公开(公告)号：US09416493B2

公开(公告)日：2016-08-16

申请号：US14378407

申请日：2013-02-12

Applicant: UPM-KYMMENE CORPORATION

Inventor： Kari Hillebrand ,  Markus Nuopponen ,  Martina Lille ,  Juha Tamper

IPC: D21H11/18 ,  D21F1/66 ,  D21F5/00 ,  D21F1/10 ,  D21C9/18 ,  D21H25/04 ,  D21H15/02

CPC classification number: D21H11/18 ,  D21C9/18 ,  D21F1/10 ,  D21F1/66 ,  D21F5/00 ,  D21H15/02 ,  D21H25/04

Abstract: The invention relates to a method for processing chemically modified fibril cellulose. The method includes introducing chemically modified fibril cellulose material to a thermal drying device including a belt in such a way that the fibril cellulose material forms at least one bar onto the belt, and dewatering the chemically modified fibril cellulose material on the belt using heated air flow having a temperature of at least 40 ° C. in order to concentrate and/or dry the chemically modified fibril cellulose material in such a way that the dry solids content of the fibril cellulose material after the thermal drying device is at least 10%. In addition, this invention relates to a thermal drying device, a system for processing chemically modified fibril cellulose, a method and a system for redispersing the fibril cellulose, and a fibril cellulose material.

Abstract translation: 本发明涉及一种加工化学改性的原纤维纤维素的方法。 该方法包括将化学改性的原纤维素材料引入包括带的热干燥装置中，使得原纤维纤维素材料在带上形成至少一个条，并使用加热的空气流使带上的化学改性的原纤维素材料脱水 具有至少40℃的温度以浓缩和/或干燥化学改性的原纤维纤维素材料，使得热干燥装置之后的原纤维纤维素材料的干固体含量至少为10％。 此外，本发明涉及热干燥装置，用于加工化学改性的原纤维纤维的系统，用于再分散原纤维素的方法和系统，以及原纤维纤维素材料。

公开(公告)号：US20150308429A1

公开(公告)日：2015-10-29

申请号：US14647584

申请日：2013-12-04

Applicant: UPM-KYMMENE CORPORATION

Inventor： Juha Tamper ,  Isko Kajanto ,  Maria Alajaaski ,  Taisto Tienvieri ,  Markus Nuopponen

IPC: F04C13/00 ,  F04C2/107 ,  B67D7/02

CPC classification number: F04C13/001 ,  B67D7/0277 ,  F04C2/107 ,  F04C2/1071 ,  F04C13/002 ,  F04C2210/44

Abstract: In a method for transporting nanofibrillar cellulose in the form of viscous liquid dispersion, the nanofibrillar cellulose is unloaded from a container (3) through a discharge point (3b) which is the lowermost point with respect to the volume of nanofibrillar cellulose in the container at least at the time of unloading. The nanofibrillar cellulose is unloaded and transported to a target location along a pipe (2) using a progressive cavity pump (P2) operating on a positive displacement principle with the suction side of the pump at a distance from the discharge point (3b). The discharge of the nanofibrillar cellulose is ensured by selecting the distance (L) of the suction side of the pump (P2) from the discharge point (3b) so short that the nanofibrillar cellulose flows from the container (3) by the effect of the pump suction, or pressurizing the nanofibrillar cellulose in the container (3) to such a pressure (p) that it will flow at the selected distance (L) of the suction side from the discharge point by the common effect of the pressure of the nanofibrillar cellulose and the pump suction.

Abstract translation: 在以粘性液体分散体形式输送纳米纤维素纤维素的方法中，纳米纤维素纤维素从容器（3）通过排放点（3b）卸载，排放点（3b）相对于容器中纳米纤维素纤维素的体积为最低点 至少在卸货时。 纳米纤维素纤维素被卸载并且使用在正位移原理上操作的逐排腔泵（P2）沿着管道（2）输送到目标位置，其中泵的吸入侧距离排放点（3b）一定距离。 纳米纤维素纤维素的排出是通过从排出点（3b）中选择泵（P2）的吸入侧的距离（L）来确保的，使得纳米纤维素纤维素通过 泵抽吸或将容器（3）中的纳米纤维素纤维素加压到这样的压力（p），使得它将在吸入侧的选定距离（L）从排放点以纳米纤维的压力的共同作用流动 纤维素和泵抽吸。