METHOD FOR IMPROVING QUALITY AND REACTIVITY OF CELLULOSE

Abstract

The invention relates to the technology for the production of celluloses having improved properties and increased reactivity, and can be used in their chemical processing, including finished batches for the production of nitrocellulose and other products. A method for improving the quality and reactivity of cellulose comprises the following steps: impregnating and hydrolyzing the cellulose in a hydrolysis solution, filtering it from the hydrolysis solution, washing it with squeezing and drying. Moreover, the stages of impregnation and hydrolysis of cellulose in hydrolysis solution, filtration from hydrolysis solution, washing, squeezing and drying are carried out with simultaneous thermovacuum-impulse action by cycles, each of which includes the heating of cellulose to a temperature of not more than 115 C., high-speed impulse action of vacuum for time of less than 10 seconds, followed by exposure of the cellulose under vacuum and vacuum relief. The method allows improving the quality of cellulose, including its reactivity.

Claims

1. A method for improving quality and reactivity of a cellulose by its activating wherein an activation of the cellulose involves the following steps to affect the cellulose: impregnating and hydrolysis of the cellulose in a hydrolysis solution, filtering the cellulose from the hydrolysis solution, washing, squeezing and drying at that the steps of impregnating and hydrolysis of the cellulose in the hydrolysis solution, filtration from hydrolysis solution, washing, squeezing and drying are performed with a simultaneous thermovacuum-pulse action by cycles, each of which involves heating the cellulose to the temperature of not more than 115 C., a high-speed impulse action of vacuum within a pressure range of not more than 100 mm Hg for a time of less than 10 seconds, followed by exposure the cellulose to vacuum and vacuum relief.

2. The method of claim 1, wherein the impregnation of a celluloses material supplied from a pulp mill is carried out after its clearing from a wrapping material, followed by the separation of fibers in the hydrolysis solution during the impregnation and hydrolysis of the cellulose.

3. The method of claim 1, wherein prior to impregnation and hydrolysis of the cellulose in the hydrolysis solution, it is pre-dried to a moisture content of not more than 12%.

4. The method of claim 1, wherein high-speed impulse action of vacuum is produced from a receiver with a high-speed valve.

Description

[0017] The object of the invention is achieved in that in the method for improving the quality and reactivity of cellulose by its activating, according to the invention, the activation of cellulose involves the following steps for affecting cellulose: impregnating and hydrolysis of cellulose in a hydrolysis solution, filtering the cellulose from the hydrolysis solution, washing, drying, at that, the steps of impregnating and hydrolysis the cellulose in a hydrolysis solution, filtration from hydrolysis solution, washing, squeezing and drying are performed with a simultaneous thermovacuum-pulse action by cycles, each of which involves heating the cellulose to a temperature of not more than 115 C., a high-speed impulse action of the vacuum within a pressure range of not more than 100 mm Hg for a time of less than 10 seconds, followed by exposure the cellulose to vacuum and vacuum relief.

[0018] Activation of the cellulosic material supplied from the pulp mill is carried out after its release from the wrapping material, followed by the separation of fibers in the hydrolysis solution during the impregnation and hydrolysis process.

[0019] If necessary, prior to the impregnation and hydrolysis of the cellulose in the hydrolysis solution, the pre-drying cellulose to a moisture content of not more than 12% is carried out.

[0020] High-speed impulse action of vacuum can be produced from a receiver with a high-speed valve. The receiver, in turn, must be connected to a vacuum source (vacuum pump).

[0021] The set goal is reached due to the fact that the stages of activation of cellulose (impregnation, hydrolysis, filtration, washing, filtration, and drying) are carried out using thermovacuum-impulse actions in the indicated modes. At impulse vacuuming of heated cellulose, the sorbed gases are removed from the surface of cellulose and its capillaries, and at the impregnating of cellulose with a hydrolysis solution, the wettability of cellulose increases and the degree of impregnation increases over the volume of the cellulose. This makes it possible also to impregnate the finished cellulose when it enters the plant after its release from the wrapping material. In addition, by means of the thermovacuum-impulse action, the moisture content of the material less than 12% is achieved, and the cellulose capillaries are not closed.

[0022] Thus, a such state of material is achieved, in which both a general weakening of the intermolecular interaction and a large internal surface with the presence of the finest capillaries that promote greater accessibility for the subsequent technological process take place.

[0023] Correspondingly, with the hydrolysis solution under intense boiling in vacuum, more complete dissolution of lignin, pectin, resins and other compounds contained in cellulose, in which the content of -cellulose increases, thereby releasing the ultramicroscopic spaces between the crystalline areas and increasing its reactivity is achieved.

[0024] In addition, the exclusion of processes for purification of cellulose against additional organic compounds and vacuum-impulse action accelerate the activation process.

[0025] The proposed method for activating cellulose can be implemented either in the pulp mill at the end of the process or before the subsequent use of the finished cellulose.

[0026] The method of activation of the finished cellulose is carried out as follows.

[0027] After unpacking, finished cellulosic material is placed in a cooker (hydrolyzer) and subjected to successive processing steps: drying to a moisture content of not more than 12% (if necessary), impregnation and hydrolysis in a hydrolysis solution, filtration of cellulose from the hydrolysis solution, washing of cellulose after hydrolysis, and subsequent pressing and drying. Moreover, these technological processes of impregnation and hydrolysis of cellulose in hydrolysis solution, filtration of cellulose from hydrolysis solution, washing after hydrolysis, squeezing and drying are carried out with simultaneous application of thermovacuum-impulse actions by cycles including the heating of cellulose to a temperature of not more than 115 C., high-speed impulse vacuuming the cooker with the cellulose in it, for a time of less than 10 seconds to a pressure of not more than 100 mm Hg; with exposure and degassing of cellulose under vacuum for 1-3 minutes, then a vacuum is discharged in the apparatus containing the cellulose by a heat air medium heated to 100-150 C.

[0028] The high-speed impulse action of vacuum is carried out from a vacuum sourcea vacuum receiver through a high-speed valve. A vacuum pump connected to the receiver provides vacuum.

[0029] Examples of quality and reactivity control of finished cellulose after activation by the claimed method:

[0030] To improve the quality of finished batches of celluloses manufactured at the appropriate plants, improving their quality and reactivity with the use of hydrolysis solutions in the thermovacuum-impulse mode, celluloses were taken from the finished batches of cellulose: cotton (CC), wood (WC), sheet cellulose (SC) of CA-grade, and flax sheet cellulose (FSC).

[0031] Technical parameters of celluloses of finished batches before and after activation by the claimed method are given in the table.

TABLE-US-00001 WC WC sulphate sulphate CC CA - grade FSC CC CA -grade FSC Parameters parameters before activation parameters after activation Content 96.0-97.2 95.6-96.5 92.8-95.7 97.5-98.7-99.1 96.8-98.6 94.5-97.7 -cellulose, %, not less than Wettability, g, not 130-135 130-135 105-130 147-150 135-138 135-140 less than Viscosity, mPa s 20-30 20-21 21-25 7.0-8.3 5.6-7.4 8.0-10.0 Lignin content, %, 0.3-0.4 0.1-0.38 0.1 not more than Resin and fats 0.07-0.5 0.2-0.4 0.1 0.1 content, %, not more than Dust content, %, 2.0 7.0 2.0 0.4 1.2 0.3 not more than Ash content, %, 0.1-0.2 0.15-0.3 0.1-0.3 0.01 0.1 0.15 not more than Humidity, %, not 10 7-12 10 5.0 6.0 8.0 more than Degree of 2500-3500 3300-4300 1000-1400 280 420 320 polymerization

[0032] From the data given, it follows that the treatment of finished batches of celluloses with the claimed method significantly improves the technical parameters of celluloses.