake, Mahesh,Dalil, Marjan,Darabi Mahboub, Mohammad Jaber,Dubois, Jean-Luc,Patience, Gregory S.
, p. 3853 - 3860 (2017/02/05)
Glycerol is a potential feedstock to produce 1,3-propanediol (1,3-PDO), which is a valuable commercial polyester monomer. Here, we report the gas-phase glycerol hydrogenolysis to 1,3-propanediol over Pt/WO3/Al2O3 in a fluidized bed operating above 240 °C and at ambient pressure. Fluidized beds are ideal contactors for this reaction because the heat transfer rates are sufficiently high to vaporize glycerol thereby minimizing its combustion and thermal degradation. The yield of 1,3-PDO approached 14% after 2 h at 260 °C. The major co-products were 1,2-PDO (18%), 1-propanol (28%) and 2-propanol (15%). In the first step, glycerol may dehydrate to acrolein, followed by rehydration to 3-hydroxypropanal and then hydrogenation to 1,3-PDO. The concentrations of the by-products including acrolein, ethylene glycol, propane, and acetone increased with increasing temperature.