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    • 3. 发明授权
    • Recovery boiler
    • 回收锅炉
    • US5771817A
    • 1998-06-30
    • US750880
    • 1996-12-17
    • Lars OlaussonJan BergmanSven-Erik JanssonAgneta Larsson
    • Lars OlaussonJan BergmanSven-Erik JanssonAgneta Larsson
    • D21C11/12F23G7/04F23L9/02
    • F23G7/04D21C11/12F23L9/02F23G2203/30
    • A recovery boiler for combusting spent liquor from cellulose cooking while at the same time recovering chemicals. The recovery boiler is constructed for so-called "rotafire" combustion and the speed of rotation of the secondary air has been increased by a constriction of the boiler being arranged at the tertiary air level. The invention also includes a process for using the boiler which is based on certain ports through which the secondary air is blown in being provided with air which is at a higher pressure than that at the other ports on the same level, thereby achieving a higher inflow velocity than from the other ports.
    • PCT No.PCT / SE95 / 00562 Sec。 371日期:1996年12月17日 102(e)日期1996年12月17日PCT提交1995年5月18日PCT公布。 WO95 / 35409 PCT出版物 日期1995年12月28日一种用于从纤维素烹饪中燃烧废液的回收锅炉,同时回收化学品。 回收锅炉构造为所谓的“rotafire”燃烧,并且通过在三级空气水平处布置的锅炉的收缩来增加二次空气的旋转速度。 本发明还包括一种使用锅炉的方法,该锅炉基于某些端口,二次空气通过该端口被吹送,该空气具有比在同一水平面上的其它端口处的压力更高的压力,从而实现更高的流入 速度比其他端口。
    • 5. 发明申请
    • METHOD AND EQUIPMENT FOR THE EVAPORATION OF BLACK LIQUOR THAT IS OBTAINED FROM A DIGESTION PROCESS DURING THE PRODUCTION OF CELLULOSE PULP
    • 用于在生产纤维素浆中从消毒过程中获得的黑色液体蒸发的方法和设备
    • US20100071862A1
    • 2010-03-25
    • US12513505
    • 2007-10-26
    • Lars Olausson
    • Lars Olausson
    • D21C11/10B01D1/26
    • B01D1/26B01D3/10B01D5/0036
    • The method and equipment are for the evaporation of hot black liquor obtained from a digestion process during the production of cellulose pulp. The black liquor is led to a multistage evaporation line with at least five evaporation stages. The black liquor that is to undergo evaporation in the evaporation line is cooled in at least one heat exchange process in a heat exchanger (HE1) against the partially evaporated black liquor that has undergone evaporation in at least one stage (I). The black liquor that is to undergo evaporation is cooled and the partially evaporated black liquor is heated by at least 5-10° C. The risk for the formation of foam and the separation of methanol are reduced. The greater part of the evaporation takes place at low temperature and at the lowest level of dry matter content in the liquor, which also suppresses encrustation in the stage.
    • 该方法和设备用于在纤维素纸浆生产期间从消化过程获得的热黑液的蒸发。 黑液被引到具有至少五个蒸发阶段的多级蒸发管线。 在蒸发管线中进行蒸发的黑液体在热交换器(HE1)中的至少一个热交换过程中被冷却至在至少一个阶段(I)中经历蒸发的部分蒸发的黑液。 将进行蒸发的黑液冷却,将部分蒸发的黑液加热至少5-10℃。形成泡沫和甲醇分离的风险降低。 蒸发的较大部分发生在低温和液体中干物质含量的最低水平,这也抑制了阶段的结垢。
    • 8. 发明授权
    • Method and equipment for the evaporation of black liquor that is obtained from a digestion process during the production of cellulose pulp
    • 在纤维素纸浆生产过程中从消化过程中获得的黑液蒸发的方法和设备
    • US08888955B2
    • 2014-11-18
    • US12513505
    • 2007-10-26
    • Lars Olausson
    • Lars Olausson
    • B01D1/26D21C11/10D21C7/10B01D3/10B01D5/00
    • B01D1/26B01D3/10B01D5/0036
    • The method and equipment are for the evaporation of hot black liquor obtained from a digestion process during the production of cellulose pulp. The black liquor is led to a multistage evaporation line with at least five evaporation stages. The black liquor that is to undergo evaporation in the evaporation line is cooled in at least one heat exchange process in a heat exchanger (HE1) against the partially evaporated black liquor that has undergone evaporation in at least one stage (I). The black liquor that is to undergo evaporation is cooled and the partially evaporated black liquor is heated by at least 5-10° C. The risk for the formation of foam and the separation of methanol are reduced. The greater part of the evaporation takes place at low temperature and at the lowest level of dry matter content in the liquor, which also suppresses encrustation in the stage.
    • 该方法和设备用于在纤维素纸浆生产期间从消化过程获得的热黑液的蒸发。 黑液被引到具有至少五个蒸发阶段的多级蒸发管线。 在蒸发管线中进行蒸发的黑液体在热交换器(HE1)中的至少一个热交换过程中被冷却至在至少一个阶段(I)中经历蒸发的部分蒸发的黑液。 将进行蒸发的黑液冷却,将部分蒸发的黑液加热至少5-10℃。形成泡沫和甲醇分离的风险降低。 蒸发的较大部分发生在低温和液体中干物质含量的最低水平,这也抑制了阶段中的结垢。