WO2006115310A1 - Process for producing fiber pulp utilizing bamboo and pulp produced using the same - Google Patents
Process for producing fiber pulp utilizing bamboo and pulp produced using the same Download PDFInfo
- Publication number
- WO2006115310A1 WO2006115310A1 PCT/KR2005/001893 KR2005001893W WO2006115310A1 WO 2006115310 A1 WO2006115310 A1 WO 2006115310A1 KR 2005001893 W KR2005001893 W KR 2005001893W WO 2006115310 A1 WO2006115310 A1 WO 2006115310A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pulp
- bamboo
- bleaching
- bamboo chips
- prehydrolysis
- Prior art date
Links
- 235000017166 Bambusa arundinacea Nutrition 0.000 title claims abstract description 124
- 235000017491 Bambusa tulda Nutrition 0.000 title claims abstract description 124
- 235000015334 Phyllostachys viridis Nutrition 0.000 title claims abstract description 124
- 241001330002 Bambuseae Species 0.000 title claims abstract description 121
- 239000011425 bamboo Substances 0.000 title claims abstract description 120
- 239000000835 fiber Substances 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims abstract description 39
- 230000008569 process Effects 0.000 title claims abstract description 23
- 238000004061 bleaching Methods 0.000 claims abstract description 56
- 238000005406 washing Methods 0.000 claims abstract description 17
- 238000005520 cutting process Methods 0.000 claims abstract description 12
- 238000004537 pulping Methods 0.000 claims abstract description 9
- 238000012216 screening Methods 0.000 claims abstract description 5
- 239000000126 substance Substances 0.000 claims description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 239000000356 contaminant Substances 0.000 claims description 24
- 238000004519 manufacturing process Methods 0.000 claims description 23
- 238000010411 cooking Methods 0.000 claims description 15
- 229920002488 Hemicellulose Polymers 0.000 claims description 11
- 229910021645 metal ion Inorganic materials 0.000 claims description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims description 8
- 239000003513 alkali Substances 0.000 claims description 8
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 claims description 8
- 150000004056 anthraquinones Chemical class 0.000 claims description 8
- 239000012634 fragment Substances 0.000 claims description 7
- 239000012535 impurity Substances 0.000 claims description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 4
- 238000010306 acid treatment Methods 0.000 claims description 4
- 239000000460 chlorine Substances 0.000 claims description 4
- 229910052801 chlorine Inorganic materials 0.000 claims description 4
- 239000000428 dust Substances 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- 229920000875 Dissolving pulp Polymers 0.000 abstract description 21
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract description 7
- 230000007062 hydrolysis Effects 0.000 abstract description 6
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 6
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 239000013043 chemical agent Substances 0.000 abstract 1
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 28
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 description 14
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 14
- 239000002023 wood Substances 0.000 description 10
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 8
- 239000002994 raw material Substances 0.000 description 7
- 241000196324 Embryophyta Species 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000005431 greenhouse gas Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 241000209128 Bambusa Species 0.000 description 4
- 239000004155 Chlorine dioxide Substances 0.000 description 4
- 239000007844 bleaching agent Substances 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 235000019398 chlorine dioxide Nutrition 0.000 description 4
- 230000006378 damage Effects 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 239000002657 fibrous material Substances 0.000 description 4
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 4
- 238000006116 polymerization reaction Methods 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 229920000297 Rayon Polymers 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002738 chelating agent Substances 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000002964 rayon Substances 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical group [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 229920001131 Pulp (paper) Polymers 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 235000003599 food sweetener Nutrition 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000003765 sweetening agent Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- RZVHIXYEVGDQDX-UHFFFAOYSA-N 9,10-anthraquinone Chemical compound C1=CC=C2C(=O)C3=CC=CC=C3C(=O)C2=C1 RZVHIXYEVGDQDX-UHFFFAOYSA-N 0.000 description 1
- 240000006248 Broussonetia kazinoki Species 0.000 description 1
- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 1
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- 208000010228 Erectile Dysfunction Diseases 0.000 description 1
- 244000299507 Gossypium hirsutum Species 0.000 description 1
- 240000000907 Musa textilis Species 0.000 description 1
- QPCDCPDFJACHGM-UHFFFAOYSA-N N,N-bis{2-[bis(carboxymethyl)amino]ethyl}glycine Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(=O)O)CCN(CC(O)=O)CC(O)=O QPCDCPDFJACHGM-UHFFFAOYSA-N 0.000 description 1
- 229920006328 Styrofoam Polymers 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- TVXBFESIOXBWNM-UHFFFAOYSA-N Xylitol Natural products OCCC(O)C(O)C(O)CCO TVXBFESIOXBWNM-UHFFFAOYSA-N 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000009120 camo Nutrition 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000005607 chanvre indien Nutrition 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000011978 dissolution method Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000005445 natural material Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 230000000243 photosynthetic effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000008261 styrofoam Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 239000000811 xylitol Substances 0.000 description 1
- 235000010447 xylitol Nutrition 0.000 description 1
- HEBKCHPVOIAQTA-SCDXWVJYSA-N xylitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)CO HEBKCHPVOIAQTA-SCDXWVJYSA-N 0.000 description 1
- 229960002675 xylitol Drugs 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
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
-
- E—FIXED CONSTRUCTIONS
- E06—DOORS, WINDOWS, SHUTTERS, OR ROLLER BLINDS IN GENERAL; LADDERS
- E06C—LADDERS
- E06C9/00—Ladders characterised by being permanently attached to fixed structures, e.g. fire escapes
- E06C9/02—Ladders characterised by being permanently attached to fixed structures, e.g. fire escapes rigidly mounted
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62B—DEVICES, APPARATUS OR METHODS FOR LIFE-SAVING
- A62B1/00—Devices for lowering persons from buildings or the like
- A62B1/20—Devices for lowering persons from buildings or the like by making use of sliding-ropes, sliding-poles or chutes, e.g. hoses, pipes, sliding-grooves, sliding-sheets
-
- E—FIXED CONSTRUCTIONS
- E06—DOORS, WINDOWS, SHUTTERS, OR ROLLER BLINDS IN GENERAL; LADDERS
- E06B—FIXED OR MOVABLE CLOSURES FOR OPENINGS IN BUILDINGS, VEHICLES, FENCES OR LIKE ENCLOSURES IN GENERAL, e.g. DOORS, WINDOWS, BLINDS, GATES
- E06B5/00—Doors, windows, or like closures for special purposes; Border constructions therefor
- E06B5/01—Trap-doors
-
- E—FIXED CONSTRUCTIONS
- E06—DOORS, WINDOWS, SHUTTERS, OR ROLLER BLINDS IN GENERAL; LADDERS
- E06C—LADDERS
- E06C7/00—Component parts, supporting parts, or accessories
- E06C7/50—Joints or other connecting parts
- E06C7/505—Anchors being adapted to fix a ladder to a vertical structure, e.g. ladder hooks
-
- 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
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/02—Pretreatment of the finely-divided materials before digesting with water or steam
-
- 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
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/04—Pretreatment of the finely-divided materials before digesting with acid reacting compounds
-
- 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
- D21C3/02—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
-
- 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
- D21C3/22—Other features of pulping processes
- D21C3/222—Use of compounds accelerating the pulping processes
-
- 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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
Definitions
- the present invention relates to a method for producing fiber pulp using bamboos, and more particularly to a method for producing good-quality fiber (dissolving) pulp using bamboos, which comprises longitudinally splitting the bamboo, transversely cutting the split bamboo to short lengths, dissolving hemicellulose from the cut material by prehydrolysis, and bleaching the prehydrolyzed material with a bleaching agent causing low environmental pollution, and thus has a high pulp production yield and does not emit environmental pollutants such as dioxin, as well as pulp produced thereby.
- papermaking and dissolving pulps are recognized to be produced using wood.
- dissolving pulp refers to fiber pulp that can be used later to produce fibers.
- the present invention relates to a method for producing pulp, and more particularly to a method for producing dissolving pulp (i.e., fiber pulp) which can be used later to produce fibers.
- Such non-woody plants include paper mulberry bast fibers, hemps, cottons, and Manila hemps, and Korea Patent Publication Nos. 98-9651 and 93-2604 disclose a method for pulp using rice-straw.
- rayon corresponding to high-grade fiber utilizes dissolving pulp produced from wood as a raw material.
- a tree is a reproducible natural material, but it requires a period of a few years to a few ten years until it reaches a usable level. For this reason, the regulation for the use of wood is tightened and the pressure for the development of an eco-friendly material that can substitute for wood is being actualized.
- a bamboo which receives attention and is used as a raw material in the present invention, is produced in large amounts in Southeast Asia countries such as China and Srivaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavaszavasza
- this technology has shortcomings in that it does not consider the compact structure of the bamboo, so that the pulping of the bamboo is not satisfactorily achieved, and it consumes large amounts of chemicals and energy, and has low yield because a bleaching process is conducted in strong conditions. In addition, it causes the decomposition and destruction of fiber, making the fiber weak.
- a chlorine bleaching process using elemental chlorine provides the cause of dioxin generation.
- this processing problem acts as the cause of increasing chemical amount, energy consumption and production cost per unit pulp production.
- the present invention has been made to solve the above- described problems occurring in the prior art, and it is an object of the present invention to provide a method for producing good-quality fiber (dissolving) pulp using a bamboo, which comprises longitudinally splitting the bamboo, transversely cutting the split bamboo to short lengths, dissolving hemicellulose from the cut material by prehydrolysis, and bleaching the prehydrolyzed pulp with a bleaching agent causing low environmental pollution, and thus has a high pulp production yield and does not emit environmental pollutants such as dioxin, as well as pulp produced thereby.
- Another object of the present invention is to provide a method for producing dissolving (fiber) fiber using bamboos, which allows the production of pulps having various qualities according to the intended use thereof by applying a technology capable of optionally controlling the degree of polymerization of the fiber pulp, and also can produce byproduct xylose using a method wherein xylose which forms a significant portion of hemicellulose dissolved during a prehydrolysis process is recovered and purified from a solution and cooked waste isolated from the pulp after prehydrolysis, as well as pulp produced thereby.
- the present invention provides a method for producing fiber pulp using a bamboo, comprising: a leaf removal step of removing the leaves of the bamboo; a longitudinal splitting step of longitudinally splitting the bamboo to have a width of 1.5-3 mm; a transverse cutting step of transversely cutting the split bamboo to a length of 10-30 mm to produce bamboo chips; a screening step of filtering out small fragments or impurities from the cut bamboo chips; a washing step of washing the bamboo chips with water to remove impurities, contaminants or dust; a prehydrolysis step of subjecting the washed bamboo chips to prehydrolysis using water or steam, and adding sulfur dioxide or sulfuric acid according to the degree of required prehydrolysis to promote the prehydrolysis so as to dissolve hemicellulose from the bamboo chips; a cooking step of introducing the bamboo chips into a digester, in which the ratio of a chemical liquor consisting of water, alkali and anthraquinone to the weight of the bamboo chips is adjusted to 1:3.5-6.0 (bamboo
- FIG. 1 is a flowchart showing sequentially the steps of a preparation method according to the present invention.
- FIG. 2 shows a general centrifugal cleaner.
- the present invention is similar to the prior art, in that it relates to a method for preparing fiber pulp.
- the present invention is remarkably different from the prior art, in that non-woody plant bamboo is used to produce pulp, the consumption of chemicals and energy is reduced by treating the bamboo in the production of the pulp so as to make prehydrolysis and cooking easy, the generation of hazardous substances such as dioxin which can be generated in a bleaching process is minimized, xylose (also used as the raw material of gum) contained in hemicellulose dissolved during the inventive prehydolysis step can be produced, and thus wood present on the globe needs not to be felled, and the pulp prepared from the bamboo has surprisingly good quality.
- xylose also used as the raw material of gum
- the inventive method for producing fiber (dissolving) pulp comprises a first step (bamboo leaf removal step) of removing the leaf of the bamboo.
- the bamboo leaf contains a large amount of extracts unnecessary to produce pulp, but has a small amount of essential fibrous material.
- the bamboo leaf is of help to prepare pulp, but rather can act as the cause of increasing the consumption of drugs, the bamboo leaf is removed before introduction into a process for producing dissolving pulp.
- the bamboo leaf is not used and only the bamboo stalk is used. Then, a second step (longitudinal splitting step) of longitudinally splitting the bamboo to a width of 1.5-3 mm is conducted.
- the bamboo is first longitudinally split into half, and the split bamboo is additionally split to a narrower width. In this step, the bamboo is preferably split to a width of 1.5-3 mm.
- This longitudinal splitting is a significantly characteristic step of the present invention, and when the bamboo is split at random without considering orientation, fibrous material will not be uniformly split, but rather the fibrous material itself can be broken.
- the bamboo is used after it is longitudinally split several times to have narrow width.
- the split bamboo is transversely cut to a length of 10-30 mm using a cutter.
- a fourth step (screening step) of filtering out small fragments or impurities from the cut bamboo chips is conducted.
- the pulp is in a state in which the fibrous material is broken.
- these small fragments can weaken the strength of the pulp and increase the consumption of chemicals.
- contaminants during the cutting step are not of any help to produce the pulp.
- a fifth step (washing step) of washing the bamboo chips with water to remove impurities, contaminants and dust from the bamboo chips is conducted.
- the contaminant, dust and the like attached to the bamboo chips are removed with water.
- a sixth step is conducted, the washed bamboo chips are subjected to prehydrolysis using water or steam, and sulfur dioxide or sulfuric acid is added to the chips depending on the degree of required prehydrolysis to promote the prehydrolysis so as to dissolve hemicellulose from the bamboo chips.
- This hydrolysis is performed with liquid water or steam using sulfur dioxide or sulfuric acid as a catalyst.
- This prehydrolysis aims to dissolve hemicellulose from the bamboo chips, and thus if an acid is used alone, acid hydrolysis can severely occur to severely destroy cellulose. For this reason, the acid must be controlled to a suitable liquor ratio according to operation circumstances.
- the ratio of the amount of liquid water and catalyst to the amount of the bamboo chips is preferably controlled within the range of 1.5-7 : 1 depending on the degree of required hydrolysis.
- the prehydrolysis is performed in a state in which the ratio of the water-containing liquor to the bamboo chips is 1.5-7:1.
- the desired polymerization degree and the hydrolysis degree of hemicellulose must be controlled using a characteristic in that, as said liquor ratio increases, the hydrolysis smoothly progresses.
- the liquor ratio if the weight of the bamboo chips is 1 on an oven-dry weight basis, volume of the aqueous solution (if chemicals such as catalysts are contained, a state in which the chemicals are dissolved in water) is 1.5-7. Also, the use of said liquor ratio aims to easily bring the bamboo chips into uniform contact with chemicals during the reaction and to control the extent of the reaction by allowing the intensity (concentration) of chemicals in contact with the bamboo chips to vary depending on the liquor ratio.
- the prehydrolysis is preferably conducted at a temperature of 100-200 ° C for 40-300 minutes.
- the term "oven-dry weight” means the mass of the bamboo chips that excludes the content of moisture in the bamboo chips.
- the moisture content of the bamboo chips is measured, and on the basis of the measured value, the weight of only the bamboo chip is calculated. Meanwhile, in the sixth step (prehydrolysis) of the present invention, xylose may additionally be extracted.
- bamboo contains pentosans in a high amount corresponding to 22%, and the pentosans are dissolved in the prehydrolysis step to produce the fiber (dissolving) pulp.
- the xylose dissolved in the sixth step is obtained by concentrating a solution isolated from the pulp after the prehydrolysis, using a heat exchange system or waste heat.
- methanol or ethanol is added to precipitate xylose through an alkanol precipitation method or a neutralization method.
- xylose may also be dissolved in a seventh step (cooking step) to be described later.
- the xylose dissolved in the cooking step is recovered by separating alkali and a xylose solution and subjecting the xylose solution to the same dissolution method as described above.
- a seventh step (cooking step) is conducted, in which the bamboo chips are introduced into a digester, in which the bamboo chips are cooked at high temperature in a liquor ratio of 1:3.5-6.0 (bamboo chips: chemical liquor) that indicates the ratio of a chemical liquor consisting of water, alkali and anthraquinone to the bamboo chips, thus softening and pulping the bamboo chips.
- a liquor ratio of 1:3.5-6.0 (bamboo chips: chemical liquor) that indicates the ratio of a chemical liquor consisting of water, alkali and anthraquinone to the bamboo chips, thus softening and pulping the bamboo chips.
- a soda-AQ process is applied in order to promote delignification and to prevent the decomposition of alpha-cellulose and also to increase the yield of the pulp.
- the soda-AQ process comprises adding a liquor consisting of alkali (mainly NaOH) , anthraquinone and water in a liquor ratio of 3.5-6.0 : 1 with respect to the oven-dry weight of the bamboo chips.
- the amount of alkali (as Na 2 O) added to water is preferably 10-30 % based on the oven- dry weight of the bamboo chips (i.e., mass excluding the content of moisture in the bamboo chips), and the anthraquinon (AQ) is preferably added in an amount of 0.01-2%.
- the cooking temperature in this cooking step is preferably 140-180 ° C , and the cooking time is preferably controlled within the range of 90-200 minutes depending on the polymerization degree and the quality of pulp to be produced.
- an eighth step contaminant removal step is conducted, in which contaminants introduced together with the bamboo is removed using a centrifugal cleaner.
- the centrifugal cleaner shown in FIG. 2 is used to remove contaminants introduced in the process together with the bamboo.
- the centrifugal cleaner is a cone-shaped device as shown in FIG. 2, and is used to remove contaminants from the cooked pulp.
- the contaminants to be removed mainly include sand, metal pieces and glass pieces, which can be introduced in each of the steps.
- the centrifugal cleaner is used considering the fact that the specific gravity of pulp when completely wetted with water approaches 1, whereas the specific gravity of the above-mentioned contaminants is higher than 1. Accordingly, when the pulp is introduced into an inlet 10 in FIG. 2, it rotates along the inner wall of the centrifugal cleaner 100 by the force of a pump while moving to the bottom 30, in which the rotating force applies centrifugal force. According to this action, relatively light pulp moves inward and is discharged through accepts 20, and heavy contaminants move outward and are discharged to the bottom 30.
- centrifugal cleaner 100 which is generally used to remove contaminant having a specific gravity higher than that of pulp during the production of the pulp, is called “forward cleaner”, and the centrifugal cleaner, which is used to removed contaminants (styrofoam, plastic, etc.) having a weight lower than that of pulp in the recycling of waste paper, is called “reverse cleaner”. Because the above-described centrifugal cleaner is well known in the art, the present invention is not limited thereto and may also utilize a variety of other centrifugal cleaners.
- a ninth step (selection step) is conducted, in which contaminants are removed from the cooked pulp using a pressure screen, and an incompletely cooked portion of the pulp is fed back into the digester.
- the pressure screen is used to remove non-dissociated fibers and contaminants.
- a fraction passed through the screen is sent to the following step, a fraction remaining on the screen is filtered through a vibrating screen, and a fraction remaining on the vibrating screen is wasted and a fibrous or incompletely cooked portion is fed back into the digester as shown in FIG. 1.
- a tenth step (washing and concentrating step) is conducted, in which a decker is used to wash the pulp to remove the chemicals, and the pulp is concentrated by squeezing water.
- the decker (not shown) is a machine that serves to wash the pulp and, at the same time, to concentrate the pulp by squeezing water. Using this decker, the pulp is washed and concentrated to a concentration suitable for bleaching.
- the washing operation is repeated at least three times in order to remove fine powders and parenchyma cells as much as possible.
- an eleventh step (bleaching step) , which is very important in the present invention, is conducted.
- ECF elementary chlorine-free
- TCF total chlorine-free
- DED, DEDD, DEDP, DEZP, DEOP, DEOZ and PEOZ can be selectively applied.
- a bleaching process, the number of bleaching stages, and bleaching conditions, are determined depending on the degree of required bleaching.
- D chlorine dioxide bleaching
- E alkaline extraction
- P peroxide bleaching
- 0 oxygen bleaching
- Z ozone bleaching
- the metal ions in the pulp will be inactivated by treating the pulp with a chelating agent (EDTA, DTPA, DTPMPA, etc.) to increase bleaching efficiency before conducting the bleaching of the pulp .
- a chelating agent EDTA, DTPA, DTPMPA, etc.
- the chelating agent is a chemical for making the reactivity of metal ions impotent, and if large amounts the metal ions are present in the pulp, they will remarkably deteriorate the performance of a bleaching chemical used for bleaching.
- the pulp is treated with the chelating agent before conducting the bleaching of the pulp.
- the bleaching stages of DEDD indicate that bleaching is conducted in four sequential steps of: (1) chlorine dioxide bleaching, (2) alkaline extraction, (3) chlorine dioxide bleaching, and (4) chlorine dioxide bleaching.
- various bleaching stages listed above indicate that a pulp producer may selectively the bleaching stages depending on the brightness or chemical purity required in the pulp to be produced, or the preference of a worker.
- the number of the bleaching stages may be increased or the amount of chemicals used may be increased. Also, even if the same level is required, a method of reducing the amount of a chemical used in each stage and increasing the number of the stages can be used in order to minimize adverse effects on pulp (pulp damage and decomposition, etc) . Accordingly, even if the quality of the same level is required, it is possible to control the number of the bleaching stages or the amount of chemicals used, and it is difficult to express this control as an absolute numerical value, because the state of pulp supplied into the bleaching process varies depending the degrees of prehydrolysis and pulping or cooking conducted in the above-described steps.
- the content of lignin in the pulp produced in the digester be first measured and, based on the measured content, the amount of addition of bleaching chemicals be calculated so as to increase or decrease the amount depending on the required quality.
- the present invention can prevent the generation of dioxin, an environmental pollutant, using said bleaching agent, and has excellent bleaching effects.
- a twelfth step (acid treatment and washing step) of removing metal ions from the surface and inside the pulp is conducted.
- the pulp us adjusted to pH 3-5, treated with acid at room temperature for
- the treatment time is preferably increased or decreased depending on the content of the metal ions and the extent of removal difficulty.
- the scope of the present invention encompasses all fiber (dissolving) pulps produced using bamboos according to the above-described method, and the pulps may be in the form of sheet or rolls.
- the sheet-shaped pulp is preferably prepared to have a thickness of 0.1-3 mm
- the roll-shaped pulp is preferably prepared by preparing the pulp into a web having a thickness of 0.1-1.5 mm and winding the web into a roll shape.
- the roll-shaped pulp is preferably prepared in a form thinner than the sheet-shaped pulp, because it should be wound on a roll.
- a Sri Lanka bamboo was split to a width of about 2 mm and then cut to a length of 15-25 mm.
- the cut material was screened through a 60-mesh screen to remove contaminants and small bamboo fragments, followed by washing.
- the bamboo was subjected to prehydrolysis at 170 ° C for 90 minutes. After completion of the prehydrolysis, the content within the digester was washed and then placed again into the digester, into which 16% active alkali (calculated as Na 2 O) and 0.1% anthraquinone were added so as to adjust the liquor ratio to 4:1. Then, the bamboo was cooked at 170 ° C for 120 minutes. The cooked pulp was washed and subjected to a four- stage bleaching of DEDD, and the properties of the resulting pulp are shown in Table 1 below.
- *Kappa number is used to indicate the amount of lignin remaining in the pulp produced in the digester, and is used as a standard for determining the amount of addition of chemicals in bleaching, and is calculated from the consumed amount of potassium permanganate through oxidation-reduction titration.
- the liquor ratio in the prehydrolysis was adjusted to 4:1, and the prehydrolysis was conducted at 170 ° C for 100 minutes .
- the cooked and washed pulp was subjected to a four- stage bleaching of DEDP, and the properties of the resulting pulp are shown in Table 2 below.
- the present invention it is possible to produce fiber (dissolving) pulp in more mild conditions by making prehydrolysis and cooking easy through longitudinal splitting and transverse cutting. Also, the soda-AQ process, in which anthraquinone is used as a catalyst in a cooking step, is applied for the pulping of bamboo, so that the present invention can have great effects on delignification, the improvement in pulp quality and the increase in pulp yield.
- an environmental problem can be solved by applying an ECF and TCF bleaching process, and it is possible to optionally control the content of alpha-cellulose and the degree of polymerization depending on the properties of rayon to be produced, by controlling the prehydrolysis, cooking and bleaching conditions.
- the use of waste as resources and the increase in economic efficiency can' be achieved by recovering xylose dissolved in a fiber (dissolving) pulp-manufacturing process and using the recovered xylose as a raw material for preparing xylitol, a sweetening agent, furfural, etc.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Business, Economics & Management (AREA)
- Emergency Management (AREA)
- Paper (AREA)
Abstract
Disclosed is a process for producing pulp utilizing bamboo, comprising finely cutting the bamboo into short segments and subjecting the cut bamboo to screening and washing processes to thereby produce dissolving pulp capable of achieving reduced consumption of chemical agents used during pre-hydrolysis and pulping processes and ease of reaction, and having superior quality and high yield. Further, provided are also a process for producing fiber (dissolving) pulp utilizing bamboo, capable of preventing generation of dioxin by bleaching the pulp via ECF or TCF bleaching, and a pulp produced using the same.
Description
PROCESS FOR PRODUCING FIBER PULP UTILIZING BAMBOO AND PULP
PRODUCED USING THE SAME
Technical Field
The present invention relates to a method for producing fiber pulp using bamboos, and more particularly to a method for producing good-quality fiber (dissolving) pulp using bamboos, which comprises longitudinally splitting the bamboo, transversely cutting the split bamboo to short lengths, dissolving hemicellulose from the cut material by prehydrolysis, and bleaching the prehydrolyzed material with a bleaching agent causing low environmental pollution, and thus has a high pulp production yield and does not emit environmental pollutants such as dioxin, as well as pulp produced thereby.
Generally, papermaking and dissolving pulps are recognized to be produced using wood.
As used herein, the term "dissolving pulp" refers to fiber pulp that can be used later to produce fibers.
In other words, because the dissolving pulps consist mostly of wood pulps, and producing pulp as the raw material of paper while conserving forests due to the lack of wood resources and maintaining the environment have recently became a great problem, effects to produce pulp using non- woody plant fibers and the like are being conducted.
Background Art
The present invention relates to a method for producing pulp, and more particularly to a method for producing
dissolving pulp (i.e., fiber pulp) which can be used later to produce fibers.
In other words, because the dissolving pulps consist mostly of wood pulps, and producing pulp as the raw material of paper while conserving forests due to the lack of wood resources and maintaining the environment have recently became a great problem, effects to produce pulp using non- woody plant fibers and the like are being conducted.
Such non-woody plants include paper mulberry bast fibers, hemps, cottons, and Manila hemps, and Korea Patent Publication Nos. 98-9651 and 93-2604 disclose a method for pulp using rice-straw.
All such efforts can be considered as efforts to conserve trees, which can prevent environmental pollution. In other words, these efforts aim to conserve trees by absorbing pollutants and carbon dioxide contained in the atmosphere through photosynthetic action while producing and supplying oxygen.
The development of industry and civilization really led to a great improvement in the quality of life of mankind, but involved a rapid increase in energy use, so that the emission of greenhouse gas was also rapidly increased, and thus the contamination of the global environment and side effects thereof became very severe. In typical examples thereof, the depletion of the ozone layer in the South Pole becomes very rapidly severe, and misfortunes caused by a rapid change in weather, global warming and ecosystem destruction occur in the whole world.
Such environment pollution phenomena very rapidly progressed to reach a state that threatens the survival of
mankind, and thus the Tokyo Protocol on the reduction of greenhouse gas emissions, which has been delayed due to the noncooperation of some of highly developed countries, became effective. Accordingly, in manufactures in various countries, efforts to reduce greenhouse gas emissions are urgently required, and in severe cases, additional expenses for purchasing greenhouse gas emission rights are expected.
Meanwhile, rayon corresponding to high-grade fiber utilizes dissolving pulp produced from wood as a raw material.
Regarding the pressure for the reduction of greenhouse gas emissions as described above, a tree is a reproducible natural material, but it requires a period of a few years to a few ten years until it reaches a usable level. For this reason, the regulation for the use of wood is tightened and the pressure for the development of an eco-friendly material that can substitute for wood is being actualized.
One mean for solving this problem, which has recently received great attention, is a non-woody plant that eliminates the need for the felling of wood.
In other words, when this non-woody plant is used to produce pulp, there will be a great advantage in that wood, which is consumed in large amounts, needs to be felled.
Among the non-woody plants, a bamboo, which receives attention and is used as a raw material in the present invention, is produced in large amounts in Southeast Asia countries such as China and Myanmar and sufficiently grows to a usable degree only within about five months.
Recently, in China, a technology for producing dissolving pulp using a bamboo having antibacterial activity
and for producing rayon fiber using the dissolving pulp was developed.
However, this technology has shortcomings in that it does not consider the compact structure of the bamboo, so that the pulping of the bamboo is not satisfactorily achieved, and it consumes large amounts of chemicals and energy, and has low yield because a bleaching process is conduced in strong conditions. In addition, it causes the decomposition and destruction of fiber, making the fiber weak. A chlorine bleaching process using elemental chlorine provides the cause of dioxin generation.
Also, because bleaching powder that acts as the cause of the corrosion of an apparatus is used as a bleaching chemical, the durability of the production apparatus is highly problematic.
In addition, this processing problem acts as the cause of increasing chemical amount, energy consumption and production cost per unit pulp production.
Disclosure of Invention
The present invention has been made to solve the above- described problems occurring in the prior art, and it is an object of the present invention to provide a method for producing good-quality fiber (dissolving) pulp using a bamboo, which comprises longitudinally splitting the bamboo, transversely cutting the split bamboo to short lengths, dissolving hemicellulose from the cut material by prehydrolysis, and bleaching the prehydrolyzed pulp with a bleaching agent causing low environmental pollution, and thus has a high pulp production yield and does not emit
environmental pollutants such as dioxin, as well as pulp produced thereby.
Another object of the present invention is to provide a method for producing dissolving (fiber) fiber using bamboos, which allows the production of pulps having various qualities according to the intended use thereof by applying a technology capable of optionally controlling the degree of polymerization of the fiber pulp, and also can produce byproduct xylose using a method wherein xylose which forms a significant portion of hemicellulose dissolved during a prehydrolysis process is recovered and purified from a solution and cooked waste isolated from the pulp after prehydrolysis, as well as pulp produced thereby.
To achieve the above objects, the present invention provides a method for producing fiber pulp using a bamboo, comprising: a leaf removal step of removing the leaves of the bamboo; a longitudinal splitting step of longitudinally splitting the bamboo to have a width of 1.5-3 mm; a transverse cutting step of transversely cutting the split bamboo to a length of 10-30 mm to produce bamboo chips; a screening step of filtering out small fragments or impurities from the cut bamboo chips; a washing step of washing the bamboo chips with water to remove impurities, contaminants or dust; a prehydrolysis step of subjecting the washed bamboo chips to prehydrolysis using water or steam, and adding sulfur dioxide or sulfuric acid according to the degree of required prehydrolysis to promote the prehydrolysis so as to dissolve hemicellulose from the bamboo chips; a cooking step of introducing the bamboo chips into a digester, in which the ratio of a chemical liquor consisting of water, alkali and
anthraquinone to the weight of the bamboo chips is adjusted to 1:3.5-6.0 (bamboo: chemical liquor), and the bamboo chips are cooked at high temperature in said liquor ratio, thus softening and pulping the bamboo chips; a contaminant removal step of removing contaminants with the bamboo using a centrifugal cleaner; a selection step of removing contaminants from the cooked pulp using a pressure screen, and feeding back an incompletely cooked portion of the bamboo into the digester; a washing and concentrating step, in which a decker is used to wash the pulp so as to remove the chemicals and to squeeze water so as to concentrate the pulp; a bleaching step of bleaching the washed and concentrated pulp; an acid treatment and washing step of removing metal ions present on the surface and inside the pulp; and a sheet preparation step of preparing the pulp into a sheet or a roll. In addition, the present invention provides fiber pulp produced by said method.
Brief Description of Drawings FIG. 1 is a flowchart showing sequentially the steps of a preparation method according to the present invention. FIG. 2 shows a general centrifugal cleaner.
Best Mode for Carrying Out the Invention The present invention is similar to the prior art, in that it relates to a method for preparing fiber pulp.
However, the present invention is remarkably different from the prior art, in that non-woody plant bamboo is used to produce pulp, the consumption of chemicals and energy is reduced by treating the bamboo in the production of the pulp
so as to make prehydrolysis and cooking easy, the generation of hazardous substances such as dioxin which can be generated in a bleaching process is minimized, xylose (also used as the raw material of gum) contained in hemicellulose dissolved during the inventive prehydolysis step can be produced, and thus wood present on the globe needs not to be felled, and the pulp prepared from the bamboo has surprisingly good quality. Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
As shown in the flowchart of FIG. 1, the inventive method for producing fiber (dissolving) pulp comprises a first step (bamboo leaf removal step) of removing the leaf of the bamboo. In other words, the bamboo leaf contains a large amount of extracts unnecessary to produce pulp, but has a small amount of essential fibrous material.
Thus, because the bamboo leaf is of help to prepare pulp, but rather can act as the cause of increasing the consumption of drugs, the bamboo leaf is removed before introduction into a process for producing dissolving pulp.
In other words, in the inventive method for producing the bamboo pulp, the bamboo leaf is not used and only the bamboo stalk is used. Then, a second step (longitudinal splitting step) of longitudinally splitting the bamboo to a width of 1.5-3 mm is conducted.
Due to the compact structure of the bamboo, chemicals are significantly difficult to penetrate the bamboo, compared to wood.
Thus, crushing must be conducted to initiate the production of pulp. For this purpose, the bamboo is first longitudinally split into half, and the split bamboo is additionally split to a narrower width. In this step, the bamboo is preferably split to a width of 1.5-3 mm.
This longitudinal splitting is a significantly characteristic step of the present invention, and when the bamboo is split at random without considering orientation, fibrous material will not be uniformly split, but rather the fibrous material itself can be broken.
This reduces the strength of the produced pulp to reduce the quality thereof.
For this reason, in the inventive production method, the bamboo is used after it is longitudinally split several times to have narrow width.
It is also possible to use a method of splitting the bamboo in a one-step process using a device mounted with a plurality of blades. Then, a third step (cutting step) of transversely cutting the longitudinally split bamboo to a length of 10-30 mm is conducted.
In other words, in order to produce small bamboo chips which are easily filled and packed in a digester, the split bamboo is transversely cut to a length of 10-30 mm using a cutter.
If the length of the bamboo chips is too large, they cannot be effectively packed into the digester, and if the bamboo is cut to an excessively short length, large damage to fiber can occur, resulting in the reduction in the strength
of the pulp.
Then, a fourth step (screening step) of filtering out small fragments or impurities from the cut bamboo chips is conducted. In other words, even if small fragments which are generated in the step of cutting the bamboo are prepared into pulp, the pulp is in a state in which the fibrous material is broken. Thus, these small fragments can weaken the strength of the pulp and increase the consumption of chemicals. Also, contaminants during the cutting step are not of any help to produce the pulp.
Accordingly, if these small fragments and contaminants are all used in the production of the fiber (dissolving) pulp, they will not be of any help for the yield (production rate) of the pulp and will adversely affect the quality of the pulp. For this reason, these are removed by screening.
Then, a fifth step (washing step) of washing the bamboo chips with water to remove impurities, contaminants and dust from the bamboo chips is conducted. In other words, the contaminant, dust and the like attached to the bamboo chips are removed with water.
This can reduce the consumption of unnecessary chemicals in a cooking process and allows pure pulp to be obtained, thus improving the quality of the produced pulp. Then, a sixth step (prehydrolysis step) is conducted, the washed bamboo chips are subjected to prehydrolysis using water or steam, and sulfur dioxide or sulfuric acid is added to the chips depending on the degree of required prehydrolysis to promote the prehydrolysis so as to dissolve hemicellulose from the bamboo chips.
In other words, to maximize the yield of fiber (dissolving) pulp in the bamboo chips while dissolving hemicellulose, the bamboo chips are subjected to prehydrolysis . This hydrolysis is performed with liquid water or steam using sulfur dioxide or sulfuric acid as a catalyst.
This prehydrolysis aims to dissolve hemicellulose from the bamboo chips, and thus if an acid is used alone, acid hydrolysis can severely occur to severely destroy cellulose. For this reason, the acid must be controlled to a suitable liquor ratio according to operation circumstances.
In this step, the ratio of the amount of liquid water and catalyst to the amount of the bamboo chips is preferably controlled within the range of 1.5-7 : 1 depending on the degree of required hydrolysis.
In other words, the prehydrolysis is performed in a state in which the ratio of the water-containing liquor to the bamboo chips is 1.5-7:1.
In this step, hemicellulose among the chemical components of the bamboo is decomposed while generating organic acid, which leads to the hydrolysis of the bamboo.
Thus, the desired polymerization degree and the hydrolysis degree of hemicellulose must be controlled using a characteristic in that, as said liquor ratio increases, the hydrolysis smoothly progresses.
In other words, regarding the liquor ratio, if the weight of the bamboo chips is 1 on an oven-dry weight basis, volume of the aqueous solution (if chemicals such as catalysts are contained, a state in which the chemicals are dissolved in water) is 1.5-7.
Also, the use of said liquor ratio aims to easily bring the bamboo chips into uniform contact with chemicals during the reaction and to control the extent of the reaction by allowing the intensity (concentration) of chemicals in contact with the bamboo chips to vary depending on the liquor ratio.
Also, although the conditions of the prehydrolysis step may slightly vary depending on the required quality, the prehydrolysis is preferably conducted at a temperature of 100-200°C for 40-300 minutes.
Such conditions were determined through many experiments conducted by the applicant.
As used herein, the term "oven-dry weight" means the mass of the bamboo chips that excludes the content of moisture in the bamboo chips.
To calculate the oven-dry weight, the moisture content of the bamboo chips is measured, and on the basis of the measured value, the weight of only the bamboo chip is calculated. Meanwhile, in the sixth step (prehydrolysis) of the present invention, xylose may additionally be extracted.
In other words, bamboo contains pentosans in a high amount corresponding to 22%, and the pentosans are dissolved in the prehydrolysis step to produce the fiber (dissolving) pulp.
These pentosans have been disposed of as waste in the prior art, but xylose that forms the significant portion of the pentosans can be used as an important raw material for producing furfural, xylitor, or a sweetening agent. In other words, the xylose dissolved in the sixth step
(prehydrolysis step) is obtained by concentrating a solution isolated from the pulp after the prehydrolysis, using a heat exchange system or waste heat.
To the concentrated solution, methanol or ethanol is added to precipitate xylose through an alkanol precipitation method or a neutralization method.
In addition, the xylose may also be dissolved in a seventh step (cooking step) to be described later.
In other words, the xylose dissolved in the cooking step is recovered by separating alkali and a xylose solution and subjecting the xylose solution to the same dissolution method as described above.
Then, a seventh step (cooking step) is conducted, in which the bamboo chips are introduced into a digester, in which the bamboo chips are cooked at high temperature in a liquor ratio of 1:3.5-6.0 (bamboo chips: chemical liquor) that indicates the ratio of a chemical liquor consisting of water, alkali and anthraquinone to the bamboo chips, thus softening and pulping the bamboo chips. The use of the prior sulfite process for the cooking of the bamboo chips has problems in that the fiber becomes weak and the yield of the pulp is low.
Thus, in the present invention, a soda-AQ process is applied in order to promote delignification and to prevent the decomposition of alpha-cellulose and also to increase the yield of the pulp.
In other words, the soda-AQ process comprises adding a liquor consisting of alkali (mainly NaOH) , anthraquinone and water in a liquor ratio of 3.5-6.0 : 1 with respect to the oven-dry weight of the bamboo chips.
Also, in the soda-AQ process, the amount of alkali (as Na2O) added to water is preferably 10-30 % based on the oven- dry weight of the bamboo chips (i.e., mass excluding the content of moisture in the bamboo chips), and the anthraquinon (AQ) is preferably added in an amount of 0.01-2%.
The cooking temperature in this cooking step is preferably 140-180 °C , and the cooking time is preferably controlled within the range of 90-200 minutes depending on the polymerization degree and the quality of pulp to be produced.
That the xylose can also be extracted in this step is already described above in the sixth step (prehydrolyiss step) , and thus the description thereof will be omitted herein. Then, an eighth step (contaminant removal step) is conducted, in which contaminants introduced together with the bamboo is removed using a centrifugal cleaner.
In other words, the centrifugal cleaner shown in FIG. 2 is used to remove contaminants introduced in the process together with the bamboo.
Briefly, the centrifugal cleaner is a cone-shaped device as shown in FIG. 2, and is used to remove contaminants from the cooked pulp. The contaminants to be removed mainly include sand, metal pieces and glass pieces, which can be introduced in each of the steps.
The centrifugal cleaner is used considering the fact that the specific gravity of pulp when completely wetted with water approaches 1, whereas the specific gravity of the above-mentioned contaminants is higher than 1. Accordingly, when the pulp is introduced into an inlet
10 in FIG. 2, it rotates along the inner wall of the centrifugal cleaner 100 by the force of a pump while moving to the bottom 30, in which the rotating force applies centrifugal force. According to this action, relatively light pulp moves inward and is discharged through accepts 20, and heavy contaminants move outward and are discharged to the bottom 30.
In addition, the centrifugal cleaner 100, which is generally used to remove contaminant having a specific gravity higher than that of pulp during the production of the pulp, is called "forward cleaner", and the centrifugal cleaner, which is used to removed contaminants (styrofoam, plastic, etc.) having a weight lower than that of pulp in the recycling of waste paper, is called "reverse cleaner". Because the above-described centrifugal cleaner is well known in the art, the present invention is not limited thereto and may also utilize a variety of other centrifugal cleaners.
Then, a ninth step (selection step) is conduced, in which contaminants are removed from the cooked pulp using a pressure screen, and an incompletely cooked portion of the pulp is fed back into the digester.
In other words, the pressure screen is used to remove non-dissociated fibers and contaminants. A fraction passed through the screen is sent to the following step, a fraction remaining on the screen is filtered through a vibrating screen, and a fraction remaining on the vibrating screen is wasted and a fibrous or incompletely cooked portion is fed back into the digester as shown in FIG. 1.
Then, a tenth step (washing and concentrating step) is conducted, in which a decker is used to wash the pulp to remove the chemicals, and the pulp is concentrated by squeezing water. The decker (not shown) is a machine that serves to wash the pulp and, at the same time, to concentrate the pulp by squeezing water. Using this decker, the pulp is washed and concentrated to a concentration suitable for bleaching.
In this step, the washing operation is repeated at least three times in order to remove fine powders and parenchyma cells as much as possible.
Then, an eleventh step (bleaching step) , which is very important in the present invention, is conducted.
In order words, in order to eliminate environmental problems such as the generation of environmental hormone dioxin, an ECF (elementary chlorine-free) or TCF (total chlorine-free) bleaching process is used.
As bleaching stages in this step, DED, DEDD, DEDP, DEZP, DEOP, DEOZ and PEOZ can be selectively applied. A bleaching process, the number of bleaching stages, and bleaching conditions, are determined depending on the degree of required bleaching.
In the above description of the bleaching stages, D means chlorine dioxide bleaching, E means alkaline extraction, P means peroxide bleaching, 0 means oxygen bleaching, and Z means ozone bleaching.
If the content of metal ions in the pulp is high, the metal ions will be inactivated by treating the pulp with a chelating agent (EDTA, DTPA, DTPMPA, etc.) to increase bleaching efficiency before conducting the bleaching of the
pulp .
Herein, the chelating agent is a chemical for making the reactivity of metal ions impotent, and if large amounts the metal ions are present in the pulp, they will remarkably deteriorate the performance of a bleaching chemical used for bleaching.
For this reason, if the content of the metal ions is large so that it reduces bleaching efficiency, the pulp is treated with the chelating agent before conducting the bleaching of the pulp.
As an example of a bleaching method using the bleaching stages, the bleaching stages of DEDD indicate that bleaching is conducted in four sequential steps of: (1) chlorine dioxide bleaching, (2) alkaline extraction, (3) chlorine dioxide bleaching, and (4) chlorine dioxide bleaching.
In other words, various bleaching stages listed above indicate that a pulp producer may selectively the bleaching stages depending on the brightness or chemical purity required in the pulp to be produced, or the preference of a worker.
Regarding the purpose for increasing the number of the bleaching stages, when the brightness or chemical purity is greatly required, the number of the bleaching stages may be increased or the amount of chemicals used may be increased. Also, even if the same level is required, a method of reducing the amount of a chemical used in each stage and increasing the number of the stages can be used in order to minimize adverse effects on pulp (pulp damage and decomposition, etc) . Accordingly, even if the quality of the same level is
required, it is possible to control the number of the bleaching stages or the amount of chemicals used, and it is difficult to express this control as an absolute numerical value, because the state of pulp supplied into the bleaching process varies depending the degrees of prehydrolysis and pulping or cooking conducted in the above-described steps.
However, when the fiber (dissolving pulp) is bleached, it is preferable that the content of lignin in the pulp produced in the digester be first measured and, based on the measured content, the amount of addition of bleaching chemicals be calculated so as to increase or decrease the amount depending on the required quality.
Thus, the present invention can prevent the generation of dioxin, an environmental pollutant, using said bleaching agent, and has excellent bleaching effects.
Then, a twelfth step (acid treatment and washing step) of removing metal ions from the surface and inside the pulp is conducted.
In other words, to remove metal ions present on the surface and inside the fiber (dissolving) pulp, the pulp us adjusted to pH 3-5, treated with acid at room temperature for
20-110 minutes and washed with clean water until it reaches the natural pH range.
The treatment time is preferably increased or decreased depending on the content of the metal ions and the extent of removal difficulty.
Finally, a thirteen step (sheet preparation method) of preparing the sheet into a sheet or a roll is conducted.
Also, the scope of the present invention encompasses all fiber (dissolving) pulps produced using bamboos according
to the above-described method, and the pulps may be in the form of sheet or rolls.
Also, the sheet-shaped pulp is preferably prepared to have a thickness of 0.1-3 mm, and the roll-shaped pulp is preferably prepared by preparing the pulp into a web having a thickness of 0.1-1.5 mm and winding the web into a roll shape. In other words, the roll-shaped pulp is preferably prepared in a form thinner than the sheet-shaped pulp, because it should be wound on a roll. Hereinafter, Examples of the present invention will be described with reference to the accompanying drawings. Example 1
A Myanmar bamboo was split to a width of about 2 mm and then cut to a length of 15-25 mm. The cut material was screened through a 60-mesh screen to remove contaminants and small bamboo fragments, followed by washing.
400 g (on a oven-dry weight basis) of the washed bamboo was placed in a digester into which water was added to make a liquor ratio of 6:1. Then, a stainless weight is laid on the bamboo such that the bamboo could be sufficiently immersed in water.
After the digester was covered with a lid and screwed, the bamboo was subjected to prehydrolysis at 170 °C for 90 minutes. After completion of the prehydrolysis, the content within the digester was washed and then placed again into the digester, into which 16% active alkali (calculated as Na2O) and 0.1% anthraquinone were added so as to adjust the liquor ratio to 4:1. Then, the bamboo was cooked at 170 °C for 120 minutes.
The cooked pulp was washed and subjected to a four- stage bleaching of DEDD, and the properties of the resulting pulp are shown in Table 1 below.
Table 1: Results of prehydrolysis and pulping tests of bamboo
*Kappa number is used to indicate the amount of lignin remaining in the pulp produced in the digester, and is used as a standard for determining the amount of addition of chemicals in bleaching, and is calculated from the consumed amount of potassium permanganate through oxidation-reduction titration.
Example 2
The treatment of bamboo and most of conditions were the same as in Example 1, but the prehydrolysis and bleaching conditions were as follows:
The liquor ratio in the prehydrolysis was adjusted to 4:1, and the prehydrolysis was conducted at 170 °C for 100 minutes . The cooked and washed pulp was subjected to a four- stage bleaching of DEDP, and the properties of the resulting pulp are shown in Table 2 below.
Table 2: Results of prehydrolysis and pulping tests of
bamboo
Industrial Applicability As described above, according to the present invention, it is possible to produce fiber (dissolving) pulp in more mild conditions by making prehydrolysis and cooking easy through longitudinal splitting and transverse cutting. Also, the soda-AQ process, in which anthraquinone is used as a catalyst in a cooking step, is applied for the pulping of bamboo, so that the present invention can have great effects on delignification, the improvement in pulp quality and the increase in pulp yield.
Also, an environmental problem can be solved by applying an ECF and TCF bleaching process, and it is possible to optionally control the content of alpha-cellulose and the degree of polymerization depending on the properties of rayon to be produced, by controlling the prehydrolysis, cooking and bleaching conditions. In addition, the use of waste as resources and the increase in economic efficiency can' be achieved by recovering xylose dissolved in a fiber (dissolving) pulp-manufacturing process and using the recovered xylose as a raw material for preparing xylitol, a sweetening agent, furfural, etc.
Claims
1. A method for producing fiber pulp using a bamboo, comprising: (1) a leaf removal step of removing a leaf from the bamboo;
(2) a longitudinal splitting step of longitudinally splitting the bamboo to have a width of 1.5-3 mm;
(3) a transverse cutting step of transversely cutting the split bamboo to a length of 10-30 mm to produce bamboo chips;
(4) a screening step of filtering out small fragments or impurities from the cut bamboo chips;
(5) a washing step of washing the bamboo chips with water to remove impurities, contaminants or dust;
(6) a prehydrolysis step of subjecting the washed bamboo chips to prehydrolysis using water or steam, and adding sulfur dioxide or sulfuric acid according to the degree of required prehydrolysis to promote the prehydrolysis so as to dissolve hemicellulose from the bamboo chips;
(7) a cooking step of introducing the bamboo chips into a digester, in which the ratio of a chemical liquor consisting of water, alkali and anthraquinone to the weight of the bamboo chips is adjusted to 1:3.5-6.0 (bamboo: chemical liquor) , and the bamboo chips are cooked at high temperature, thus softening and pulping the bamboo chips;
(8) a contaminant removal step of removing contaminants with the bamboo using a centrifugal cleaner;
(9) a selection step of removing contaminants from the cooked pulp using a pressure screen, and feeding back an incompletely cooked portion of the bamboo into the digester;
(10) a washing and concentrating step, in which a decker is used to wash the pulp so as to remove the chemicals and to squeeze water so as to concentrate the pulp; (11) a bleaching step of bleaching the washed and concentrated pulp;
(12) an acid treatment and washing step of removing metal ions present on the surface and inside the pulp; and
(13) a sheet preparation step of preparing the pulp into a sheet or a roll.
2. The method of Claim 1, wherein the prehydrolysis in the step (6) is performed in a state in which the liquor ratio of a water-containing liquor to the bamboo chips is 1.5-7:1.
3. The method of Claim 1, wherein, in the step (7), the alkali (as Na2O) added to water is 10-30% based on the oven- dry weight of the bamboo chips (i.e., (mass excluding the water content of the bamboo chips) , and the anthraquinone (AQ) is added in an amount of 0.01-2%.
4. The method of Claim 1, wherein the bleaching of the step (11) is performed using bleaching stages according to an ECF (elementary chlorine free) or TCF (total chlorine free) bleaching process.
5. The method of Claim 4, wherein the bleaching stages are selected from the group consisting of DED, DEDD, DEDP, DEZP, DEOP, DEOZ, and PEOZ.
6. The method of Claim 1, wherein the acid treatment and washing step of the step (12) comprises adjusting the pH of the pulp to 3-5, treating the pulp with acid at room temperature for 20-110 minutes, and washing the treated pulp with clean water until the pH of the pulp reaches a natural pH range.
7. Fiber pulp produced using a bamboo according to the method of any one of Claims 1 to 6.
8. The fiber pulp of Claim 7, wherein the pulp is in the form of a sheet or a roll.
9. The fiber pulp of Claim 8, wherein the sheet-shaped pulp is produced using a bamboo having a thickness of 0.1-3 mm.
10. The fiber pulp of Claim 8, wherein the roll-shaped pulp consists of a wound web having a thickness of 0.1-1.5mm.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/592,680 US20080295982A1 (en) | 2005-04-27 | 2005-06-18 | Process for Producing Fiber Pulp Utilizing Bamboo and Pulp Produced Using the Same |
JP2007514926A JP4586066B2 (en) | 2005-04-27 | 2005-06-18 | Pulp manufacturing method using bamboo and pulp manufactured using this method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR10-2005-0035117 | 2005-04-27 | ||
KR1020050035117A KR100547491B1 (en) | 2005-04-27 | 2005-04-27 | The production method and pulp maked bamboos |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2006115310A1 true WO2006115310A1 (en) | 2006-11-02 |
Family
ID=37178526
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/KR2005/001893 WO2006115310A1 (en) | 2005-04-27 | 2005-06-18 | Process for producing fiber pulp utilizing bamboo and pulp produced using the same |
Country Status (5)
Country | Link |
---|---|
US (1) | US20080295982A1 (en) |
JP (1) | JP4586066B2 (en) |
KR (1) | KR100547491B1 (en) |
CN (1) | CN1854388A (en) |
WO (1) | WO2006115310A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010046532A1 (en) * | 2008-10-21 | 2010-04-29 | Danisco A/S | Process of producing xylose and dissolving pulp |
US20100294443A1 (en) * | 2006-11-22 | 2010-11-25 | I'big, Inc. | Manufacturing method of bamboo chip and manufacturing method bamboo fiber using the bamboo chip |
EP2322713A1 (en) * | 2009-11-11 | 2011-05-18 | Aarsen Holding B.V. | Method for producing bamboo fibres as well as plastics containing same |
WO2022235212A1 (en) * | 2021-05-03 | 2022-11-10 | Asia Pacific Resources International Holdings Ltd. | Process for treating non-wood feedstock |
WO2023132814A1 (en) * | 2022-01-04 | 2023-07-13 | Releaf Paper France Sas | Method of obtaining chemical-thermomechanical fibrous mass from plant raw materials and systems for its realization |
Families Citing this family (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100638607B1 (en) | 2006-03-09 | 2006-10-31 | 이권혁 | The production method for xylose maked from bamboos |
CN100441772C (en) * | 2007-02-06 | 2008-12-10 | 新邵县广信有限责任公司 | Production technology of thermomechanical bamboo pulp |
CN101748630B (en) * | 2009-12-14 | 2012-10-17 | 昆明理工大学 | Acid-free pre-hydrolysis enzymolysis-free method for preparing bamboo pulp of Dendrocalamus giganteus Munro series |
CN102174765B (en) * | 2010-12-01 | 2013-12-25 | 江西含珠实业有限公司 | Technological process for making Lian-si paper by using moso bamboo |
CN102127877B (en) * | 2010-12-28 | 2012-07-25 | 宜宾竹海竹资源科技有限责任公司 | Production process of bamboo-dissolving pulp |
CN102959142B (en) * | 2011-03-21 | 2016-01-06 | 张毅 | The production technology of natural bamboo fibres |
CN102154884B (en) * | 2011-03-31 | 2012-07-18 | 重庆理文造纸有限公司 | Improved bleaching process for bamboo wood dissolving pulp |
CN102242403B (en) * | 2011-06-15 | 2013-11-06 | 浙江农林大学 | Production process for linen bamboo fibers, spinnable linen bamboo fibers and bamboo fiber yarns |
CN102321990A (en) * | 2011-09-16 | 2012-01-18 | 四川永丰纸业股份有限公司 | Method for preparing bamboo pulp with full liquid phase pre-hydrolytic sulfate rapid displacement cooking |
WO2013044347A1 (en) * | 2011-09-28 | 2013-04-04 | Prairie Pulp & Paper Inc. | Method for preparing nonwood fiber paper |
CN102517968B (en) * | 2011-12-20 | 2014-01-15 | 恒天海龙股份有限公司 | Method for preparing dissolving pulp for viscose fibers by using mulberry twig stem cores |
JP2014037643A (en) * | 2012-08-15 | 2014-02-27 | Nippon Paper Industries Co Ltd | Dissolving pulp |
CN103114482B (en) * | 2013-01-23 | 2015-07-15 | 天津商业大学 | Preparation method for dissolving pulp of monterey pine of needlebush |
JP5713413B2 (en) * | 2013-02-04 | 2015-05-07 | 国立大学法人九州工業大学 | Bamboo heat treatment equipment |
JP6522274B2 (en) * | 2013-08-06 | 2019-05-29 | 日本製紙株式会社 | Method of making dissolved kraft pulp. |
JP6398388B2 (en) * | 2014-07-02 | 2018-10-03 | 王子ホールディングス株式会社 | Dissolving pulp and method for producing the same |
CN104141256B (en) * | 2014-07-24 | 2017-01-18 | 四川环龙新材料有限公司 | Uncolored bamboo fiber with high antibacterial activity and processing method thereof |
CN105672013A (en) * | 2016-02-17 | 2016-06-15 | 四川永丰纸业股份有限公司 | Natural color bamboo pulp production method and natural color paper for daily use produced through same |
CN108252141A (en) * | 2018-01-04 | 2018-07-06 | 安徽工程大学 | A kind of preparation method of Lin's grass fiber and its wet laid nonwoven fabric |
JP7129710B2 (en) * | 2018-01-10 | 2022-09-02 | 国立大学法人 大分大学 | CELLULOSE NANOFIBER AND SHEET-LIKE MATERIAL COMPOSITION THEREOF, AND METHOD FOR MANUFACTURING THEM |
CN108588852B (en) * | 2018-03-20 | 2020-08-18 | 青岛大学 | Method for cleaning and degumming high-lignin raw material |
CN108486950A (en) * | 2018-05-18 | 2018-09-04 | 四川环龙新材料有限公司 | A kind of antibacterial paper used for sexual life of height and its preparation process based on non-sulfuric acid salt method this colour chemistry bamboo pulp |
CN109015976A (en) * | 2018-10-08 | 2018-12-18 | 四川工商职业技术学院 | A kind of cutting process of pulping and paper-making bamboo |
CN109403118B (en) * | 2018-11-21 | 2021-02-02 | 湖南骏泰新材料科技有限责任公司 | Washing, selecting and bleaching method for preparing cellulose from agricultural and forestry residues |
US10926998B2 (en) * | 2018-11-30 | 2021-02-23 | Jiyang College Of Zhejiang A&F University | Pure bamboo fiber mattress and manufacturing method thereof |
CN110747673B (en) * | 2019-09-23 | 2021-01-19 | 西南科技大学 | Bi/Mo/Co2O4/CO2Method for catalytically purifying Si impurities on surface layer of pulping bamboo chip |
KR20190121272A (en) | 2019-10-07 | 2019-10-25 | 정우동 | Nonwoven fabric for mask and manufacturing method thereof |
JP6866052B1 (en) * | 2020-03-27 | 2021-04-28 | 株式会社ナファ生活研究所 | Method for producing dissolved pulp derived from bamboo |
CN112813713B (en) * | 2021-01-07 | 2022-12-27 | 山东鸿泰鼎新材料科技有限公司 | Preparation method of special pulp for producing lyocell fibers from bamboo willows |
CN113201961A (en) * | 2021-05-20 | 2021-08-03 | 四川工商职业技术学院 | Preparation method of bamboo dissolving pulp |
CN113882181B (en) * | 2021-09-03 | 2022-08-12 | 四川天竹竹资源开发有限公司 | Lyocell fiber bamboo pulp and preparation method thereof |
CN114687234B (en) * | 2022-03-31 | 2023-06-16 | 华南理工大学 | Method for preparing fluff pulp by utilizing bamboo and fluff pulp prepared by same |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4259147A (en) * | 1975-02-12 | 1981-03-31 | New Fibers International | Pulping process |
US4857145A (en) * | 1987-07-13 | 1989-08-15 | Process Evaluation And Development Corporation | Process for making a pulp from bamboo |
JPH04126885A (en) * | 1990-09-14 | 1992-04-27 | Akio Onda | Production of chemical pulp |
US5198074A (en) * | 1991-11-29 | 1993-03-30 | Companhia Industreas Brasileiras Portela | Process to produce a high quality paper product and an ethanol product from bamboo |
JPH05239791A (en) * | 1992-02-25 | 1993-09-17 | Tootaru In:Kk | Paper comprising bamboo material as raw material |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB265697A (en) * | 1925-11-14 | 1927-02-14 | Arthur Henry Lymn | Process for the production of cellulosic material |
JPS4829801B1 (en) * | 1970-07-09 | 1973-09-13 | ||
JPS5685489A (en) * | 1979-12-10 | 1981-07-11 | Kogyo Gijutsuin | Pulp production |
JPH0364589A (en) * | 1989-07-28 | 1991-03-19 | Mitsubishi Gas Chem Co Inc | Bleaching of chemical pulp |
SE470065C (en) * | 1991-04-30 | 1996-01-15 | Eka Nobel Ab | Treatment of chemical pulp with an acid and then a magnesium and calcium compound in chlorine-free bleaching |
US20030029589A1 (en) * | 1998-06-17 | 2003-02-13 | Nile Fiber Pulp & Paper, Inc. | Total chlorine free bleaching of Arundo donax pulp |
CN1231632C (en) * | 1998-06-17 | 2005-12-14 | 尼勒纤维纸浆和纸公司 | Arundo donax pulp, paper products and particle board |
JP2001192991A (en) * | 2000-01-01 | 2001-07-17 | Institute Of Tsukuba Liaison Co Ltd | Method of bleaching alkali pulp |
JP2001248084A (en) * | 2000-02-29 | 2001-09-14 | Mitsubishi Paper Mills Ltd | Method for producing bleached kraft pulp and printing paper |
JP2001248083A (en) * | 2000-03-01 | 2001-09-14 | Onda Akio | Method for producing chemical pulp containing nonwoody and woody resource as raw material |
JP3556209B1 (en) * | 2002-04-22 | 2004-08-18 | 倉敷紡績株式会社 | Antibacterial and antifungal fiber |
JP2003310721A (en) * | 2002-04-25 | 2003-11-05 | Miyo Kk | Antibacterial cloth made of bamboo fibers |
JP4336562B2 (en) * | 2003-10-27 | 2009-09-30 | 株式会社ナファ生活研究所 | Method for producing cellulose fiber having antibacterial properties from bamboo pulp produced from bamboo |
-
2005
- 2005-04-27 KR KR1020050035117A patent/KR100547491B1/en not_active IP Right Cessation
- 2005-06-18 JP JP2007514926A patent/JP4586066B2/en not_active Expired - Fee Related
- 2005-06-18 WO PCT/KR2005/001893 patent/WO2006115310A1/en active Application Filing
- 2005-06-18 US US10/592,680 patent/US20080295982A1/en not_active Abandoned
- 2005-10-10 CN CNA2005101082940A patent/CN1854388A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4259147A (en) * | 1975-02-12 | 1981-03-31 | New Fibers International | Pulping process |
US4857145A (en) * | 1987-07-13 | 1989-08-15 | Process Evaluation And Development Corporation | Process for making a pulp from bamboo |
JPH04126885A (en) * | 1990-09-14 | 1992-04-27 | Akio Onda | Production of chemical pulp |
US5198074A (en) * | 1991-11-29 | 1993-03-30 | Companhia Industreas Brasileiras Portela | Process to produce a high quality paper product and an ethanol product from bamboo |
JPH05239791A (en) * | 1992-02-25 | 1993-09-17 | Tootaru In:Kk | Paper comprising bamboo material as raw material |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100294443A1 (en) * | 2006-11-22 | 2010-11-25 | I'big, Inc. | Manufacturing method of bamboo chip and manufacturing method bamboo fiber using the bamboo chip |
WO2010046532A1 (en) * | 2008-10-21 | 2010-04-29 | Danisco A/S | Process of producing xylose and dissolving pulp |
US9068236B2 (en) | 2008-10-21 | 2015-06-30 | Dupont Nutrition Biosciences Aps | Process of producing xylose and dissolving pulp |
EP2322713A1 (en) * | 2009-11-11 | 2011-05-18 | Aarsen Holding B.V. | Method for producing bamboo fibres as well as plastics containing same |
WO2022235212A1 (en) * | 2021-05-03 | 2022-11-10 | Asia Pacific Resources International Holdings Ltd. | Process for treating non-wood feedstock |
WO2023132814A1 (en) * | 2022-01-04 | 2023-07-13 | Releaf Paper France Sas | Method of obtaining chemical-thermomechanical fibrous mass from plant raw materials and systems for its realization |
Also Published As
Publication number | Publication date |
---|---|
JP2008501074A (en) | 2008-01-17 |
US20080295982A1 (en) | 2008-12-04 |
CN1854388A (en) | 2006-11-01 |
JP4586066B2 (en) | 2010-11-24 |
KR100547491B1 (en) | 2006-01-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20080295982A1 (en) | Process for Producing Fiber Pulp Utilizing Bamboo and Pulp Produced Using the Same | |
CN1010698B (en) | Make the method for paper pulp by bamboo | |
WO2007102638A1 (en) | Method for producing xylose from bamboos | |
WO2007004757A1 (en) | Process for producing pulp utilizing bamboo and pulp and papers produced using the same | |
JP2009516086A (en) | New pulp and pulping methods. | |
JPS6011159B2 (en) | Method for producing cellulose pulp with yields ranging from 65 to 95% | |
KR100662042B1 (en) | The production method and pulp maked bamboos | |
JP2004503683A5 (en) | ||
FI69656C (en) | FOERFARANDE FOER FOERBAETTRAD TVAETTNING AV UR LIGNOCELLULOSAMATERIAL FRAMSTAELLDA CELLULOSAMASSOR. | |
CN110894696A (en) | Method for bleaching bamboo pulp | |
JP2010144273A (en) | Method for producing chemical pulp of lignocellulose material | |
CN1458334A (en) | Presteaming process for plant fiber material in steam explosion pulping | |
NO140535B (en) | PROCEDURE FOR THE PREPARATION OF CELLULOSE PULP BY CONNECTION WITH THE OXYGEN | |
CN103343468A (en) | Clean production technology based on steam explosion slurrying | |
CN103526629A (en) | Pulping process of waste paper with high wet strength | |
KR20110026635A (en) | Method of manufacture pulp for bamboos fiber | |
CN101158121B (en) | Process for manufacturing dissolved pulp by using ethanol, sulfate and acetic acid | |
CN102373638B (en) | High-yield clean pulping method from oil palm EFB (empty fruit bunch) fiber through biological enzyme process | |
KR101282830B1 (en) | Production Method of Solubility Pulp Made From Dioscorea batatas | |
KR101282831B1 (en) | Solubility Pulp Made From Dioscorea batatas | |
CN101235607B (en) | Method for producing natural antibacterial bamboo fiber | |
WO2016072885A2 (en) | Cellulose production method | |
CN101871135A (en) | Method for producing bleaching man-made fiber pulp | |
WO2005052247A1 (en) | Catalyzer for clean pulping and process for using the same | |
JPH11158788A (en) | Pulp production |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 2007514926 Country of ref document: JP |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
NENP | Non-entry into the national phase |
Ref country code: DE |
|
NENP | Non-entry into the national phase |
Ref country code: RU |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1200702520 Country of ref document: VN |
|
32PN | Ep: public notification in the ep bulletin as address of the adressee cannot be established |
Free format text: EPO FORM 1205A "NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 112(1) EPC" |
|
WWE | Wipo information: entry into national phase |
Ref document number: 10592680 Country of ref document: US |