Method of Recovering Aqueous N-Methylmorpholine-N-Oxide Solution Used in Production of Lyocell Fiber
    5.
    发明申请
    Method of Recovering Aqueous N-Methylmorpholine-N-Oxide Solution Used in Production of Lyocell Fiber 审中-公开
    回收用于生产Lyocell纤维的N-甲基吗啉-N-氧化物水溶液的方法

    公开(公告)号:US20140008577A1

    公开(公告)日:2014-01-09

    申请号:US13953202

    申请日:2013-07-29

    CPC classification number: D01F13/00 D01F13/02 D21C11/0007 Y02P70/627

    Abstract: A method of recovering aqueous N-Methylmorpholine-N-Oxide solution used in production of Lyocell fiber comprises following steps. Bleach means for decoloring coloration in aqueous NMMO solution via alternate blow-mixing adsorption mode and static suspending adsorption mode reiteration. Filtration means for purifying the activated carbon powder and impurities by two filtering stages of first coarse filtering stage and second fine filtering stage. Concentration means for intensifying aqueous NMMO solution to obtain a condensed aqueous solution without NMMO solvent and a concentrated aqueous solution with NMMO solvent respectively by a sequential multi-stage evaporating system. Refinement means for purifying aqueous NMMO solution with promoting purity of concentrated aqueous solution to obtain required recovered aqueous solution by adding suitable agents in the redox reactions involved. Owing to streamlining and simplicity, the method not only has better competitiveness from promoted recovery cost, efficiency and quality but also meets regulations of environmental protection.

    Abstract translation: 回收生产Lyocell纤维中使用的N-甲基吗啉-N-氧化物水溶液的方法包括以下步骤。 漂白剂意味着通过交替吹气混合吸附模式和静态悬浮吸附模式重复来对NMMO水溶液中的着色进行脱色。 过滤是指通过第一粗过滤阶段和第二精细过滤阶段的两个过滤阶段来净化活性炭粉末和杂质。 浓缩装置用于强化NMMO水溶液以通过顺序多级蒸发系统分别得到不含NMMO溶剂的冷凝水溶液和具有NMMO溶剂的浓缩水溶液。 精制装置用于纯化NMMO水溶液,促进浓缩水溶液的纯度,通过在所涉及的氧化还原反应中加入适当的试剂来获得所需的回收水溶液。 由于精简简单,该方法不仅具有提升的回收成本,效率和质量的更好的竞争力,而且符合环保法规。

    Method for making product from fiber glass waste
    8.
    发明授权
    Method for making product from fiber glass waste 失效
    从玻璃纤维废物制造产品的方法

    公开(公告)号:US07416690B2

    公开(公告)日:2008-08-26

    申请号:US10725171

    申请日:2003-12-01

    Inventor: Michael J. Haun

    Abstract: The invention provides a method to transform large quantities of fiber glass waste into useful ceramic products by a low-cost manufacturing process. The method consists of reducing the fiber glass waste into a glass powder; mixing the glass powder with additives into a glass-additives mixture; granulating the glass-additives mixture into granulated particles; forming the granulated particles into a green ceramic article; and heating the green ceramic article into the ceramic product. Water and clay can be included in the processing. Only one firing step is needed with a low peak firing temperature of about 700° C. to about 1000° C. The method conserves energy and natural resources compared to clay-based traditional ceramic manufacturing. High-quality impervious ceramic products can be produced by the invention.

    Abstract translation: 本发明提供了一种通过低成本制造工艺将大量玻璃纤维废料转化为有用陶瓷产品的方法。 该方法包括将玻璃纤维废物减少为玻璃粉末; 将玻璃粉与添加剂混合成玻璃 - 添加剂混合物; 将玻璃添加剂混合物制粒成粒状颗粒; 将造粒颗粒形成绿色陶瓷制品; 并将生陶瓷制品加热到陶瓷制品中。 水和粘土可以包括在加工中。 只需要一个焙烧步骤,低峰值焙烧温度约为700℃至约1000℃。与基于粘土的传统陶瓷制造相比,该方法节省了能源和自然资源。 本发明可以生产高品质的不透性陶瓷产品。

    Process of separating catalyst from oxidation mixtures
    9.
    发明授权
    Process of separating catalyst from oxidation mixtures 失效
    从氧化混合物中分离催化剂的方法

    公开(公告)号:US6129875A

    公开(公告)日:2000-10-10

    申请号:US245156

    申请日:1999-02-04

    CPC classification number: C07C51/313

    Abstract: This invention relates to methods for controlling the oxidation of hydrocarbons to dibasic acids, in the presence of a catalyst and a monobasic acid, by removing the catalyst from the reaction mixture, outside the oxidation zone, after the oxidation has taken place at least partially. Initially, the catalyst is partially precipitated and removed by reducing the water level in the reaction mixture and/or subjecting the reaction mixture to a temperature, at which or over which catalyst precipitates. After the initial partial precipitation of the catalyst, the remaining catalyst is subjected to a thermal treatment, during which at least part of the monobasic acid is removed leaving behind molten dibasic acids, in which, at least a major part of the remaining catalyst is precipitated, and it is removed. A minor part of remaining catalyst is removed by methods, which include but are not limited to ion exchange, precipitation with a base or appropriate salt, and electrodialysis. The precipitated catalyst in the three removal stages may be recycled in miscellaneous ways. The dibasic acid(s) may be removed at least partially before or after any catalyst precipitation stage.

    Abstract translation: 本发明涉及在催化剂和一元酸的存在下,通过在至少部分氧化发生氧化区之后从反应混合物外部除去催化剂来控制烃类二元酸的氧化的方法。 最初,通过降低反应混合物中的水位和/或使反应混合物达到催化剂沉淀的温度,部分沉淀和除去催化剂。 在催化剂的初始部分沉淀之后,对剩余的催化剂进行热处理,其中除去至少部分一元酸,留下熔融二元酸,其中至少大部分剩余的催化剂沉淀 ,并被删除。 通过方法除去剩余催化剂的一小部分,其包括但不限于离子交换,用碱或适当的盐沉淀和电渗析。 三个去除阶段中的沉淀催化剂可以以各种方式回收。 在任何催化剂沉淀阶段之前或之后,可以至少部分去除二元酸。

    Process for disposing of carbon fibers
    10.
    发明授权
    Process for disposing of carbon fibers 失效
    处理碳纤维的方法

    公开(公告)号:US4411880A

    公开(公告)日:1983-10-25

    申请号:US378980

    申请日:1982-05-17

    CPC classification number: D01F11/121 D01F11/122 D01F13/00 Y02P70/625

    Abstract: A simple and efficient process is provided for disposing of easily airborne carbon fibers by subjecting them to an aqueous solution of an alkali metal or alkaline earth metal hypohalogenite at an elevated temperature for a period of time sufficient to substantially destroy the fibrous configuration of said fibers. In a preferred embodiment, carbon fibers are contacted with a solution of sodium hypochlorite (approximately 5 to 6 percent active chlorine concentration by weight based on the weight of the solution) at a temperature of between about 50.degree. and about 60.degree. C. for between about 1 and about 12 hours.

    Abstract translation: 提供了一种简单有效的方法,用于通过在高温下将碱金属或碱土金属次卤酸盐的水溶液经受足以基本上破坏所述纤维的纤维构造的时间来容易地处理空气中的碳纤维。 在一个优选的实施方案中,碳纤维与次氯酸钠溶液(基于溶液的重量计约5-6%的活性氯浓度)在约50℃至约60℃之间的温度下接触, 约1小时左右。

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