Water-soluble derivatives of 3,5-diphenyl-diazole compounds

    公开(公告)号:US10308671B2

    公开(公告)日:2019-06-04

    申请号:US16062258

    申请日:2016-12-14

    IPC分类号: C07F9/11 A61P25/28 A61P25/16

    摘要: The present invention is concerned with derivatives of 3,5-diphenyl-diazole compounds, which are effective therapeutic agents for use in treating diseases linked to protein aggregation and/or neurodegenerative diseases such as Alzheimer's disease (AD), Parkinson's disease (PD), and Transmissible spongiform encephalopathies (TSEs) such as Creutzfeldt-Jakob disease (CJD). The therapeutic effect is caused by the inhibition of the protein aggregation in the affected tissue, such as the brain. 3,5-Diphenyl-diazole derivatives have been shown to be effective in inhibiting aggregation of proteins but are also characterized by their poor solubility in aqueous solutions. The prodrugs of the invention are modified 3,5-diphenyl-diazole derivatives, which are characterized by their improved solubility in aqueous solutions, and by their increased bioavailability.

    Method for producing lithium carbonate from low-lithium brine by separating magnesium and enriching lithium

    公开(公告)号:US10246341B2

    公开(公告)日:2019-04-02

    申请号:US15789997

    申请日:2017-10-21

    摘要: The present invention discloses a method for producing lithium carbonate from a low-lithium brine by separating magnesium and enriching lithium. A salt-lake brine is used as a raw material and is converted into halide salts through dehydration by evaporation and separation by crystallization; the halide salts are directly extracted using trialkyl phosphate or a mixture of trialkyl phosphate and monohydric alcohol, and an organic extraction phase as well as remaining halide salts are obtained after solid-liquid separation; reverse extraction is performed on the organic extraction phase to obtain a lithium-rich solution with a low magnesium-to-lithium ratio, and lithium carbonate is obtained after concentration and removal of magnesium by alkalization. The used solid-liquid extraction method is simple with no co-extraction agent used, and a solute distribution driving force is strong, unaffected by phase equilibrium of the brine extraction agent. The mass ratio of magnesium-to-lithium significantly decreases in the extraction phase.