会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明公开
    • PURIFICATION DEVICE
    • EP4249095A1
    • 2023-09-27
    • EP21894686.1
    • 2021-11-17
    • Nippon Shokubai Co., Ltd.
    • ARAI, ShogoMUKAE, MasashiWADA, HirokiFUKUMOTO, ToshiyaMATSUDA, TakayukiSAKAI, Toyofumi
    • B01D9/02C07C51/43C07C57/07C07B61/00
    • The present invention aims to provide a compound purification apparatus capable of providing a high purity compound in high yield and at low cost. The present invention relates to an apparatus for purifying a compound, the purification apparatus including: a crystallizing unit including a crystal forming section; and a wash column including a mechanism that forcibly transfers crystals, the crystallizing unit including N tanks connected in series, wherein N is 2 or greater, a 1st tank is a most downstream tank, a (N)th tank is a most upstream tank, at least the 1st tank is a crystallization tank including a cooling mechanism, and a 2nd and subsequent tanks are each a crystallization tank or a ripening tank, the purification apparatus including a line that feeds a compound-containing liquid to be purified to at least one of the N tanks, the wash column including: a line that sends a product out; and a line that returns a mother liquor to the crystallizing unit, with the line that returns a mother liquor to the crystallizing unit being connected to at least the (N)th tank, the crystallizing unit including: a line that feeds a slurry from the (N)th tank to the wash column; a line that sends a slurry from a tank among the 1st to (N - 1)th tanks to the next upstream tank; and a line that is provided to each of the 1st to (N - 1)th tanks and that sends thereto a mother liquor withdrawn from an upstream tank, wherein at least one of the lines that send a slurry from a tank among the 1st to (N - 1)th tanks to the next upstream tank is a line that sends a slurry from a tank to the next upstream tank via a solid-liquid separator and that has a line that returns a mother liquor from which crystals are removed in the solid-liquid separator to the tank where the slurry came from, and wherein the line that is provided to each of the 1st to (N - 1)th tanks and that sends thereto a mother liquor withdrawn from an upstream tank is a line that directly sends a mother liquor withdrawn from a tank one upstream or a line that sends a mother liquor withdrawn from a tank one upstream via a solid-liquid separator, the purification apparatus further including a line that sends a mother liquor to the outside of the purification apparatus.
    • 6. 发明公开
    • METHOD FOR PURIFYING COMPOUND
    • EP4249096A1
    • 2023-09-27
    • EP21894687.9
    • 2021-11-17
    • Nippon Shokubai Co., Ltd.
    • ARAI, ShogoMUKAE, MasashiWADA, HirokiFUKUMOTO, ToshiyaMATSUDA, TakayukiSAKAI, Toyofumi
    • B01D9/02C07C51/43C07C57/07C07B61/00
    • Provided is a method for purifying a compound capable of providing a high purity compound in high yield and at low cost. The present invention relates to the method for purifying a compound using a purification apparatus, the purification apparatus including: a crystallizing unit including a crystal forming section; and a wash column including a mechanism that forcibly transfers crystals. The crystallizing unit includes N tanks connected in series, wherein N is 2 or greater, a 1st tank is a most downstream tank, a (N)th tank is a most upstream tank, at least the 1st tank is a crystallization tank including a cooling mechanism, and a 2nd and subsequent tanks are each a crystallization tank or a ripening tank. The purification apparatus includes a line that feeds a compound-containing liquid to be purified to at least one of the N tanks. The wash column includes a line that sends a product out; and a line that returns a mother liquor to the crystallizing unit, with the line that returns a mother liquor to the crystallizing unit being connected to at least the (N)th tank. The crystallizing unit includes a line that feeds a slurry from the (N)th tank to the wash column; a line that sends a slurry from a tank among the 1st to (N - 1)th tanks to the next upstream tank; and a line that is provided to each of the 1st to (N - 1)th tanks and that sends thereto a mother liquor withdrawn from an upstream tank, wherein at least one of the lines that send a slurry from a tank among the 1st to (N - 1)th tanks to the next upstream tank is a line that sends a slurry from a tank to the next upstream tank via a solid-liquid separator and that has a line that returns a mother liquor from which crystals are removed in the solid-liquid separator to the tank where the slurry came from, and wherein the line that is provided to each of the 1st to (N - 1)th tanks and that sends thereto a mother liquor withdrawn from an upstream tank is a line that directly sends a mother liquor withdrawn from a tank one upstream or a line that sends a mother liquor withdrawn from a tank one upstream via a solid-liquid separator. The purification method includes forming crystals of the compound in the crystallizing unit; discharging at least a portion of a mother liquor to the outside of the purification apparatus; separating a slurry containing the formed crystals into a mother liquor and a slurry having an increased crystal concentration; returning at least a portion of the separated mother liquor to the tank where the slurry came from; mixing a compound-containing liquid to be purified fed to the crystallizing unit with a slurry in the crystallizing unit; sending a slurry in order from any one of the 1st to (N - 1)th tanks to the next upstream tank among the N tanks in the crystallizing unit; and feeding at least a portion of a slurry from the crystallizing unit to the wash column; wherein the compound-containing liquid to be purified has a higher purity than the mother liquor discharged to the outside of the purification apparatus, the slurry fed to the wash column contains a mother liquor having a purity A1 of 80 mol% or higher, and a difference between the purity A1 and a purity A2 of the mother liquor discharged, A1 - A2, is 5 mol% or more.