C08B15/10

POLYMER AND METHOD FOR PRODUCING POLYMER MEMBRANE
20190330383 · 2019-10-31 ·

In order to obtain a crosslinked cellulose without derivatization, a polymer according to an embodiment of the present disclosure is a polymer having a structure in which cellulose substantially represented by the following formula (c1) is crosslinked with a polyfunctional epoxy compound:

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wherein in the formula (c1), n represents an integer of 2 or more.

POLYMER AND METHOD FOR PRODUCING POLYMER MEMBRANE
20190330383 · 2019-10-31 ·

In order to obtain a crosslinked cellulose without derivatization, a polymer according to an embodiment of the present disclosure is a polymer having a structure in which cellulose substantially represented by the following formula (c1) is crosslinked with a polyfunctional epoxy compound:

##STR00001##

wherein in the formula (c1), n represents an integer of 2 or more.

Carrier for ligand immobilization

A carrier for ligand immobilization obtained by shrinking polysaccharide porous beads not less than 10% by a shrinkage rate defined by the following formula, and crosslinking the polysaccharide porous beads: Shrinkage rate (%)=(1V.sub.2/V.sub.1)100 (wherein, V.sub.1 indicates the gel volume of polysaccharide porous beads before shrinkage, and V.sub.2 indicates the gel volume of polysaccharide porous beads after shrinkage).

Carrier for ligand immobilization

A carrier for ligand immobilization obtained by shrinking polysaccharide porous beads not less than 10% by a shrinkage rate defined by the following formula, and crosslinking the polysaccharide porous beads: Shrinkage rate (%)=(1V.sub.2/V.sub.1)100 (wherein, V.sub.1 indicates the gel volume of polysaccharide porous beads before shrinkage, and V.sub.2 indicates the gel volume of polysaccharide porous beads after shrinkage).

NANOCELLULOSE AEROGELS AND FOAMS
20190309144 · 2019-10-10 ·

The present disclosure provides a method for preparing an aerogel or a foam, the method comprising: forming a reaction mixture comprising a cellulose nanofibril gel, a first solvent, and one or more crosslinking agents under conditions sufficient to crosslink the gel; and contacting the crosslinked gel with a second solvent under conditions sufficient to dry the crosslinked gel, thereby forming an aerogel or foam.

Crosslinked cellulose as precursor in production of high-grade cellulose derivatives and related technology
10428459 · 2019-10-01 · ·

A pulp in accordance with a particular embodiment includes crosslinked cellulose fibers. The pulp can have high brightness, reactivity, and intrinsic viscosity. The pulp, therefore, can be well suited for use as a precursor in the production of low-color, high-viscosity cellulose derivatives. A method in accordance with a particular embodiment of the present technology includes forming a pulp from a cellulosic feedstock, bleaching the pulp, crosslinking cellulose fibers within the pulp while the pulp has a high consistency, and drying the pulp. The bleaching process can reduce a lignin content of the pulp to less than or equal to 0.09% by oven-dried weight of the crosslinked cellulose fibers. Crosslinking the cellulose fibers can include exposing the cellulose fibers to a glycidyl ether crosslinker having two or more glycidyl groups and a molecular weight per epoxide within a range from 140 to 175.

Crosslinked cellulose as precursor in production of high-grade cellulose derivatives and related technology
10428459 · 2019-10-01 · ·

A pulp in accordance with a particular embodiment includes crosslinked cellulose fibers. The pulp can have high brightness, reactivity, and intrinsic viscosity. The pulp, therefore, can be well suited for use as a precursor in the production of low-color, high-viscosity cellulose derivatives. A method in accordance with a particular embodiment of the present technology includes forming a pulp from a cellulosic feedstock, bleaching the pulp, crosslinking cellulose fibers within the pulp while the pulp has a high consistency, and drying the pulp. The bleaching process can reduce a lignin content of the pulp to less than or equal to 0.09% by oven-dried weight of the crosslinked cellulose fibers. Crosslinking the cellulose fibers can include exposing the cellulose fibers to a glycidyl ether crosslinker having two or more glycidyl groups and a molecular weight per epoxide within a range from 140 to 175.

CARRIER FOR LIGAND IMMOBILIZATION

A carrier for ligand immobilization obtained by shrinking polysaccharide porous beads not less than 10% by a shrinkage rate defined by the following formula, and crosslinking the polysaccharide porous beads: Shrinkage rate (%)=(1V.sub.2/V.sub.1)100 (wherein, V.sub.1 indicates the gel volume of polysaccharide porous beads before shrinkage, and V.sub.2 indicates the gel volume of polysaccharide porous beads after shrinkage).

CARRIER FOR LIGAND IMMOBILIZATION

A carrier for ligand immobilization obtained by shrinking polysaccharide porous beads not less than 10% by a shrinkage rate defined by the following formula, and crosslinking the polysaccharide porous beads: Shrinkage rate (%)=(1V.sub.2/V.sub.1)100 (wherein, V.sub.1 indicates the gel volume of polysaccharide porous beads before shrinkage, and V.sub.2 indicates the gel volume of polysaccharide porous beads after shrinkage).

Oxygen and water vapour barrier films with low moisture sensitivity fabricated from self-cross-linking fibrillated cellulose
10384424 · 2019-08-20 · ·

There is provided a package material comprising an oxygen barrier polymer film, wherein the film comprises a polymer obtainable by a process comprising the steps of: a) oxidizing cellulose fibers to ultimately obtain cross-linked cellulose; and b) homogenizing the product of step a) to obtain fibrils in a width range of 1 nm to 150 nm. A corresponding use is also provided.