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1. 发明授权

US07070677B2 Method and apparatus for treating pulp with filler 失效
标题翻译：用填料处理纸浆的方法和设备
公开(公告)号：US07070677B2
公开(公告)日：2006-07-04
申请号：US10415921
申请日：2001-11-14
申请人： Kaj Henricson
发明人： Kaj Henricson
IPC分类号： D21H17/70 , D21H17/67
CPC分类号： D21H17/70 , D21H17/675 , D21H23/20
摘要： The present invention relates to a method of and apparatus for treating pulp with filler. The method and apparatus according to the invention are especially well suitable for treating pulp with filler, the mixing of which to the pulp requires simultaneous treatment of the pulp with gas. The treatment of cellulose pulp suspension of the paper making industry and calcium hydroxide with carbon dioxide is presented as one preferred embodiment of the invention.
摘要翻译：本发明涉及一种用填料处理纸浆的方法和设备。根据本发明的方法和设备特别适用于用填料处理纸浆，其与纸浆的混合需要用气体同时处理纸浆。作为本发明的一个优选实施方案，提出了造纸工业的纤维素纸浆悬浮液和氢氧化钙与二氧化碳的处理。

2. 发明授权

US5607545A Ozone bleaching process utilizing a fluidizing mixer and super-atmospheric pressure 失效
标题翻译：臭氧漂白工艺利用流化搅拌机和超大气压力
公开(公告)号：US5607545A
公开(公告)日：1997-03-04
申请号：US935334
申请日：1992-08-27
申请人： Kaj Henricson , Brian Greenwood
发明人： Kaj Henricson , Brian Greenwood
IPC分类号： D21C9/10 , D21C9/153 , D21C9/14 , D21C9/16
CPC分类号： D21C9/153 , D21C9/10
摘要： Method and apparatus for ozone bleaching a medium consistency cellulosic fiber suspension include feeding the fiber suspension and an ozone in carrier gas stream under pressure into a fluidizing mixer; intimately and uniformly mixing the fiber suspension with the ozone to achieve a bleaching reaction; passing the mixture into a first reaction vessel to permit the bleaching reaction to proceed and to consume a major part of the ozone; adding a second bleaching chemical to the mixture; separating the excess ozone and carrier gas from the mixture in a second considerably larger vessel and removing the fiber suspension from the second vessel after the effective second bleaching reaction.
摘要翻译：用于臭氧漂白中等稠度纤维素纤维悬浮液的方法和装置包括在压力下将纤维悬浮液和载气中的臭氧进料到流化混合器中; 将纤维悬浮液与臭氧紧密均匀混合以实现漂白反应; 将混合物通入第一反应容器以允许漂白反应进行并消耗大部分臭氧; 向混合物中加入第二漂白化学品; 在第二相当大的容器中从混合物中分离多余的臭氧和载气，并在有效的第二漂白反应之后从第二容器中除去纤维悬浮液。

3. 发明授权

US5575395A Method and apparatus for screening fibrous suspensions 失效
标题翻译：筛选纤维悬浮液的方法和装置
公开(公告)号：US5575395A
公开(公告)日：1996-11-19
申请号：US275343
申请日：1994-07-15
申请人： Timo Alajaaski , Kaj Henricson , Kalevi Laakso , Antero Laine , Risto Ljokkoi , Olavi Pikka , Markku Simola , Pertti Wathen
发明人： Timo Alajaaski , Kaj Henricson , Kalevi Laakso , Antero Laine , Risto Ljokkoi , Olavi Pikka , Markku Simola , Pertti Wathen
IPC分类号： D21D5/00 , D21D5/02 , B03B7/00
CPC分类号： D21D5/026 , D21D5/00
摘要： A fiber suspension, such as an in a pulp mill, is treated in an manner which minimizes both the investment and the operating costs associated with a screening plant. A single pump has an outlet connected to a knotter and primary and secondary screening states so that the pump provides substantially the sole motive force to the pulp moving it through the knotter and screening stages. The knotter and screening stages are provided in a common housing with the knotter vertically above the screening stages, and the screening stages one above the other. A single motor may be provided to rotate rotatable elements associated with the knotter and screening stages. The knotter may be connected to a knot washer external of the housing by a valved conduit less than two meters in length, and the secondary screening stage can be connected to a tertiary screening stage exterior of the housing by a valved conduit less than two meters long. Rejects from the knot washer and secondary screening stage may be recycled to the pulp inlet, and dilution water may be introduced where necessary.
摘要翻译：纤维悬浮液，例如在纸浆厂中，以最小化与筛选设备相关的投资和操作成本的方式进行处理。单个泵具有连接到打结器和主要和次要筛选状态的出口，使得泵基本上为通过打结器和筛选阶段将纸浆移动的纸浆提供唯一的动力。打结器和筛选阶段提供在公共壳体中，打结器垂直地位于筛选阶段上方，筛选阶段一个在另一个之上。可以提供单个电动机以旋转与打结器和筛选阶段相关联的可旋转元件。打结器可以通过长度不超过两米的阀门导管连接到外壳外部的结垫圈，并且二次筛分阶段可以通过小于两米长的阀门导管连接到壳体外部的三级筛分台。结节垫和二次筛分阶段的拒绝可以再循环到纸浆入口，并且必要时可以引入稀释水。

4. 发明授权

US5328563A Method of treating material containing sodium sulphate and/or sodium carbonate in a pulp mill 失效
标题翻译：在纸浆厂中处理含有硫酸钠和/或碳酸钠的材料的方法
公开(公告)号：US5328563A
公开(公告)日：1994-07-12
申请号：US943234
申请日：1992-09-11
申请人： Kaj Henricson , Anja Klarin
发明人： Kaj Henricson , Anja Klarin
IPC分类号： C01B17/22 , C01B17/28 , D21C11/00 , D21C11/04 , D21C11/06
CPC分类号： D21C11/066 , C01B17/22 , C01B17/28 , D21C11/0071 , D21C11/04
摘要： Sodium sulphate and/or sodium carbonate containing material from a cellulose pulp mill, such as fly ash from a recovery boiler, or a by-product from a chlorine dioxide production plant, is brought into contact with a a gas containing hydrocarbons and/or hydrogen sulphide which chemically reacts with the material to produce sodium sulphide. Preferably the gas contains one or both of ethene and hydrogen sulphide. The sodium sulphide produced is used to effect sulphate cooking of cellulose pulp. The gas may be brought into contact with the melt of a soda recovery boiler to increase its sulphidity, either prior to, after, or simultaneously with bringing the gas into contact with the material. The sources of the fly ash and melt may be a soda recovery boiler combusting black liquor under oxidizing conditions.
摘要翻译：来自纤维素纸浆磨机的来自回收锅炉的飞灰或来自二氧化氯生产设备的副产物的含硫酸钠和/或碳酸钠的物质与含有烃和/或硫化氢的气体接触其与该材料发生化学反应以产生硫化钠。气体优选包含乙烯和硫化氢中的一种或两种。所生产的硫化钠用于对纤维素纸浆进行硫酸盐蒸煮。气体可以与苏打回收锅炉的熔体接触，以在使气体与材料接触之前，之后或同时使其硫化物增加。飞灰和熔体的来源可以是在氧化条件下燃烧黑液的苏打回收锅炉。

5. 发明授权

US5323914A Method of and apparatus for separating heavy impurities from fiber suspensions in connection with pumping 失效
标题翻译：从泵送中分离纤维悬浮液中的重杂质的方法和设备
公开(公告)号：US5323914A
公开(公告)日：1994-06-28
申请号：US778814
申请日：1992-02-06
申请人： Kaj Henricson , Raimo Pitkanen , Pentti Vikio
发明人： Kaj Henricson , Raimo Pitkanen , Pentti Vikio
IPC分类号： B01D21/26 , D21D5/20 , F04D7/04 , F04D29/44 , B04B5/12
CPC分类号： F04D7/045 , B01D21/262 , D21D5/20 , F04D29/445 , F05B2210/132
摘要： A method and an apparatus for separating heavy impurities from a fiber suspension include a centrifugal pump capable of separating heavy impurities towards the periphery of the interior chamber of the pump. The fiber suspension is caused to rotate in the interior chamber so as to urge the suspension downstream as well as separate the impurities towards the periphery of the chamber where they can be collected.
摘要翻译： PCT No.PCT / FI90 / 00154 Sec。 371日期：1992年2月6日 102（e）日期1992年2月6日PCT Filed 1990年6月6日PCT公布。 WO90 / 15183 PCT出版物日本1990年12月13日。用于从纤维悬浮液中分离重杂质的方法和设备包括能够将重质杂质分离到泵的内部室的周边的离心泵。使纤维悬浮液在内部室中旋转，以便将下游的悬浮液推动并将杂质分离到室的周边，在那里它们可被收集。

6. 发明授权

US08277608B2 Method for treating pulp in connection with the bleaching of chemical pulp 有权
标题翻译：与化学纸浆漂白有关的纸浆处理方法
公开(公告)号：US08277608B2
公开(公告)日：2012-10-02
申请号：US10595053
申请日：2004-06-17
申请人： Kaj Henricson , Olavi Pikka , Pekka Tervola
发明人： Kaj Henricson , Olavi Pikka , Pekka Tervola
IPC分类号： D21C9/02
CPC分类号： D21C9/14 , D21C9/02 , D21C9/08 , D21C9/153
摘要： A method of treating pulp in connection with the bleaching of chemical pulp, said method including treating of the pulp in at least an ozone, chlorine dioxide or alkali phase and thereafter washing of the pulp in a washing device having an E10 value of at least 3, whereby washing liquid is introduced into the washing device countercurrently in relation to the pulp and filtrate is discharged from the washing device. At first the pulp is washed in the washing device so that the washing liquid is filtrate obtained from the washing device itself and the amount of thus circulated washing liquid is 1.5 - 3.5 t/adt pulp, whereafter the pulp is washed with liquid introduced from outside the washing device, the amount of said liquid being such that the dilution factor in the latter wash is less than 1 t/adt and that the total amount of washing liquid used in the washing device is such that the dilution factor is more than 0 t/adt.
摘要翻译：一种处理与化学纸浆漂白有关的纸浆的方法，所述方法包括至少在臭氧，二氧化氯或碱相中处理纸浆，然后在具有至少3的E10值的洗涤装置中清洗纸浆其中洗涤液相对于纸浆逆流地引入洗涤装置中，滤液从洗涤装置排出。首先，在洗涤装置中洗涤纸浆，使得洗涤液体是从洗涤装置本身获得的滤液，并且这样循环的洗涤液体的量为1.5-3.5吨/重量浆，然后用从外部引入的液体洗涤纸浆洗涤装置，所述液体的量使得后一次洗涤中的稀释因子小于1t / adt，并且洗涤装置中使用的洗涤液的总量使得稀释因子大于0t / adt。

7. 发明申请

US20050087314A1 Pulp cooking with particular alkali profiles 审中-公开
标题翻译：用特定的碱性型材烹制的纸浆
公开(公告)号：US20050087314A1
公开(公告)日：2005-04-28
申请号：US10994262
申请日：2004-11-23
申请人： C. Stromberg , Auvo Kettunen , Jian Jiang , Kaj Henricson
发明人： C. Stromberg , Auvo Kettunen , Jian Jiang , Kaj Henricson
IPC分类号： D21C3/02 , D21C3/26 , D21C7/10 , D21C7/14 , D21B1/16
CPC分类号： D21C7/14 , D21C3/02 , D21C3/26 , D21C7/10
摘要： Yield, particularly when treating hardwood chips, can be improved by at least 1-2% in a kraft cellulose pulping process by keeping the temperature and effective alkali (EA) low during impregnation, and by keeping the EA low in at least a first cook stage. After cooking, the pulp is subjected to cooling low EA liquor, e.g. to reduce its temperature to below 120° C. (preferably below 100° C.) with an EA below about 5 g/L (expressed as NaOH). Continuous treatment in a continuous digester system is preferred, with the EA below about 20 g/L during impregnation and the first cook.
摘要翻译：产量，特别是当处理硬木屑时，可以通过在浸渍过程中保持温度和有效碱（EA）较低，并且通过将EA保持在至少第一次烹调中而在牛皮纸纤维素制浆过程中提高至少1-2％阶段。烹饪后，将纸浆冷却到低EA液，例如将其温度降低到低于120℃（优选低于100℃），EA低于约5g / L（以NaOH表示）。在连续蒸煮系统中的连续处理是优选的，在浸渍和第一次煮煮期间，EA低于约20g / L。

8. 发明授权

US06733625B2 Method and apparatus for treating pulp 失效
标题翻译：纸浆处理方法和设备
公开(公告)号：US06733625B2
公开(公告)日：2004-05-11
申请号：US09855022
申请日：2001-05-15
申请人： Kaj Henricson , Eero Kontturi , Olavi Pikka , Janne Vehmaa
发明人： Kaj Henricson , Eero Kontturi , Olavi Pikka , Janne Vehmaa
IPC分类号： D21C902
CPC分类号： D21C9/147 , D21C9/163 , D21C11/0028
摘要： The present invention relates to a method of treating chemical pulp in order to optimize the consumption of bleaching chemicals and to improve the quality of the pulp. Especially the invention relates to a method according to which filtrate obtained from a suitable stage of the washing of brown stock preferably cooked by an alkaline cooking method is treated with an oxidizing chemical prior to the oxygen stage following the brown stock washing.
摘要翻译：本发明涉及一种处理化学纸浆的方法，以优化漂白化学品的消耗并提高纸浆的质量。特别地，本发明涉及一种方法，根据该方法，通过碱性烹饪方法烹饪的棕色原液的洗涤的合适阶段得到的滤液在褐色洗涤后的氧气阶段之前用氧化剂处理。

9. 发明授权

US6024837A Low temperature gas phase continuous digester 失效
标题翻译：低温气相连续蒸煮器
公开(公告)号：US6024837A
公开(公告)日：2000-02-15
申请号：US14243
申请日：1998-01-27
申请人： Richard Laakso , C. Bertil Stromberg , Kaj Henricson
发明人： Richard Laakso , C. Bertil Stromberg , Kaj Henricson
IPC分类号： D21C7/00 , D21C3/22 , D21C3/24 , D21C7/06 , D21C7/10 , D21C7/12
CPC分类号： D21C7/06 , D21C3/22 , D21C3/24 , D21C7/00 , D21C7/10
摘要： A cellulose pulp continuous digester (e.g. for producing kraft pulp) is operated so that it has the advantages of a hydraulic digester yet has a gas-filled zone over the liquid level. A slurry of chips and cooking liquor is introduced into the top of the digester vessel through an inverted top separator. A liquid level is established below the inverted top separator, and a chips level is established below the inverted top separator (above or below the liquid level). A gas-filled zone above the liquid level includes compressed gas, and is at a temperature of less than 160 (preferably less than 120).degree. C. and at a pressure of between 50-200 (preferably 80-150) psig. The digester may have a first diameter portion (about 3-5 meters) at the top and a second diameter portion (at least about seven meters) below the top, with the inverted separator in the first diameter portion, the liquid level in the first diameter portion, and the chips level in the second diameter portion. A shoulder is provided between the first and second diameter portions and a withdrawal screen is preferably mounted just below the shoulder in the second diameter portion. A plurality of different liquor flows may be extracted from the inverted top separator.
摘要翻译：操作纤维素纸浆连续蒸煮器（例如，用于生产牛皮纸浆）的操作使得其具有液压消化器的优点，但在液面上具有气体填充区域。将碎屑和蒸煮液的浆料通过倒置的顶部分离器引入蒸煮器容器的顶部。在倒置顶部分离器下面建立一个液位，并且在倒置顶部分离器之下建立一个切片液面（在液面上方或下方）。液面以上的充气区包括压缩气体，并且温度低于160℃（优选小于120℃），压力为50-200（优选80-150）psig。蒸煮器可以在顶部具有第一直径部分（约3-5米），在顶部具有第二直径部分（至少约七米），第一直径部分中的反向分离器，第一直径部分直径部分和第二直径部分中的切屑液面。肩部设置在第一直径部分和第二直径部分之间，并且优选地将拔出筛网安装在第二直径部分的肩部正下方。可以从倒置的顶部分离器中提取多个不同的液流。

10. 发明授权

US5411634A Medium consistency ozone bleaching 失效
标题翻译：中等稠度臭氧漂白
公开(公告)号：US5411634A
公开(公告)日：1995-05-02
申请号：US710439
申请日：1991-06-07
申请人： Kaj Henricson , Joseph Phillips , Brian F. Greenwood , Erwin D. Funk , Stephen J. Dunne
发明人： Kaj Henricson , Joseph Phillips , Brian F. Greenwood , Erwin D. Funk , Stephen J. Dunne
IPC分类号： D21C9/10 , D21C9/153
CPC分类号： D21C9/153
摘要： In a method of bleaching medium consistency pulp with ozone using a mixer, ozone containing gas and about 6-15% consistency pulp are fed to the mixer, and then discharged in a first, preferably vertical, path. The mixture of pulp and ozone moves in a first part of the vertical path a time period of about 1-5 seconds at a velocity of about 1-5 m/s so that the gas and pulp do not separate during movement in this first part, and the vast majority of the pulp brightening reaction between the ozone and pulp takes place. This is preferably accomplished by passing the mixture upwardly in a small diameter conduit having a height of about 3-20 meters. Then the velocity of the pulp is slowed while still moving in the first path, preferably by feeding it directly to a much larger diameter (e. g. 1.5-10 times) conduit, so the height of the unit may be kept under 100 feet. The pulp flows in the large diameter conduit for about 0.5-5 minutes so that residual reactions take place.
摘要翻译：在使用混合器将具有臭氧的中等稠度纸浆漂白的方法中，将含臭氧的气体和约6-15％浓度的纸浆送入混合器中，然后以第一，优选垂直的路径排出。纸浆和臭氧的混合物以约1-5m / s的速度在垂直路径的第一部分中移动大约1-5秒的时间段，使得气体和纸浆在该第一部分的运动期间不分离，并且发生了臭氧和纸浆之间绝大多数纸浆增白反应。这优选通过将混合物向上通过高度为约3-20米的小直径导管来完成。然后，纸浆的速度在第一路径中仍然运动时减速，优选通过将其直接送入更大直径（例如1.5-10倍）的导管，因此该单元的高度可以保持在100英尺以下。纸浆在大直径导管中流动约0.5-5分钟，从而发生残留反应。

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