Composition and Method of Application of Precious Metals to Tobacco Products
    1.
    发明申请
    Composition and Method of Application of Precious Metals to Tobacco Products 审中-公开
    贵金属应用于烟草制品的组成和方法

    公开(公告)号:US20130333710A1

    公开(公告)日:2013-12-19

    申请号:US13495582

    申请日:2012-06-13

    IPC分类号: A24C1/00 A24B15/10

    摘要: A method of applying precious and semi-precious metals to cigars such that the draw and ignitability of the cigar remains unaffected by the application. An embodiment of the present invention includes a composition and method of applying edible gold leaf to the external surface or wrapper of a cigar or rolled tobacco product.

    摘要翻译: 贵金属和半贵金属应用于雪茄的方法,使得雪茄的拉丝和点火性不受应用影响。 本发明的一个实施方案包括将可食用金箔施用到雪茄或卷烟烟草制品的外表面或包装物上的组合物和方法。

    Chemical process and production unit
    2.
    发明申请
    Chemical process and production unit 有权
    化工过程和生产单位

    公开(公告)号:US20060133983A1

    公开(公告)日:2006-06-22

    申请号:US11281890

    申请日:2005-11-18

    IPC分类号: C01B11/02 B01J8/00

    摘要: The invention relates to a continuous process for producing chlorine dioxide comprising the steps of continuously: a) feeding to a reactor (1) an acid, hydrogen peroxide and alkali metal chlorate; b) reacting the alkali metal chlorate with the acid and the hydrogen peroxide to form a product stream (2) containing chlorine dioxide, oxygen and alkali metal salt of the acid, c) bringing the product stream from the reactor to an eductor (3) and mixing it with motive water fed to the eductor and thereby forming a diluted product stream; d) removing oxygen from the diluted product stream; e) withdrawing part of the diluted product stream (9), before, during or after the step of removing oxygen; f) adding water (11) to the non-withdrawn part of the diluted product stream to form a recycle stream (12); and, g) bringing the recycle stream (12) to the eductor and feeding it thereto as motive water (4). The invention further relates to a production unit for the production of an aqueous solution comprising chlorine dioxide.

    摘要翻译: 本发明涉及一种用于生产二氧化氯的连续方法,包括以下步骤:连续地:a)将酸,过氧化氢和碱金属氯酸盐进料到反应器(1)中; b)使碱金属氯酸盐与酸和过氧化氢反应以形成含有二氧化氯,酸的氧和碱金属盐的产物流(2),c)将来自反应器的产物流引入喷射器(3) 并将其与供给到喷射器的动力水混合,从而形成稀释的产物流; d)从稀释的产物流中除去氧气; e)在除去氧气的步骤之前,期间或之后取出部分稀释产物流(9); f)向稀释产物流的未抽出部分加入水(11)以形成循环物流(12); 并且g)将再循环物流(12)引入喷射器并将其作为运动水(4)进料。 本发明还涉及用于生产包含二氧化氯的水溶液的生产单元。

    Process for production of chlorine dioxide
    3.
    发明申请
    Process for production of chlorine dioxide 审中-公开
    二氧化氯生产工艺

    公开(公告)号:US20070116637A1

    公开(公告)日:2007-05-24

    申请号:US11598226

    申请日:2006-11-13

    IPC分类号: C01B11/02 B01J19/00

    CPC分类号: C01B11/025 B01J2219/0011

    摘要: The present invention relates to a process for the production of chlorine dioxide, said process comprising the steps of continuously: (a) feeding to a reactor an acid, alkali metal chlorate and a reducing agent; (b) reacting the alkali metal chlorate with the acid and the reducing agent to form a product stream comprising chlorine dioxide and alkali metal salt of the acid; (c) bringing the product stream from the reactor to an eductor and mixing it with motive fluid fed to the eductor and thereby forming a diluted product stream; (d) bringing the diluted product stream to a gas-liquid separator where gas is separated from liquid therein; (e) withdrawing a gaseous product stream comprising chlorine dioxide and inert gas from said gas-liquid separator; and, (f) withdrawing a liquid phase from the gas-liquid separator. The invention also relates to a production unit to produce chlorine dioxide.

    摘要翻译: 本发明涉及一种生产二氧化氯的方法,所述方法包括以下步骤:连续地:(a)向反应器中加入酸,碱金属氯酸盐和还原剂; (b)碱金属氯酸盐与酸和还原剂反应形成包含二氧化氯和酸的碱金属盐的产物流; (c)将来自反应器的产物流引入喷射器并将其与供给到喷射器的动力流体混合,从而形成稀释的产物流; (d)将稀释的产物流送入气液分离器,其中气体与液体分离; (e)从所述气液分离器中取出包含二氧化氯和惰性气体的气态产物流; 和(f)从气 - 液分离器中取出液相。 本发明还涉及生产二氧化氯的生产单元。

    Process for treating wastewater from a bleach plant
    4.
    发明授权
    Process for treating wastewater from a bleach plant 有权
    处理漂白厂废水的工艺

    公开(公告)号:US06425974B1

    公开(公告)日:2002-07-30

    申请号:US09380335

    申请日:1999-11-08

    IPC分类号: D21C1100

    摘要: The process according to the present invention relates to the treatment of wastewater discharged from a bleach plant and more particularly treatment of bleach plant alkaline wash filtrate from treatment-steps and/or delignification/bleaching-steps of pulp. Further improvements of known processes are needed for solving the problems associated with the recovery of alkaline filtrates into the chemical recovery system. According to the process of the present invention, alkaline wash filtrate from treatment-steps and/or delignification/bleaching-steps of pulp is treated in a process by the following steps: i) treating at least a part of the alkaline filtrate in order to produce an alkaline concentrate enriched in high molecular weight dissolved organic compounds and a stream depleted in organic compounds, where the share of the alkaline concentrate to the total amount of the alkaline filtrate corresponds to a volume reduction factor (VRP) in the range of from about 2.0 up to about 7.5; ii) withdrawing the depleted stream; iii) collecting at least a part of the alkaline concentrate from step i) and using the concentrate as wash or dilution water in brownstock washing fiberline with a dilution factor of up to about 4.0, where at least a part of the washing filtrate is brought to the chemical recovery system.

    摘要翻译: 根据本发明的方法涉及从漂白设备排出的废水的处理,更具体地说是处理步骤和/或纸浆的脱木素/漂白步骤处理漂白剂碱性洗涤滤液。 需要进一步改进已知的方法来解决与将碱性滤液回收到化学品回收系统中相关的问题。 根据本发明的方法,通过以下步骤处理来自处理步骤和/或脱木素/漂白步骤的纸浆的碱洗涤滤液:i)处理至少一部分碱性滤液以便 产生富含高分子量溶解的有机化合物的碱性浓缩物和贫的有机化合物的流,其中碱性浓缩物与碱性滤液的总量相当于体积减少因子(VRP)在约 2.0至7.5; ii)撤回耗尽的流; iii)收集来自步骤i)的至少一部分碱性浓缩物,并将稀释浓度用作洗涤或稀释水作为洗涤或稀释水,稀释倍数高达约4.0,其中至少一部分洗涤滤液被带到 化学品回收系统。