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Pure water and concentrates are recovered from dilute fermentation substrates or wash waters, e.g. in winemaking cellars, beverage and glucose production and breweries

机译:从稀发酵底物或洗涤水(例如纯净水)中回收纯净水和浓缩物。在葡萄酒窖,饮料和葡萄糖生产以及啤酒厂中

摘要

Pure water and concentrates are recovered by extraction and concentration of dilute substrates or wash waters stabilized with a recycled volatile bactericidal additive. Pure water and concentrates are obtained from dilute substrates or wash waters mainly containing sugars and volatile compounds from fermentation, by: (a) storage of the dilute substrates or wash waters stabilized by addition of a volatile bactericidal product; (b) column extraction of the volatile compounds to produce a concentrated bactericide solution for recycling and for production of concentrated organic distillates; (c) evaporative concentration of the treated substrates with elimination of volatile organic acids from the vapor by scrubbing in a column supplied with an alkaline solution; (d) combination of the concentrates; and (e) storage and stabilization of the purified water for further use. An Independent claim is also included for an installation for carrying out the above process, comprising: (i) a stirred storage tank (SSD) for the dilute substrate (SD) mixed with absorption liquor (BV) and a volatile bactericide (aBV); (ii) a heat exchanger (R) for preheating the dilute substrate; (iii) extraction and concentration columns (CS, CC) fitted with condensers (C1, C2); (iv) a non-condensed product transfer system and a volatile bactericide absorption column (CA) for producing the absorption liquor (BV); (v) an energy efficient evaporator (EV) which concentrates the substrate transferred from the extraction column (CS) and which consists of an exchange surface, a cyclone separator, a column for vapor scrubbing with alkaline solution (CLA), a thermocompressor (TC) fed with pressurized steam and a mechanical steam compressor (C); (vi) a stirred storage tank for the treated water (ET) which can be supplied with volatile bactericide after stabilization; (vii) a stirred storage tank for the concentrated and reconstituted wort (SMR); and (viii) a stirred storage tank for the concentrated distillates (SDC). Preferred Features: The volatile bactericide is a solution of SO2 or formaldehyde, recycled with greater than 98% efficiency. The purified water (ET) comprises the condensed vapors from the evaporator (EV) and is reused for washing operations. The extraction column (CS) is heated solely by steam (VbP) from the evaporator (EV), the steam optionally being compressed by mechanical compression. The evaporator (EV) is a cascade type evaporator in which liquid is recirculated and distributed by a conical spray nozzle and which has an exterior/interior tube temperature difference of 3-8 deg C. The scrubber column has an upper stage fed with condensate and a lower stage fed with recirculated alkaline solution.
机译:通过萃取和浓缩稀释的底物或用回收的挥发性杀菌添加剂稳定的洗涤水,可以回收纯水和浓缩物。通过以下方法,从稀释的底物或主要来自发酵的糖和挥发性化合物的洗涤水中获得纯水和浓缩物:(a)储存通过添加挥发性杀菌产品而稳定化的稀释底物或洗涤水; (b)柱提取挥发性化合物,以产生浓缩的杀菌剂溶液,以循环利用和生产浓缩的有机馏出液; (c)通过在装有碱性溶液的塔中洗涤,蒸发浓缩处理过的底物,从蒸气中除去挥发性有机酸; (d)浓缩物的组合; (e)储存和稳定纯净水以备将来使用。还包括用于执行上述过程的设备的独立权利要求,其包括:(i)搅拌的储罐(SSD),用于与吸收液(BV)和挥发性杀菌剂(aBV)混合的稀释基质(SD); (ii)用于预热稀释基板的热交换器(R); (iii)装有冷凝器(C1,C2)的萃取和浓缩塔(CS,CC); (iv)非冷凝产品转移系统和用于生产吸收液(BV)的挥发性杀菌剂吸收塔(CA); (v)高效节能的蒸发器(EV),用于浓缩从萃取塔(CS)输送来的底物,该蒸发器由交换表面,旋风分离器,用于碱溶液蒸气洗涤的塔(CLA),热压缩机(TC)组成)供给加压蒸汽和机械蒸汽压缩机(C); (vi)用于处理水(ET)的搅拌储罐,其可以在稳定后供应挥发性杀菌剂; (vii)用于浓缩和复原麦芽汁(SMR)的搅拌储罐; (viii)用于浓缩馏出物(SDC)的搅拌储罐。首选功能:挥发性杀菌剂是SO2或甲醛的溶液,可回收利用,回收率大于98%。净化水(ET)包含来自蒸发器(EV)的冷凝蒸汽,并重新用于洗涤操作。萃取塔(CS)仅由来自蒸发器(EV)的蒸汽(VbP)加热,蒸汽可选地通过机械压缩进行压缩。蒸发器(EV)是一种级联式蒸发器,其中液体通过圆锥形喷嘴进行再循环和分配,并且其内外管温差为3-8摄氏度。洗涤塔的上部装有冷凝水和下部装有再循环的碱性溶液。

著录项

  • 公开/公告号FR2780719A1

    专利类型

  • 公开/公告日2000-01-07

    原文格式PDF

  • 申请/专利权人 COGAT PIERRE OLIVIER;

    申请/专利号FR19980008592

  • 发明设计人 COGAT PIERRE OLIVIER;

    申请日1998-07-06

  • 分类号C02F1/00;C02F1/50;C02F1/04;B01D3/14;B01D3/38;

  • 国家 FR

  • 入库时间 2022-08-22 01:39:45

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