EP2876202A1 - Utilisation de solvants eutectiques profonds dans la production de papier - Google Patents
Utilisation de solvants eutectiques profonds dans la production de papier Download PDFInfo
- Publication number
- EP2876202A1 EP2876202A1 EP13194321.9A EP13194321A EP2876202A1 EP 2876202 A1 EP2876202 A1 EP 2876202A1 EP 13194321 A EP13194321 A EP 13194321A EP 2876202 A1 EP2876202 A1 EP 2876202A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- deep eutectic
- process according
- cellulose
- eutectic solvent
- paper
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
- 239000002904 solvent Substances 0.000 title claims abstract description 49
- 230000005496 eutectics Effects 0.000 title claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 title abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 47
- 230000008569 process Effects 0.000 claims abstract description 46
- 229920002678 cellulose Polymers 0.000 claims description 28
- 239000001913 cellulose Substances 0.000 claims description 28
- 229920005610 lignin Polymers 0.000 claims description 27
- 238000005406 washing Methods 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000000463 material Substances 0.000 claims description 15
- 230000001376 precipitating effect Effects 0.000 claims description 12
- 239000002699 waste material Substances 0.000 claims description 9
- 239000012978 lignocellulosic material Substances 0.000 claims description 8
- 239000000835 fiber Substances 0.000 claims description 7
- 239000002023 wood Substances 0.000 claims description 7
- 238000012545 processing Methods 0.000 claims description 4
- -1 woodchips Substances 0.000 claims description 4
- 239000010893 paper waste Substances 0.000 claims description 3
- 229920000875 Dissolving pulp Polymers 0.000 claims 2
- 239000000123 paper Substances 0.000 description 17
- 229920002488 Hemicellulose Polymers 0.000 description 11
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 10
- 239000000126 substance Substances 0.000 description 9
- 241000196324 Embryophyta Species 0.000 description 8
- 239000007788 liquid Substances 0.000 description 6
- 238000004061 bleaching Methods 0.000 description 4
- 210000002421 cell wall Anatomy 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000004537 pulping Methods 0.000 description 4
- 229920003043 Cellulose fiber Polymers 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 239000000852 hydrogen donor Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 239000002608 ionic liquid Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000002029 lignocellulosic biomass Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000001728 nano-filtration Methods 0.000 description 2
- 235000020912 omnivore Nutrition 0.000 description 2
- 244000054334 omnivore Species 0.000 description 2
- 239000011087 paperboard Substances 0.000 description 2
- 229920001282 polysaccharide Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000011877 solvent mixture Substances 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 208000005156 Dehydration Diseases 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 241000209504 Poaceae Species 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- ORXJMBXYSGGCHG-UHFFFAOYSA-N dimethyl 2-methoxypropanedioate Chemical compound COC(=O)C(OC)C(=O)OC ORXJMBXYSGGCHG-UHFFFAOYSA-N 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 235000015099 wheat brans Nutrition 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/20—Pulping cellulose-containing materials with organic solvents or in solvent environment
Definitions
- the present invention relates to the use of deep eutectic solvents in the production of pulp and/or paper and the treatment of pulp and paper waste and residues.
- DES solvents are an adaption of a natural phenomenon known from plant metabolism. Science has found plants can build cell walls even under water stress (i.e. during periods of drought or frost). With the help of the organics present in their cells, plants produce so-called deep eutectic solvents. These represent a completely new generation of natural solvents that can dissolve components under mild conditions. DES technology is available at labscale[1].
- DES enables the biobased economy to become reality.
- This application may allow an economical operation of production facilities as small as 50 ktpa, perfectly meeting the increasing demand for production units based on local or regional resources and serving local and regional markets - drastically reducing transport emissions and costs.
- DES also called Low Transition Temperature Mixtures or LTTM
- LTTM Low Transition Temperature Mixtures
- DES are designer solvents, typically consisting of mixtures of at least two substances (at least 1 hydrogen donor and at least 1 hydrogen acceptor) that melt at a lower temperature than either of the individual components. This property is a consequence of hydrogen interaction between the components.
- DES are nonvolatile, biodegradable and do not react with water.
- DES are composed of non-toxic and relatively inexpensive substances including amides, sugars, and alcohols.
- the present invention provides in a first aspect a process for producing pulp and/or paper comprising using deep eutectic solvents.
- a process for producing pulp and/or paper comprising a dissolving step to dissolve lignin from a lignocellulosic material by using deep eutectic solvents.
- a process for processing recycled fibres comprising a contacting step of contacting recycled fibres with deep eutectic solvents.
- a process for producing paper comprising a dissolving step to dissolve cellulose from a cellulosic material by using deep eutectic solvents and optionally a precipitating step of precipitating the cellulose obtained in the dissolving step in sheet format.
- a process for recovering cellulose from cellulosic waste material comprising a dissolving step to dissolve cellulose from the waste material by using deep eutectic solvents.
- cellulose is a complex carbohydrate, (C 6 H 10 O 5 ) n , that is composed of glucose units, forms the main constituent of the cell wall in most plants, and is important in the manufacture of numerous products, such as paper, textiles, pharmaceuticals, and explosives. It is crystalline, strong, and resistant to hydrolysis.
- DES refers to deep eutectic solvent.
- a deep eutectic solvent is a type of ionic liquid (a salt in the liquid state) with special properties composed of a mixture which forms a eutectic with a melting point much lower than either of the individual components. While ordinary liquids such as water and gasoline are predominantly made of electrically neutral molecules, ionic liquids are largely made of ions and short-lived ion pairs.
- Furfural is an organic compound derived from a variety of agricultural by-products, including corncobs, oat, wheat bran, and sawdust. Furfural is a heterocyclic aldehyde (OC 4 H 3 CHO).
- hemicellulose is any of several polysaccharides that are more complex than a sugar and less complex than cellulose, present along with cellulose in almost all plant cell walls. While cellulose is crystalline, strong, and resistant to hydrolysis, hemicellulose has a random, amorphous structure with little strength. It is easily hydrolyzed by dilute acid or base as well as myriad hemicellulose.
- ktpa refers to kiloton per annum.
- Ligand is a complex chemical compound most commonly derived from lignocellulosic biomass, and an integral part of the secondary cell walls of plants.
- “Lignocellulose” refers to plant dry matter (biomass), so called lignocellulosic biomass. It is composed of carbohydrate polymers (cellulose, hemicellulose), and an aromatic polymer (lignin).
- Paper refers to a thin material currently produced by pressing together moist fibers, typically cellulose pulp derived from wood, rags or grasses, and drying them into sheets.
- moist fibers typically cellulose pulp derived from wood, rags or grasses
- PRODCOM 48 PRODCOM 48.
- Pulps is a processing of wood, wood chips or other lignocellulosic materials (containing agricultural or agro-industrial side streams) and the like to isolate individual fibres. Pulps produced thereby can often be further subjected to bleaching and purification operations in a bleach plant, including further delignification of the pulp.
- a definition may be found in NACE, chapter 17 (Manufacture of paper and paper products, Statistical classification of economic activities in the European Community, chapter 17.1 Manufacture of pulp) and PRODCOM 47.
- lignocellulosic material is any material that comprises, consists of, includes, contains or encompasses lignocellulose.
- a "cellulosic material” is any material that comprises, consists of, includes, contains or encompasses cellulose.
- the invention provides in a first aspect a process for producing pulp and/or paper comprising using a deep eutectic solvent.
- the invention provides in a second aspect a process for producing pulp and/or paper comprising a dissolving step to dissolve lignin from a lignocellulosic material by using a deep eutectic solvent. Therewith, a lignin containing deep eutectic solvent and a remaining material is obtained.
- the lignocellulosic material is selected from wood, woodchips, fibre crops, paper, board, waste paper or any combination thereof.
- the dissolving step is typically carried out at a temperature between 40 to 120°C, preferably 40 to 100°C and more preferably between 60 to 80°C.
- the dissolving step is typically carried out for 10 to 120 min, preferably 20 to 60 min and more preferably for 30 to 40 min.
- the process may further comprise a separating step of separating the lignin containing deep eutectic solvent after the dissolving step from the remaining material, which typically contains or consists of cellulose.
- the process may further comprise a washing step of washing the remaining material with a washing solvent, wherein the washing solvent preferably comprises or is preferably water, after the separating step.
- the washing solvent preferably comprises or is preferably water
- the deep eutectic solvent is removed from the remaining material, which typically comprises or consists of cellulose.
- the process may further comprise a precipitating step of precipitating the lignin from the lignin containing deep eutectic solvent after the separating step by a solvent; preferably using water, preferably using the water that has been used as a washing solvent in the washing step and is obtained after said washing step.
- a solvent preferably using water, preferably using the water that has been used as a washing solvent in the washing step and is obtained after said washing step.
- the ratio of deep eutectic solvent to water is between 3:1 to 1: 3, more preferably 2:1 to 1: 2, and most preferably 1:1.
- the separating step may be done in parallel, before or after the washing step.
- the process may further comprise a removing step of removing the lignin from the remaining washing solvent/deep eutectic solvent mixture after the precipitating step, preferably by a solid/liquid separation. Typically, 98% of the lignin is recovered.
- the remaining washing solvent/deep eutectic solvent mixture may contain hemicellulose. Therefore, the process may further comprise a converting step of converting the hemicellulose into other chemicals, preferably furfural.
- the process may further comprise a recovering step of recovering the used deep eutectic solvent, preferably after the converting step of converting the hemicellulose into other chemicals and optionally removing of said other chemicals.
- the deep eutectic solvent is recovered by nano-filtration.
- this process may allow recovering lignin, cellulose and hemicellulose at low temperature and atmospheric pressure, from any lignocellulosic resource. It has shown to be possible with wood as well as with straw (where silica is removed with the DES). By adjusting DES properties and the process lay-out, tailor-made fibre qualities can be obtained (e.g. with different lignin-content).
- a process for processing recycled fibres comprising a contacting step of contacting recycled fibres with a deep eutectic solvent.
- a deep eutectic solvent is used that selectively, or almost selectively, dissolves ink-components and preferably other contaminants from recycled fibres or paper, yielding clean cellulose fibres without fibre losses.
- a process for producing paper comprising a dissolving step to dissolve cellulose from a cellulosic material by using a deep eutectic solvent and optionally a precipitating step of precipitating the cellulose obtained in the dissolving step in sheet format.
- This process may have the advantage that water may be eliminated from the papermaking process.
- a process for recovering cellulose from cellulosic waste material comprising a dissolving step to dissolve cellulose from the cellulosic waste material by using a deep eutectic solvent.
- the cellulose waste material is preferably selected from papermaking residues, and is in particular selected from papermaking rejects or papermaking sludges.
- the dissolving step is typically carried out at a temperature of 40 to 120°C, preferably 40 to 100°C and more preferably 60 to 80°C.
- Cellulose solubility in a DES should allow recovering pure cellulose from papermaking residues (rejects, sludges) in the form of clean dissolved pulp or as a basic building block for biochemicals, materials or fuels. This could very well be applied in the treatment of tissue waste after use, closing the loop in this value chain as well.
Landscapes
- Paper (AREA)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP13194321.9A EP2876202A1 (fr) | 2013-11-25 | 2013-11-25 | Utilisation de solvants eutectiques profonds dans la production de papier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP13194321.9A EP2876202A1 (fr) | 2013-11-25 | 2013-11-25 | Utilisation de solvants eutectiques profonds dans la production de papier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP2876202A1 true EP2876202A1 (fr) | 2015-05-27 |
Family
ID=49639782
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP13194321.9A Ceased EP2876202A1 (fr) | 2013-11-25 | 2013-11-25 | Utilisation de solvants eutectiques profonds dans la production de papier |
Country Status (1)
| Country | Link |
|---|---|
| EP (1) | EP2876202A1 (fr) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017032926A3 (fr) * | 2015-08-27 | 2017-04-13 | Teknologian Tutkimuskeskus Vtt Oy | Procédé de conversion de biomasse |
| CN107200851A (zh) * | 2017-07-17 | 2017-09-26 | 陕西科技大学 | 一种低共熔溶剂制备纳米木质素的方法 |
| DE102016205954A1 (de) * | 2016-04-28 | 2017-11-02 | Duale Hochschule Baden-Württemberg -Körperschaft Des Öffentlichen Rechts- | Verfahren und Anlage zum Herstellen eines flächigen imprägnierten Faserstoffproduktes |
| CN108797115A (zh) * | 2018-06-21 | 2018-11-13 | 东华大学 | 一种基于低共熔溶剂的织物多功能耐久后整理方法 |
| WO2020229732A1 (fr) * | 2019-05-15 | 2020-11-19 | Lappeenrannan-Lahden Teknillinen Yliopisto Lut | Procédé de fractionnement d'une matière lignocellulosique et produits obtenus selon ledit procédé |
| WO2020234761A1 (fr) * | 2019-05-23 | 2020-11-26 | Politecnico Di Milano | Procédé de traitement de biomasse |
| WO2022013482A1 (fr) * | 2020-07-17 | 2022-01-20 | Lappeenrannan-Lahden Teknillinen Yliopisto | Procédé de séparation d'au moins une fraction de polymère à partir d'un matériau comprenant des textiles, ainsi que des fractions de polymère spécifiques et leurs utilisations |
| CN114086414A (zh) * | 2021-10-26 | 2022-02-25 | 华南理工大学 | 一种基于酸性低共熔溶剂的木质纤维素制浆方法 |
| CN114855487A (zh) * | 2022-06-08 | 2022-08-05 | 陕西科技大学 | 一种采用酸性低共熔溶剂提升溶解浆反应性能的方法 |
| WO2022170373A1 (fr) | 2021-02-12 | 2022-08-18 | Mondi Ag | Procédé de pulpage mécanique assisté chimiquement de copeaux de bois ou de chutes de bois |
| CN116023819A (zh) * | 2022-11-21 | 2023-04-28 | 青岛科技大学 | 一种具有天然花香的3d打印墨水及其制备方法与应用 |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8022014B2 (en) | 2008-03-26 | 2011-09-20 | Shrieve Chemical Products, Inc. | Deep eutectic solvents and applications |
| WO2013153203A1 (fr) * | 2012-04-12 | 2013-10-17 | Technische Universiteit Eindhoven | Prétraitement de biomasse lignocellulosique et récupération de substituants au moyen de mélanges naturels de solvants eutectiques profonds (des)/composés présentant des températures de transition basses |
-
2013
- 2013-11-25 EP EP13194321.9A patent/EP2876202A1/fr not_active Ceased
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8022014B2 (en) | 2008-03-26 | 2011-09-20 | Shrieve Chemical Products, Inc. | Deep eutectic solvents and applications |
| WO2013153203A1 (fr) * | 2012-04-12 | 2013-10-17 | Technische Universiteit Eindhoven | Prétraitement de biomasse lignocellulosique et récupération de substituants au moyen de mélanges naturels de solvants eutectiques profonds (des)/composés présentant des températures de transition basses |
Non-Patent Citations (4)
| Title |
|---|
| "Tracking industrial energy efficiency and C02 emissions", IEA, IN SUPPORT OF THE G8 ACTION PLAN, 2007 |
| J. MICHELS, DIE LIGNOCELLULOSE BIORAFFINERIE - VON DER IDEE ZUR REALISIERUNG, 25 January 2013 (2013-01-25) |
| M. FRANCISCO; A. VAN DEN BRUINHORST; MAAIKE C. KROON: "Low-Transition-Temperature Mixtures (LTTMs): A new generation of designer solvents", ANGEW. CHEM. INT. ED, vol. 52, 2013, pages 3074 - 3085 |
| M. FRANCISCO; A. VAN DEN BRUINHORST; MAAIKE C. KROON: "New natural and renewable low transition temperature mixtures (LTTMs): screening as solvents for lignocellulosic biomass processing", GREEN CHEM., vol. 14, 2012, pages 2153 - 2157 |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017032926A3 (fr) * | 2015-08-27 | 2017-04-13 | Teknologian Tutkimuskeskus Vtt Oy | Procédé de conversion de biomasse |
| DE102016205954A1 (de) * | 2016-04-28 | 2017-11-02 | Duale Hochschule Baden-Württemberg -Körperschaft Des Öffentlichen Rechts- | Verfahren und Anlage zum Herstellen eines flächigen imprägnierten Faserstoffproduktes |
| CN107200851A (zh) * | 2017-07-17 | 2017-09-26 | 陕西科技大学 | 一种低共熔溶剂制备纳米木质素的方法 |
| CN108797115A (zh) * | 2018-06-21 | 2018-11-13 | 东华大学 | 一种基于低共熔溶剂的织物多功能耐久后整理方法 |
| CN108797115B (zh) * | 2018-06-21 | 2020-08-04 | 东华大学 | 一种基于低共熔溶剂的织物多功能耐久后整理方法 |
| WO2020229732A1 (fr) * | 2019-05-15 | 2020-11-19 | Lappeenrannan-Lahden Teknillinen Yliopisto Lut | Procédé de fractionnement d'une matière lignocellulosique et produits obtenus selon ledit procédé |
| WO2020234761A1 (fr) * | 2019-05-23 | 2020-11-26 | Politecnico Di Milano | Procédé de traitement de biomasse |
| US20220213276A1 (en) * | 2019-05-23 | 2022-07-07 | Politecnico Di Milano | Processes for biomass treatments |
| WO2022013482A1 (fr) * | 2020-07-17 | 2022-01-20 | Lappeenrannan-Lahden Teknillinen Yliopisto | Procédé de séparation d'au moins une fraction de polymère à partir d'un matériau comprenant des textiles, ainsi que des fractions de polymère spécifiques et leurs utilisations |
| WO2022170373A1 (fr) | 2021-02-12 | 2022-08-18 | Mondi Ag | Procédé de pulpage mécanique assisté chimiquement de copeaux de bois ou de chutes de bois |
| CN114086414A (zh) * | 2021-10-26 | 2022-02-25 | 华南理工大学 | 一种基于酸性低共熔溶剂的木质纤维素制浆方法 |
| CN114855487A (zh) * | 2022-06-08 | 2022-08-05 | 陕西科技大学 | 一种采用酸性低共熔溶剂提升溶解浆反应性能的方法 |
| CN116023819A (zh) * | 2022-11-21 | 2023-04-28 | 青岛科技大学 | 一种具有天然花香的3d打印墨水及其制备方法与应用 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP2876202A1 (fr) | Utilisation de solvants eutectiques profonds dans la production de papier | |
| Rieland et al. | Ionic liquids: A milestone on the pathway to greener recycling of cellulose from biomass | |
| US20250059709A1 (en) | Nanocellulose-reinforced corrugated medium | |
| Sun et al. | One-pot integrated biofuel production using low-cost biocompatible protic ionic liquids | |
| Andrade et al. | Dissolving pulp production from sugar cane bagasse | |
| Rocha et al. | Mass balance of pilot-scale pretreatment of sugarcane bagasse by steam explosion followed by alkaline delignification | |
| Garcia et al. | Search for optimum conditions of wheat straw hemicelluloses cold alkaline extraction process | |
| Rosales‐Calderon et al. | Economic assessment of the conversion of bleached eucalyptus Kraft pulp into cellulose nanocrystals in a stand‐alone facility via acid and enzymatic hydrolysis | |
| CN102803352B (zh) | 用于生物产品的生物质分级方法 | |
| Hou et al. | Facile and simple pretreatment of sugar cane bagasse without size reduction using renewable ionic liquids–water mixtures | |
| CN104532641B (zh) | 植物纤维的节能、环保、资源化制浆方法 | |
| US10266610B2 (en) | Method of processing and fractionating biomass and use of fractions thus obtained | |
| Shatalov et al. | High-grade sulfur-free cellulose fibers by pre-hydrolysis and ethanol-alkali delignification of giant reed (Arundo donax L.) stems | |
| US7585387B2 (en) | Chemical oxidation for cellulose separation with a hypochlorite and peroxide mixture | |
| WO2016022172A1 (fr) | Procédé d'isolement de cellulose à partir d'une biomasse et des produits obtenus à partir de celui-ci | |
| CN107881842B (zh) | 一种利用秸秆和废纸浆制备高强度瓦楞原纸的方法 | |
| Jahan et al. | Fractionation of rice straw for producing dissolving pulp in biorefinery concept | |
| CN101555667B (zh) | 一种木质纤维原料的生物炼制方法 | |
| EP3337925A2 (fr) | Procédé de production de cellulose présentant de faibles impuretés à partir de bagasse de canne à sucre | |
| JP2006238728A (ja) | 製紙排水からの糖類の製造方法 | |
| Popy et al. | Mild potassium hydroxide pulping of straw | |
| CN109826044A (zh) | 棉杆中纤维素、半纤维素、木质素的分离方法 | |
| CA2717995C (fr) | Procede de fabrication de bioethanol a partir de biomasse lignocellulosique | |
| CN103031762A (zh) | 一种在可降解型离子液体溶剂中制备富含纤维素材料的方法 | |
| Arce et al. | Use of green solvents as pre-treatment of dissolving pulp to decrease CS2 consumption from viscose production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| 17P | Request for examination filed |
Effective date: 20131125 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
| AX | Request for extension of the european patent |
Extension state: BA ME |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN REFUSED |
|
| 18R | Application refused |
Effective date: 20150615 |