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Fluff pulp

A fluff pulp and range technology, applied in the field of fluff pulp, can solve the problem of less resources

Pending Publication Date: 2022-04-08
STORA ENSO OYJ
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Considering the production costs, resource requirements and environmental impact of bleaching, it is desirable to be able to achieve sufficient fluff pulp properties (especially sufficient absorption) but using fewer resources

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] Collected from the production scale pulp digester immediately after (“unbleached”), after the subsequent oxygen delignification step (“oxygen delignified”) and after the bleaching step (“bleached”) Kraft pulp samples. Thus, the "bleached" samples have been subjected to both oxygen delignification and bleaching.

[0039] Each slurry sample was rinsed thoroughly with water, centrifuged, pelleted and stored in a refrigerator prior to analysis.

[0040] Laboratory sheets are formed from various types of pulp. The laboratory sheets were defibrated using a laboratory hammer mill (Kamas H01).

[0041] Tested for chemicals and fluff properties according to standard test methods. The results obtained are illustrated in Table 1. Kappa values ​​are measured on the formed dry sheet. ISO brightness is measured on the formed dry sheet. Specific volume, absorption time and absorption capacity are measured on the fluffed material (ie after defibration). Sheet and pulp properties w...

Embodiment 2

[0046] Kraft pulp samples were collected immediately after the subsequent oxygen delignification step at production scale ("oxygen delignified") and after the bleaching step ("bleached"). Thus, the "bleached" samples have been subjected to both oxygen delignification and bleaching.

[0047] Subsequently, the pulp was centrifuged, pelletized and stored in dark plastic bags at 25 to 30% dry content in the refrigerator. The slurry for a sheet is soaked and wet disintegrated. The slurry suspension pH was adjusted to 5.8, agitated for 10 minutes, and then dewatered in a sheet former. Al 2 (SO 4 ) 3 The solution was treated and its pH was then adjusted to 5.8 with NaOH.

[0048] The wet sheet was pressed and dried to a moisture content of <7%.

[0049] Tested for chemicals and fluff properties according to standard test methods. The results obtained are illustrated in Table 1. Kappa values ​​are measured on the formed dry sheet. ISO brightness is measured on the formed dry ...

Embodiment 3

[0054] Production trials were carried out on a kraft fiber line with a dryer for fluff pulp. The kraft pulp was oxygen delignified and either bleached or unbleached. The pulp has a Kappa value between 8 and 11 measured on-line after oxygen delignification. A bleached control fluff pulp was produced on the same fiber line, but this pulp was bleached to a Kappa value of 1 in the bleaching plant.

[0055] At the drying machine, the slurry of test point 2 and test point 3 was treated with Al 2 (SO 4 ) 3 Treated and pH adjusted with NaOH.

[0056] Fluff properties were tested according to standard test methods. The results obtained are illustrated in Table 1. ISO brightness is measured on fluff pulp. Nodule content, specific volume, absorption time and absorbent capacity are measured on the fluffed material (ie after defibration). Sheet and pulp properties were evaluated according to ISO 187 in a controlled environment.

[0057] Table 3. Chemical and Fluff Properties

[0...

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Abstract

The invention relates to a fluff pulp having a Kappa value in the range of 5 to 18, and having an ISO brightness in the range of 30 to 60% when in the form of a dry sheet, and having a specific volume in the dry defibrated state of at least 19 dm3 / kg, and an absorption time in the range of 2 to 4 seconds.

Description

technical field [0001] The present invention relates to a fluff pulp having a Kappa value in the range of 5 to 18, and an ISO brightness in the range of 30 to 60% when in the form of a dry sheet, and having at least 19 dm 3 / kg specific volume in dry defibrated (defibrated) state and have an absorption time in the range of 2 to 4 seconds. The invention also relates to a process for producing such fluff pulp and its use. Background technique [0002] Fluff pulp is usually made from softwood pulp from kraft pulping. Depending on the pulping method, the properties of fluff pulp differ. The raw material for softwood pulp can be various softwood species such as Scandinavian pine, spruce, southern pine, loblolly pine, slash pine, Radiata pine, Douglas fir, Hemlock Cedar , white spruce, lodgepolepine, alpine fir, or mixtures thereof. [0003] Bleaching is a common method for removing lignin and color compounds remaining after pulp cooking and thereby increasing the brightness o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): D21C9/147D21C9/10A61F13/15D21H11/00D21H11/04D21H27/00
CPCA61F2013/530007D21C3/02D21C9/007D21H27/002D21H15/04D21H27/42D21C9/147D21C9/005D21H11/04D21C9/10D21H11/00A61F13/15D21H27/00D21H27/004D21H27/005D21H27/007D21H11/16
Inventor H.图夫韦森M.科尼格G.索德斯塔姆A.蒙吉亚-张
Owner STORA ENSO OYJ
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