Process for isolating cellulose from cellulosic biomass, isolated cellulose of type i and composite materials comprising same

a cellulosic biomass and isolating technology, applied in the field of biomass delignification and cellulose extraction, can solve the problems of high heat and high pressure in the kraft process for several hours, high pollution of both processes, and general undesirable lignin, etc., and achieves the effects of less water, and less water and gas pollution

Inactive Publication Date: 2015-12-17
VENTIX ENVIRONNEMENT
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  • Abstract
  • Description
  • Claims
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AI Technical Summary

Benefits of technology

[0036]An advantage of the present invention is that it provides relatively simpler, cheaper and more efficient means than all other chemical processes for making cellulose pulp and extracting cellulose from biomass. The processes of the invention can be implemented in variable sizes, such as large industrial facilities or smaller mobile units installed near or on the very sites of wood processing activities. The processes of the invention can be carried out at ambient pressure conditions and do not require external source of energy such as heating, pressurizing or the like. The chemical processes of the invention are likely more environmental friendly because they use less water and they produce less water and gas pollutants than other existing chemical processes. Furthermore, the cellulose that is obtained from these processes possess advantages in terms of purity (i.e. less lignin and less hemicelluloses), cell integrity, reactivity and abundance, than typical commercial type I and type II celluloses.
[0037]Additional aspects, advantages and features of the present invention will become more apparent upon reading of the following non-restrictive description of preferred embodiments which are exemplary and should not be interpreted as limiting the scope of the invention.

Problems solved by technology

Lignin is generally undesirable because of its adverse effect on paper, in particular as regards to its resistance and yellowing over time.
The Kraft process requires high heat and high pressure for several hours.
Both processes are highly polluting despite efforts since the 1930's to recover the chemical products used therein.
Chemical processes further require massive industrial facilities and huge investments to build and operate since these known processes require large amounts of energy and water and they must also deal with air and water pollutants.
All of these processes require however expensive equipment because of their use of high temperatures (between 95° C. and 270° C.) and pressure (between 3 and 40 bars).
In addition, these processes do not handle large volumes of material for industrial production, precisely because of the high cost of their facilities.
Although the method provides some advantages over the Kraft process, it still presents some disadvantages, including the need for thermal energy and the use of high pressure and the low yield of pure cellulose.

Method used

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  • Process for isolating cellulose from cellulosic biomass, isolated cellulose of type i and composite materials comprising same
  • Process for isolating cellulose from cellulosic biomass, isolated cellulose of type i and composite materials comprising same
  • Process for isolating cellulose from cellulosic biomass, isolated cellulose of type i and composite materials comprising same

Examples

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examples

[0191]In the following examples, these abbreviations are used:[0192]MXG Mannose, Xylose, Galactose[0193]HMF Hydroxymethylfurfural[0194]HmO Hemicelluloses derivatives and other products[0195]ASL Acid Soluble Lignin[0196]AIL Acid Insoluble Lignin[0197]LI1 2-Aminoethanol[0198]LI2 2,2′-Iminodiethanol[0199]Cel Cellulose[0200]Lig Lignin

examples 1 to 5

Cellulose Extraction from Woody Biomass

[0201]Experimental parameters in all the following examples are described in Table 2 below.

TABLE 2Experimental parameters and resultsExample 1(Control)Example 2Example 3Example 4Example 5NameReferenceLl1 - NO3Ll2 - NO3Ll1 - ClLl2 - NO3(woodchipswithout useof theprocess)Biomass100 g of100 g of100 g of100 g of150 g ofwashedwashedwashedwashedwashedmaplemaplemaplemaplewhite birchwoodchipswoodchipswoodchipswoodchipswoodchipsGradingBetween 20Between 9Between 9Between 20and 80 meshand 20and 20and 80meshmeshmeshCompoundnoneNitric acidNitric acidHydrochloricNitric acidA(H+NO3−)(H+NO3−)acid (H+Cl−)(H+NO3−)200 g200 g200 g200 mlIncubation30 min30 min45 min12 mintime with ACompoundnoneLl1Ll2Ll1Ll2B100 g80 g100 g100 mlIncubation30 min30 min30 min10 mintime with BFinal solidRaw40 g40 g95 g70 gproductwoodchipsCel: 82.5%;Cel: 84.4%;Cel: 57.2%;Cel:(unchanged)Lig: 0.6%;Lig: 1.3%;Lig: 23.9%;1005%HmO:HmO:HmO:16.9%14.2%18.9%

[0202]For each example, the biomass was fi...

example 5

[0209]200 g of white birch wood chips (Betula papyrifera var. papyrifera) were washed with 750 ml of tap water and heated in a microwave oven (max. setting) three times 5 minutes. After a fourth washing with 750 ml of distilled water, the chips were dried at room temperature for 3 days. The chips were then ground to pass through a 10 mesh sieve and left to macerate for an extra 5 to 6 days in two times 1000 ml of distilled ethanol. The washed biomass was again dried at room temperature for 1 more day. The chips were then finely ground and screened to pass through a 18 mesh sieve.

[0210]150 g of washed birch sawdust was put in a well-mixed open batch reactor made of HDPE, displaced under a fume hood. The reactor was settled semi-inclined on a platform, equipped with a bidirectional motor shaft for lateral rotation; 200 ml of concentrated nitric acid (≈70%) was poured on the biomass. The solution was mixed during 12 minutes, allowing some time for impregnation without mixing (≈3 minute...

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Abstract

Described herein are processes for the production of a cellulose pulp and processes for isolating cellulose from cellulose-containing biomass. The processes of the invention comprises contacting the biomass with a source of anions and a source of cations, the source of anions and the source of cations being selected to react exothermically with the biomass and with each other. The processes of the invention have the particularity of generating exothermic reactions through enthalpies of reaction and mixture. Accordingly, the processes of the invention do not require any supply of external energy since the required energy is provided by chemical reagents that are already present in the biomass or added as needed. The invention also relates to isolated cellulose obtained from these processes and the use of same in various materials.

Description

RELATED APPLICATION[0001]The present application claims priority to Canadian patent application No. 2,803,863 filed Jan. 25, 2013, the content of which is incorporated herein by reference in its entirety.FIELD OF THE INVENTION[0002]The present invention relates to the field of biomass delignification and cellulose extraction. More particularly, the invention relates to processes for the production of a cellulose pulp and processes for isolating cellulose from cellulose-containing biomass. The invention further relates to isolated cellulose obtained from these processes and to the use of same in various materials.BACKGROUND OF THE INVENTION[0003]Plant biomass is primarily composed of cellulose (˜50%), lignin (˜25%) and hemicelluloses (˜25%).[0004]Although cellulose was first extracted using mechanical processes, nowadays cellulose is mostly obtained by chemical extraction processes, that were first developed on an industrial scale in Europe in 1850's. Those chemical processes general...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): D21C3/00D21C9/00D21C9/10D21C3/16D21C9/02
CPCD21C3/003D21C3/16D21C9/007D21C9/10D21C9/02D21C11/0007C08H8/00
Inventor ESSADDAM, HATEM
Owner VENTIX ENVIRONNEMENT
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