Method for making a chlorohydrin starting with a polyhydroxylated aliphatic hydrocarbon
A technology of polyhydroxy aliphatic hydrocarbons and chlorohydrins, which is applied in the preparation of hydroxyl compounds, chemical instruments and methods, and the preparation of organic compounds, and can solve problems such as hindering economic benefits
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[0093] In the production process according to the present invention, the organic acid may be a product produced by the process for producing polyhydroxy aliphatic hydrocarbons, or a product not produced by the process. In the latter case, the products in question may be organic acids used to catalyze the reaction of polyhydroxyaliphatic hydrocarbons with chlorinating agents, and / or acids produced in processes for the preparation of chlorohydrins. For example, acid formation starting from aldehydes present in polyhydric aliphatic hydrocarbons or during the preparation of chlorohydrins needs to be considered. The organic acid may also be a mixture of organic acids derived from the polyhydroxy aliphatic hydrocarbon production process and organic acids not derived from the polyhydroxy aliphatic hydrocarbon production process.
[0094] In the process according to the invention, the esters of polyhydroxyaliphatic hydrocarbons may result from the reaction between polyhydroxyaliphatic...
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[0130] Figure 1 shows a diagram of a specific apparatus that can be used to carry out the separation process according to the invention.
[0131] Polyhydroxy aliphatic hydrocarbons, esters of polyhydroxy aliphatic hydrocarbons or mixtures thereof are supplied to reactor (4) via line (1) and catalyst via line (2) in continuous or batch mode; chlorinating agent is supplied via (3) in continuous mode mode or batch mode supply; the vapor generated in the reactor (4) is supplied to the distillation column (6) via the line (5); the stream separated from the distillation column (6) via the line (7) is introduced into the condenser (8 ); the stream obtained from this condenser is introduced via line (9) into a phase separator (10) in which the aqueous and organic phases are separated. A part of the separated aqueous phase is optionally recycled to the top of the distillation column via line (11 ) to maintain reflux. Fresh water can be introduced into line (11) via line (12). The chl...
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