SEPARATION AND PURIFICATION METHOD OF 2-NITROETHANOL

    公开(公告)号:US20240018088A1

    公开(公告)日:2024-01-18

    申请号:US18361533

    申请日:2023-07-28

    CPC classification number: C07C201/16

    Abstract: A separation and purification method of 2-nitroethanol, including: (a) reacting paraformaldehyde with nitromethane in the presence of a base to obtain a mixture of 2-nitroethanol (I), 2-nitro-1,3-propanediol (II) and tris(hydroxymethyl) nitromethane (III); and (b) selecting an extraction solvent in which 2-nitroethanol (I), 2-nitro-1,3-propanediol (II) and tris(hydroxymethyl) nitromethane (III) are different in solubility; adding the extraction solvent to the mixture followed by extraction, separation, and vacuum concentration to obtain the 2-nitroethanol (I).

    METHOD FOR PREPARING 3-CHLORO-4-OXOPENTYL ACETATE USING FULLY CONTINUOUS-FLOW MICRO-REACTION SYSTEM

    公开(公告)号:US20210355070A1

    公开(公告)日:2021-11-18

    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.

    CONTINUOUS-FLOW PREPARATION METHOD OF DIOL SULFONE

    公开(公告)号:US20230127147A1

    公开(公告)日:2023-04-27

    申请号:US18068151

    申请日:2022-12-19

    Abstract: A continuous-flow preparation method of diol sulfone using a two-stage micro-reaction system. The system includes a first micro-mixer, a first micro-channel reactor, a second micro-mixer, and a second micro-channel reactor communicated in sequence. The method includes: feeding hydrogen peroxide, a catalyst and a diol thioether solution simultaneously to the first micro-mixer followed by mixing; feeding the reaction mixture to the first micro-channel reactor for continuous oxidation; and feeding the reaction mixture and water simultaneously to the second micro-mixer and the second micro-channel reactor for continuous quenching and crystallization to obtain diol sulfone.

    METHOD FOR PREPARING (DIMETHYLAMINOMETHYLENE) MALONONITRILE USING A MICRO REACTION SYSTEM

    公开(公告)号:US20220089524A1

    公开(公告)日:2022-03-24

    申请号:US17103520

    申请日:2020-11-24

    Abstract: A method for preparing (dimethylaminomethylene) malononitrile by using a micro reaction system. Cyanoacetamide, N,N-dimethylformamide and a catalyst are mixed to obtain a mixture, and the mixture and phosphorus oxychloride are simultaneously pumped into the micro reaction system that includes a micromixer and a microchannel reactor connected in series for continuous dehydration condensation. After adjusted to a target pH, the crude product is subjected to continuous liquid-liquid extraction with an organic solvent in a centrifugal extraction unit comprising a plurality of annular centrifugal extractors connected in series. The organic phase is collected to obtain the target product (dimethyl aminomethylene) malononitrile.

    MULTI-LAYERED MICRO-CHANNEL MIXER AND METHOD FOR MIXING FLUIDS

    公开(公告)号:US20210394141A1

    公开(公告)日:2021-12-23

    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.

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