Method for preparing decane dialdehyde intermediate
A technology of deca-carbon dialdehyde and intermediates, which is applied in the field of intermediates for the preparation of deca-carbon dialdehydes, and can solve problems such as low yield, environmental pollution, and equipment corrosion
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Embodiment 1
[0054] Preparation method of the present embodiment provides a decadialdehyde intermediate, such as process diagram figure 1 As shown, specifically includes the following steps:
[0055] (1) 130.1g 2,5- dimethoxy-2,5-dihydrofuran with 106.1g trimethyl orthoformate to give the mixed solution A, 1.3g of the catalyst I (activated carbon catalyst is ferric chloride) and 160.2 g of methanol were mixed to give solution B. The propenyl ether 133.9g, 267.7g toluene solution was mixed with solution D; 0.26g catalyst II (SO 4 2- -Tio 2 -Fe 3 O 4 Solid superacid catalyst) adsorbed and fixed in a microchannel.
[0056] (2) Step (1) Solution A and Solution B were obtained via a metering pump and a metering pump 2 to feed flow ratio of 1.2: entering a continuous flow microreactor (channel hydraulic diameter 0.3mm) 1, wherein the metering the flow rate of the pump 1 is 2.4ml / min, the flow rate of the metering pump 2 was 2ml / min, acetalization reaction is carried out at 50 ℃, the residence t...
Embodiment 2
[0067] (1) 104.1g 2,5- dimethoxy-2,5-dihydrofuran and 93.4g trimethyl orthoformate to give a mixed solution of A, and 3.1g of the catalyst I (ferric bromide activated carbon catalyst) and 76.9 g of methanol were mixed to give solution B. The propenyl ether 135.1g, 731.2g toluene solution was mixed with solution D; 0.41g catalyst II (SO 4 2- -Tio 2 -Al 2 O 3 Solid superacid catalyst) adsorbed and fixed in a microchannel.
[0068] (2) Step (1) Solution A and Solution B were obtained via a metering pump 2 and the metering pump 1 at a feed flow rate ratio of 2: 1 to enter a continuous flow microreactor (channel hydraulic diameter 0.5mm), wherein the metering the flow rate of the pump 1 is 2.4ml / min, the flow rate of the metering pump 2 is 1.2ml / min, acetalization reaction is carried out at 40 ℃, the residence time of the material in a continuous-flow micro-reactor is 85s, the resulting reaction solution stored in the storage tank 10 (e.g. figure 2 ) As shown, referred to as solut...
Embodiment 3
[0072] (1) 130.1g 2,5- dimethoxy-2,5-dihydrofuran and 95.5g trimethyl orthoformate to give a mixed solution of A, and 1.95g of the catalyst I (activated carbon catalyst is ferric chloride) and 160.2 g of methanol were mixed to give solution B. The propenyl ether 180.3g, 360.6g toluene solution was mixed with solution D; 0.18g catalyst II (SO 4 2- -Tio 2 -Fe 3 O 4 Solid superacid catalyst) adsorbed and fixed in a microchannel.
[0073] (2) Step (1) Solution A and Solution B were obtained via a metering pump and a metering pump 2 to feed flow ratio of 1.1: 1 to enter a continuous flow microreactor (channel hydraulic diameter 1mm), wherein the metering pump 1 is a flow rate 2.2ml / min, the flow rate of the metering pump 2 was 2ml / min, acetalization reaction is carried out at 10 ℃, the residence time of the material in a continuous-flow micro-reactor is 72s, the resulting reaction solution was stored at storage tank 10 (e.g. figure 2 ) As shown, referred to as solution C; sample f...
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