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    • 3. 发明授权
    • Pretreatment of chips before cooking
    • US06506283B2
    • 2003-01-14
    • US09770408
    • 2001-01-29
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • D21C706
    • D21C1/06
    • The strength properties of chemical cellulose pulp (particularly kraft pulp) are improved by substituting a cold impregnation soak for conventional impregnation procedures. After steaming, wood chips are soaked in an alkaline liquid at a temperature of about 80-110° C. (preferably 80-100° C., or 90-105° C.) for between one-half-72 hours (typically about 2-4 hours) at a pressure of about 0-15 bar (preferably about 1-5 bar), to dissolve at least about 8% of the wood (preferably about 10-20%) and at least about 15% of the lignin. The alkaline liquid used preferably contains sulfide (e.g. black liquor, green liquor, white liquor, or mixtures thereof), but almost any alkaline liquid having an alkali concentration of about 1.0 mole of NaOH/liter or less (typically about 0.75 m/l or less) is suitable. The wood chips are then raised to a cooking temperature of about 145-180° C. and cooked to produce the cellulose chemical pulp. There may be an intermediate step, between soaking and raising the cooking temperature, of heating the wood chips to a temperature of about 110-150° C. (preferably about 120-140° C.) for about 10-90 minutes (preferably about 10-30 minutes). Alternatively or additionally the majority of the dissolved lignin (and/or other solids) may be removed before raising the wood chips to cooking temperature. The system for treating the wood chips need only include a low pressure soaking vessel (with an associated pump or other transfer device) in addition to conventional equipment.
    • 5. 发明授权
    • Pretreatment of chips before cooking
    • 烹饪前预处理薯片
    • US06248208B1
    • 2001-06-19
    • US08460723
    • 1995-06-02
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • D21C102
    • D21C1/06
    • The strength properties of chemical cellulose pulp (particularly kraft pulp) are improved by substituting a cold impregnation soak for conventional impregnation procedures. After steaming, wood chips are soaked in an alkaline liquid at a temperature of about 80-110° C. (preferably 80-100° C., or alternatively 90-105° C.) for between one-half-72 hours (typically about 2-4 hours) at a pressure of about 0-15 bar (preferably about 1-5 bar), to dissolve at least about 8% of the wood (preferably about 10-20%) and at least about 15% of the lignin. The alkaline liquid used preferably contains sulfide (e.g. black liquor, green liquor, white liquor, or mixtures thereof), but almost any alkaline liquid having an alkali concentration of about 1.0 mole of NaOH/liter or less (typically about 0.75 m/l or less) is suitable. The wood chips are then raised to a cooking temperature of about 145-180° C. and cooked to produce the cellulose chemical pulp. There may be an intermediate step, between soaking and raising the cooking temperature, of heating the wood chips to a temperature of about 110-150° C. (preferably about 120-140° C.) for about 10-90 minutes (preferably about 10-30 minutes). Alternatively or additionally the majority of the dissolved lignin (and/or other solids) may be removed before raising the wood chips to cooking temperature. The system for treating the wood chips need only include a low pressure soaking vessel (with an associated pump or other transfer device) in addition to conventional equipment.
    • 化学纤维素纸浆(特别是牛皮纸浆)的强度性能通过用常规浸渍方法的冷浸渍浸渍来改善。 蒸汽之后,将木屑浸入碱性液体中,温度约为80-110℃(优选80-100℃,或90-105℃)浸渍半个小时之间(通常为 约2-4小时),在约0-15巴(优选约1-5巴)的压力下溶解至少约8%的木材(优选约10-20%)和至少约15% 木质素。 使用的碱性液体优选含有硫化物(例如黑液,绿液,白液或其混合物),但几乎任何碱性浓度为约1.0摩尔NaOH /升或更低(通常约0.75米2 /升)或 少)适合。 然后将木屑升至约145-180℃的烹饪温度,并煮熟以生产纤维素化学纸浆。 在浸泡和提高烹饪温度之间可以有一个中间步骤,将木片加热至约110-150℃(优选约120-140℃)的温度约10-90分钟(优选约为 10-30分钟)。 或者或另外,在将木屑升高至烹饪温度之前,可以除去大部分溶解的木质素(和/或其它固体)。 用于处理木片的系统除了常规设备之外仅需要包括低压均热容器(具有相关联的泵或其它转移装置)。
    • 6. 发明授权
    • Pretreatment of chips before cooking
    • US06544384B2
    • 2003-04-08
    • US09975984
    • 2001-10-15
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • Kaj O. HenricsonAki Hannu VilpponenHannu Olavi RamarkAuvo Kimmo KettunenC. Bertil Stromberg
    • D21C712
    • D21C1/06
    • The strength properties of chemical cellulose pulp (particularly kraft pulp) are improved by substituting a cold impregnation soak for conventional impregnation procedures. After steaming, wood chips are soaked in an alkaline liquid at a temperature of about 80-110° C. (preferably 80-100° C., or 90-105° C.) for between one-half-72 hours (typically about 2-4 hours) at a pressure of about 0-15 bar (preferably about 1-5 bar), to dissolve at least about 8% of the wood (preferably about 10-20%) and at least about 15% of the lignin. The alkaline liquid used preferably contains sulfide (e.g. black liquor, green liquor, white liquor, or mixtures thereof), but almost any alkaline liquid having an alkali concentration of about 1.0 mole of NaOH/liter or less (typically about 0.75 m/l or less) is suitable. The wood chips are then raised to a cooking temperature of about 145-180° C. and cooked to produce the cellulose chemical pulp. There may be an intermediate step, between soaking and raising the cooking temperature, of heating the wood chips to a temperature of about 110-150° C. (preferably about 120-140° C.) for about 10-90 minutes (preferably about 10-30 minutes). Alternatively or additionally the majority of the dissolved lignin (and/or other solids) may be removed before raising the wood chips to cooking temperature. The system for treating the wood chips need only include a low pressure soaking vessel (with an associated pump or other transfer device) in addition to conventional equipment.
    • 7. 发明授权
    • Low temperature gas phase continuous digester
    • 低温气相连续蒸煮器
    • US6024837A
    • 2000-02-15
    • US14243
    • 1998-01-27
    • Richard LaaksoC. Bertil StrombergKaj Henricson
    • Richard LaaksoC. Bertil StrombergKaj Henricson
    • D21C7/00D21C3/22D21C3/24D21C7/06D21C7/10D21C7/12
    • D21C7/06D21C3/22D21C3/24D21C7/00D21C7/10
    • 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.
    • 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。
    • 8. 发明授权
    • Continuous digester with a low temperature gas-phase
    • 连续蒸煮器具有低温气相
    • US5882477A
    • 1999-03-16
    • US797327
    • 1997-02-10
    • Richard LaaksoC. Bertil Stromberg
    • Richard LaaksoC. Bertil Stromberg
    • D21C7/00D21C3/22D21C3/24D21C7/06D21C7/10D21C7/12D21C3/26
    • D21C7/06D21C3/22D21C3/24D21C7/00D21C7/10
    • 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 chips are heated by recirculating and heating liquid using a recirculation loop below the chips level, and a countercurrent flow zone is preferably provided.
    • 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。 通过使用低于芯片水平面的再循环回路循环和加热液体来加热芯片,并且优选地提供逆流流动区域。