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    • 4. 发明公开
    • METHOD FOR LEACHING RECOVERY-BOILER ASH
    • 浸取回收锅炉灰的方法
    • EP2920359A1
    • 2015-09-23
    • EP13808059.3
    • 2013-11-15
    • Andritz Oy
    • McKEOUGH Paterson
    • D21C11/00D21C11/12
    • D21C11/066C22B7/007C22B26/10D21C11/0007D21C11/0064D21C11/12Y02P40/44Y02P70/24
    • The subject of the invention is a new method to be used in conjunction with a single- stage or multi-stage process for leaching ash originating from the recovery boiler of a pulp mill, particularly when the ash contains a significant amount of carbonate. In the method, calcium compounds, most preferably calcium oxide (CaO) and/or calcium hydroxide (Ca(OH)2), are employed as additives in one or more leaching stages. The liquid fraction formed in the leaching process is utilized outside the main chemical recovery cycle, preferably as a substitute for purchased sodium hydroxide in the bleaching line of the pulp mill. The solids fraction may be mixed with a black-liquor stream of the mill or subjected to further processing in order to separate calcium compounds for recycle.
    • 本发明的主题是与用于沥滤来自纸浆厂的回收锅炉的灰分的单阶段或多阶段方法结合使用的新方法,特别是当灰分含有大量碳酸盐时。 在该方法中,在一个或多个浸出阶段中使用钙化合物,最优选氧化钙(CaO)和/或氢氧化钙(Ca(OH)2)作为添加剂。 浸出过程中形成的液体部分在主化学回收循环之外使用,优选作为纸浆厂漂白生产线中购买的氢氧化钠的替代品。 固体部分可与磨机的黑液流混合或进行进一步处理以分离用于再循环的钙化合物。
    • 9. 发明公开
    • Leaching process
    • 浸出过程
    • EP0754799A3
    • 1997-03-26
    • EP96201661.4
    • 1996-06-14
    • Eka Chemicals AB
    • Landfors, JohanHammer-Olsen, RoyHäggström, Kimona
    • D21C11/06D21C11/12
    • D21C11/125C02F1/469D21C11/066
    • An increasing problem with the pulping chemical recovery system, is the presence of chloride and potassium in the recovery boiler. Chloride and potassium increase inter alia the stickiness of carryover deposits and dust particles to the recovery boiler tubes, which accelerate fouling, corrosion and plugging of the recovery boiler. As the environmental legislation becomes more stringent, the degree of system closure increases. The present invention relates to a process by which the collected precipitator dust (1) is leached (2), at a temperature exceeding 50°C, for a residence time sufficient to get a chloride and potassium enriched leach solution (4) and to remove at least a part of the content of metal ions in a solid phase (3). Said leach solution is electrochemically treated (5), preferably in an electrodialysis cell, in order to remove at least a part of the chloride and potassium therein. By the present process, the problem of sticky deposits in the recovery boiler can be substantially reduced. This means an improved energy efficiency as well as a higher degree of recovery of the pulping and bleaching chemicals.
    • 制浆化学回收系统存在的问题是回收锅炉中存在氯化物和钾。 氯化物和钾会增加夹带沉积物和灰尘颗粒到回收锅炉管的粘性,这会加速回收锅炉的结垢,腐蚀和堵塞。 随着环境立法越来越严格,系统关闭的程度越来越高。 本发明涉及一种方法,其中在超过50℃的温度下将收集的沉淀器粉尘(1)浸出(2)足以获得富含氯化物和钾的浸出溶液(4)的停留时间并去除 (3)中的至少一部分金属离子的含量。 所述浸出溶液电化学处理(5),优选在电渗析池中,以除去其中的至少一部分氯化物和钾。 通过本过程,回收锅炉中的粘性沉积物的问题可以大大减少。 这意味着改进的能源效率以及制浆和漂白化学品的更高程度的回收率。