Multi-layered micro-channel mixer and method for mixing fluids

    公开(公告)号:US12194428B2

    公开(公告)日:2025-01-14

    申请号:US17467377

    申请日:2021-09-06

    Abstract: A multi-layered micro-channel mixer includes a base plate and a cover plate. Two inlet fluid reservoirs, two inlet channels, two groups of fluid distribution channel networks, two groups of process fluid channels, an impinging stream mixing chamber, a fluid mixing intensification channel and an outlet buffer reservoir are provided on the base plate. Two fluids are fed into the two inlet fluid reservoirs, respectively. The fluids then flow into the process fluid channels via the inlet channels and the multi-stage fluid distribution channel networks, respectively. Then the two fluid streams ejected from the opposing process fluid channels impinges upon each other in the impinging stream mixing chamber. The mixed fluid is subjected to vortex or secondary flow generated by the baffles or the internals in the impinging stream mixing chamber and fluid mixing intensification channel, and finally the mixed fluid is discharged through the outlet buffer reservoir.

    Full continuous-flow preparation method of vitamin B1

    公开(公告)号:US11834425B2

    公开(公告)日:2023-12-05

    申请号:US18166478

    申请日:2023-02-09

    CPC classification number: C07D279/06

    Abstract: A full continuous-flow preparation method of vitamin B1 includes: (S1) feeding 3-chloro-4-oxopentyl acetate, 2-methyl-4-amino-5-(aminomethyl) pyrimidine and carbon disulfide to a first continuous-flow reactor for addition; (S2) allowing the reaction mixture to flow into a first continuous filtration and reaction device to collect a filter cake; subjecting the filter cake and hydrochloric acid solution to cyclization; transporting the reaction mixture and an aqueous inorganic base solution to a micromixer and a second continuous-flow reactor for hydrolysis to obtain thiothiamine; (S3) transporting the thiothiamine to a third continuous-flow reactor with hydrogen peroxide for oxidation to obtain thiamine sulfate; and (S4) allowing the thiamine sulfate to enter a second continuous filtration and reaction device for filtration to collect a filter cake; and subjecting the filter cake to reaction with organic hydrochloric acid solution followed by filtration and drying to obtain vitamin B1.

    Method for preparing a key intermediate for the synthesis of statins

    公开(公告)号:US11708363B2

    公开(公告)日:2023-07-25

    申请号:US17488276

    申请日:2021-09-28

    CPC classification number: C07D417/12

    Abstract: Disclosed herein relates to organic synthesis, and more particularly to a method for preparing a key intermediate for the synthesis of statins. The key intermediate is 2-[(4R,6S)-6-[(benzo[d]thiazol-2-ylthio)methyl]-2,2-disubstituted-1,3-dioxan-4-yl] acetate of formula (I):




    where R1 is a C1-C8 alkyl group, a C3-C8 cycloalkyl group, a monosubstituted or polysubstituted aryl group, or monosubstituted or polysubstituted aralkyl group; R2 is hydrogen, or monosubstituted or polysubstituted C1-C3 alkyl group, or halogen; and R3 and R4 are each independently a C1-C5 alkyl group, a C3-C7 cycloalkyl group, a C3-C7 cycloalkenyl group, a C1-C3 alkoxy group, a C6-C10 aryl group, or C7-C12 aralkyl group. In the method, a halomethyl compound and a thiol reagent are subjected to nucleophilic substitution in an organic solvent to synthesize a thioether, which then undergoes ketal exchange reaction with a carbonyl compound (V) in the presence of an organic acid to obtain a target product.

    Method for preparing 3-chloro-4-oxopentyl acetate using fully continuous-flow micro-reaction system

    公开(公告)号:US11618727B2

    公开(公告)日:2023-04-04

    申请号:US17384747

    申请日:2021-07-24

    Abstract: This disclosure relates to organic synthesis, and more particularly to a method for preparing 3-chloro-4-oxopentyl acetate using a fully continuous-flow micro-reaction system. In this method, chlorine and an acetylbutyrolactone-containing liquid are simultaneously transported to a first micro-channel reactor for continuous chlorination to obtain α-acetyl-α-chloro-γ-butyrolactone. The reaction mixture is simultaneously transported to a micro-mixer and a second micro-channel reactor together with a mixed solution of glacial acetic acid, hydrochloric acid and water, and the continuous acylation is carried out to obtain 3-chloro-4-oxopentyl acetate. After quenched with a quenching agent, the reaction mixture was subjected to extraction and separation to obtain the 3-chloro-4-oxopentyl acetate.

    Preparation method for (R)-3-hydroxyl-5-hexenoate

    公开(公告)号:US10526622B2

    公开(公告)日:2020-01-07

    申请号:US15871039

    申请日:2018-01-14

    Abstract: The present disclosure relates to the technical field of biochemical engineering and particularly discloses a preparation method for (R)-3-hydroxyl-5-hexenoate. In the method of the present disclosure, the (R)-3-hydroxyl-5-hexenoate is prepared by catalytic reduction of 3-carbonyl-5-hexenoate by ketoreductase with 3-carbonyl-5-hexenoate as the substrate. The amino acid sequence of ketoreductase is shown in SEQ ID NO.1. In the present disclosure, the (R)-3-hydroxyl-5-hexenoate having a very high chiral purity is obtained by asymmetric reduction by ketoreductase as the biocatalyst. The present disclosure has the advantages of easy operation, mild reaction conditions, high reaction yield and good practical industrial application value.

    Method for the continuous flow synthesis of (R)-4-halo-3-hydroxy-butyrate

    公开(公告)号:US12281348B2

    公开(公告)日:2025-04-22

    申请号:US17516894

    申请日:2021-11-02

    Abstract: This application relates to organic synthesis, and more particularly to a method for the continuous flow synthesis of (R)-4-halo-3-hydroxy-butyrate using a micro-reaction system. This application performs an enzymatic asymmetric reduction of a substrate solution containing halogenated acetoacetate and a biocatalyst solution in the micro-reaction system composed of a micro-mixer, a micro-channel reactor, and a pH regulator to obtain the (R)-4-halo-3-hydroxy-butyrate. Compared to the prior art, the reaction time of the method is only a few minutes, the yield of the product (R)-4-halo-3-hydroxy-butyrate is greater than 95%, the reaction process is continuous, the degree of automation is high, the efficiency is high, and the process is simple to operate and easy to be used in industrialized production.

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