l‑threonine synthesis process
A synthesis process and threonine technology, applied in the field of L-threonine synthesis technology, can solve the problems of difficulty in realizing industrialized production, low yield, etc., and achieve the effects of improving utilization rate, reducing raw material cost, and simple and convenient process operation.
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Embodiment 1
[0016] L-threonine synthesis process, with CH 2 CHCH(OH)CH 3 (3-buten-2-ol) as raw material, Cu 2 (OH) 2 CO 3 and CuCl 2 As a catalyst, after the double bond is epoxidized, under the action of the catalyst, it reacts with phCONCO to generate a five-membered heterocyclic compound. After diluting the solution, filter and remove Cu 2 (OH) 2 CO 3 and CuCl 2 Catalyst, acidification and ring opening to generate DL-threonine, and then split to obtain L-threonine.
[0017] Preferably, the mass ratio of the raw material to the catalyst is 100:0.2.
[0018] Among them, preferably, the Cu 2 (OH) 2 CO 3 with CuC1 2 The mass ratio is 1:1.
[0019] Among them, preferably, the Cu 2 (OH) 2 CO 3 The purity is 99.9%.
[0020] Among them, preferably, the CuCl 2 The purity is 99.9%.
[0021] The productive rate of L-threonine in this embodiment is shown in Table 1.
Embodiment 2
[0023] The specific steps are as in Example 1, wherein preferably, the mass ratio of the raw material to the catalyst is 100:0.1. The Cu 2 (OH) 2 CO 3 with CuCl 2 The mass ratio is 1:1.2. The Cu 2 (OH) 2 CO 3 The purity is 99.5%, the CuCl 2 The purity is 99.5%. The productive rate of L-threonine in this embodiment is shown in Table 1.
Embodiment 3
[0025] The specific steps are as in Example 1, wherein preferably, the mass ratio of the raw material to the catalyst is 100:0.05. The Cu 2 (OH) 2 CO 3 with CuCl 2 The mass ratio is 1:0.8. The Cu 2 (OH) 2 CO 3 The purity is 99.9%, the CuCl 2 The purity is 99.9%. The productive rate of L-threonine in this embodiment is shown in Table 1.
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