WO2006035696A1 - セルロース誘導体リン酸エステル及びそれを用いた金属吸着材 - Google Patents
セルロース誘導体リン酸エステル及びそれを用いた金属吸着材 Download PDFInfo
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- WO2006035696A1 WO2006035696A1 PCT/JP2005/017605 JP2005017605W WO2006035696A1 WO 2006035696 A1 WO2006035696 A1 WO 2006035696A1 JP 2005017605 W JP2005017605 W JP 2005017605W WO 2006035696 A1 WO2006035696 A1 WO 2006035696A1
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- metal
- cellulose
- phosphate
- dihydroxypropylcellulose
- dihydroxypropoxy
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B5/00—Preparation of cellulose esters of inorganic acids, e.g. phosphates
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/262—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon to carbon unsaturated bonds, e.g. obtained by polycondensation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/265—Synthetic macromolecular compounds modified or post-treated polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B11/00—Preparation of cellulose ethers
- C08B11/02—Alkyl or cycloalkyl ethers
- C08B11/04—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B11/00—Preparation of cellulose ethers
- C08B11/02—Alkyl or cycloalkyl ethers
- C08B11/04—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals
- C08B11/08—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals with hydroxylated hydrocarbon radicals; Esters, ethers, or acetals thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B11/00—Preparation of cellulose ethers
- C08B11/20—Post-etherification treatments of chemical or physical type, e.g. mixed etherification in two steps, including purification
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B13/00—Preparation of cellulose ether-esters
Definitions
- the present invention relates to a cellulose derivative phosphate that efficiently adsorbs metal ions in a solution.
- the present invention relates to a manufacturing method thereof, a metal adsorbent using the same, and a metal adsorbing apparatus using the metal adsorbent.
- a metal adsorbent a material in which a functional group that adsorbs metal ions is chemically bonded to a carrier that immobilizes the metal ion, and the low molecular weight compound having the functional group is not eluted by the carrier.
- the metal adsorption functional group include a carboxyl group, a sulfonic acid group, an amino group, an imino group, a thiol group, and a phosphoric acid group.
- the metal species that are easily adsorbed differ depending on the type of the metal-adsorbing functional group.
- the sulfonic acid group mainly adsorbs monovalent metal ions such as potassium and sodium, and the carboxyl group and phosphate group are all metals including calcium and magnesium.
- Amino groups, imino groups and thiol groups are said to adsorb heavy metals. Therefore, the metal adsorption functional group is selected according to the metal species to be adsorbed.
- various carriers and styrene resins, acrylic resins, and other bur resins, and natural materials such as cellulose (powder, fiber, gel), chitin, chitosan, wool, etc. are used.
- metal adsorbents In the production of metal adsorbents, from the viewpoint of ease of synthesis and homogeneity in quality, they are often produced by introducing metal adsorbing functional groups into polymerizable monomers and then polymerizing them. Known as. In addition, metal adsorbing functional groups are also chemically introduced into natural materials such as cellulose and wool because of the low cost of raw materials and production.
- the metal adsorption capacity of a metal adsorbent is greatly influenced by the shape of the material in addition to its chemical structure. Resin is often molded into beads due to its properties, and the proportion of functional groups contained in the beads increases, and the resin is hydrophobic and the diffusion rate of metal ions and regenerant into the resin decreases. In addition, there is a problem in processing efficiency, such as increasing the minimum adsorbable concentration. Moreover, the usage method of a metal adsorbent is also limited by the shape of the material.
- the amount to be treated in the case of treatment for the purpose of metal removal or capture especially water softening, removal of harmful metals from industrial wastewater, removal of harmful metals from contaminated soil or capture of beneficial metals
- a large amount of metal adsorbent to be used is required because of its large area. Therefore, for these purposes, it is desirable that the metal adsorbent used has a high adsorption capacity and is inexpensive and recyclable.
- the phosphate group as a metal-adsorbing functional group is: 1) a single phosphate group can adsorb divalent metal ions, so the amount of metal adsorption is large, and 2) it is easy to liberate hydrogen ions on the acidic side. Solution capable of metal adsorption Wide range of pH 3) Low metal ion concentration capable of metal adsorption is low.
- cellulose as a carrier has the following features: 1) the fiber itself has high rigidity, 2) most of the functional groups are exposed on the fiber surface, and 3) it is highly processable.
- a metal adsorbent having a phosphate group using a natural material as a carrier is attracting attention.
- cellulose phosphate ester is used for removal of heavy metals and radioactive metals (Patent Document 1), a method for increasing the mechanical strength of cellulose fiber using sulfur powder in the production of cell mouth phosphates (Patent Document 2), cellulose and Use starch phosphate ester, acetate ester, and benzoate ester to remove heavy metals from water (Patent Document 3), filter made of cellulose having rubamide group and phosphate ester group Materials for removing components or heavy metals (Patent Documents 3 and 4) are known.
- metal adsorption capacity is not sufficient from the standpoint of metal adsorption capacity or economic efficiency.
- metal reaction rate is excellent and inexpensive.
- mechanical strength is excellent and inexpensive.
- workability is excellent and inexpensive.
- application range is excellent and inexpensive.
- reusability is excellent and inexpensive. Development of metal adsorbents is strongly desired.
- Patent Document 1 Russian Patent No. 2096082 C1
- Patent Document 2 International Publication No. 99/28372
- Patent Document 3 German Patent Application Publication No. 19859746 A
- Patent Document 4 Special Table 2003-500199
- the object of the present invention is to provide a metal adsorbing compound excellent in the adsorption ability and adsorption rate of metal ions in a solution, excellent in mechanical strength and processability, and in a wide range of applications and reusability, and its production And a metal adsorbent using these and a metal adsorber using the adsorbent.
- the present invention may be partially carbamidated, 2,3-dihydroxypropylcellulose or 3_ (2,3-dihydroxypropoxy) _2-hydroxypropylcellulose phosphate.
- An ester compound is provided.
- the present invention may be partially oxidized to carbamide, phosphorous oxidation into 2,3-dihydroxypropylcellulose or 3_ (2,3-dihydroxypropoxy) _2-hydroxypropyl cellulose.
- Phosphoric acid halide, phosphoric acid or salts thereof may be partially carbamidated, 2, 3-dihydroxypropyl cellulose or 3_ (2, 3— Dihydroxypropoxy) —
- the present invention relates to 2,3-dihydroxypropyl cellulose or 3- (2,3-dihydroxypropoxy) -2-hydroxypropyl cell port, which may be partially carbamidated.
- the present invention provides a metal adsorbent containing a phosphoric acid ester and a metal adsorber comprising the metal adsorbent.
- a part of the present invention may be carbamidated, 2,3 dihydroxypropyl cellulose or 3- (2,3 dihydroxypropoxy) 2 hydroxypropylcellulose phosphate ester is a unit.
- Metal adsorbent with high metal adsorption capacity and adsorption rate per weight, excellent mechanical strength, water softening effect such as water, and extremely efficient removal of heavy metals from wastewater etc. Excellent in various shapes and can be easily reused due to its wide range of application. Furthermore, it has excellent antibacterial properties, and when mixed with water, a high viscosity can be obtained.
- FIG. 1 is a diagram showing infrared absorption spectra of cellulose phosphate ester and 2,3-dihydroxypropyl cellulose phosphate ester.
- FIG. 2 is a graph showing the amount of adsorption of 2, 3 dihydroxypropyl cellulose phosphate to various metals at pH 4-6.
- FIG. 3 is a graph showing neutralization titration curves of 2,3 dihydroxypropyl cellulose phosphate and cellulose phosphate ester.
- FIG. 4 is a view showing a metal adsorbing device in which a metal adsorbent of the present invention is packed in a column.
- FIG. 5 is a view showing a metal adsorbing device in a bag shape of the metal adsorbing material of the present invention.
- FIG. 6 is a view showing a metal adsorbing device in which the metal adsorbing material of the present invention is installed inside a water storage tank.
- FIG. 7 is a graph showing antibacterial properties of 2,3-dihydroxypropyl cell mouth-phosphate ester.
- the cellulose derivative phosphate ester of the present invention is a phosphate ester of 2,3-dihydroxypropyl cellulose or 3_ (2,3-dihydroxypropoxy) _2-hydroxypropylcellulose, a part of which is strong. It may be rubamided (aminomethanoic acid ester structure).
- a part of the present invention may be carbamidated, 2, 3 dihydroxypropyl cellulose or 3- (2, 3 dihydroxypropoxy) 2 hydroxypropyl cellulose phosphoric acid
- the ester (hereinafter sometimes referred to as the cellulose derivative phosphate ester of the present invention) may be partially carbamidated, 2,3-dihydroxypropylcellulose or 3- (2,3-dihydroxypropoxy) 2) It is produced by reacting 2-hydroxypropylcellulose with phosphorous oxide, phosphoric acid halide, phosphoric acid or a salt thereof alone or in combination.
- the raw material 2,3-dihydroxypropylcellulose used in the present invention can be produced according to US Pat. No. 4,001,210 or US Pat. No. 4,096,326.
- 3- (2,3 dihydroxypropoxy) 1-2 hydroxypropyl cellulose is a capihalohydrin that reacts 2,3 dihydroxypropyl cellulose with glycidol or 3-halo-1,2-propanediol in the presence of alkali. After reacting to daricidyl ether, it can be produced by acid treatment.
- alkali metal hydroxides such as sodium methoxide methanol solution, potassium hydroxide and sodium hydroxide
- alkali metal carbonates such as sodium carbonate, sodium hydrogen carbonate and potassium carbonate
- triethanolamine Alkanolamines such as sodium methoxide methanol solution and alkali metal hydroxide are preferable.
- the alkali is preferably added in an amount of 0.0005 to 1 mol, more preferably 0.002 to 0.3 mol, relative to 2,3 dihydroxypropylcellulose lg. It is preferable to use an alkaline solution for the reaction.
- the concentration of the alkaline aqueous solution to be used is preferably 0.5 to 10 mol / L, and more preferably 2 to 10 mol / L.
- the reaction temperature is preferably 20 to 150 ° C, and more preferably 4 to 130 ° C.
- the reaction time is 0.:! ⁇ 50 hours, preferably 1-30 hours.
- the epihalohydrin include epichlorohydrin and epip oral mohydrin.
- the acid include perchloric acid, hydrochloric acid, sulfuric acid and the like.
- natural cellulose materials having various forms can be used.
- natural cellulose materials include microcrystalline cellulose, cotton, and wood-based materials.
- examples thereof include cellulose fibers obtained by treating pulp, kenaf, hemp, etc., absorbent cotton, cotton linter, cotton yarn, cotton knitted fabric, cotton woven fabric, filter paper, small piece of wood, and large sawdust.
- 2,3 dihydroxypropyl cellulose or 3- (2,3 dihydroxypropoxy) 2 -Phosphorus oxides and phosphoric acid halides used for the esterification of hydroxypropylcellulose include phosphorous trioxide, phosphorous tetroxide, phosphorous pentoxide, phosphorous oxychloride, phosphorous oxybromide, etc. .
- Examples of phosphoric acid include metaphosphoric acid, pyrophosphoric acid, orthophosphoric acid (sometimes referred to as phosphoric acid), triphosphoric acid, and tetraphosphoric acid.
- the salt include ammonium salt, alkanolamine salt, alkali metal salt and the like.
- ammonium dihydrogen phosphate ammonium dihydrogen phosphate, ammonium dihydrogen phosphate, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, sodium dihydrogen phosphate, and disodium hydrogen phosphate.
- oxides of phosphorus halides of phosphoric acid, phosphoric acid or salts thereof, phosphorus oxychloride, phosphoric acid, diammonium hydrogen phosphate and the like are preferable.
- the reaction ratio of the reaction of 2,3 dihydroxypropylcellulose or 3- (2,3 dihydroxypropoxy) 2-hydroxypropylcellulose with an oxide of phosphorus, a halide of phosphoric acid, phosphoric acid or a salt thereof is 2,3 dihydroxypropylcellulose or 3- (2,3-dihydroxypropoxy) -2-hydroxypropylcellulose lg phosphorous acid, phosphoric acid neurogenic compound, phosphoric acid or its salt SO. 0.4 mol, and further 0.:! To 0.2 mol is preferred.
- the reaction temperature is preferably 0 to 150 ° C, more preferably 50 to 100 ° C.
- the reaction time is preferably 0.5 to 10 hours, more preferably 2 to 6 hours.
- 2,3-dihydroxypropylcellulose or 3_ (2,3-dihydroxypropoxy) _2-hydroxypropylcellulose phosphate partially carbamidated is 2,3-dihydroxypropylcellulose. It can be obtained by phosphorylating 2,3-dihydroxypropylcellulose, in which a part of the hydroxyl group of this is carbamidated, under the same conditions as described above.
- 2,3-Dihydroxypropylcellulose or 3_ (2,3-dihydroxypropoxy) -2 hydroxypropylcellulose partially carbamidated is, for example, 2, 3 dihydro It is obtained by reacting urea with xylpropylcellulose or 3_ (2,3-dihydroxypropoxy) _2-hydroxypropylcellulose.
- a part of it is carbamylated by the coexistence of urea.
- a phosphoric acid ester of 2,3-dihydroxypropylcellulose or 3_ (2,3-dihydroxypropoxy) _2-hydroxypropylcellulose is obtained.
- the amount of urea used for carbamide ⁇ is 0.005 to 0.3 mol per lg of 2,3-dihydroxypropylcellulose or 3_ (2,3-dihydroxypropoxy) 2-hydroxypropylcellulose, and 0.2 It is preferably ⁇ 0.15 mol.
- the phosphorylation rate of the cellulose derivative phosphate ester of the present invention is 8.0 to 15.7% by weight in the case of 2, 3 dihydroxypropyl cellulose phosphate ester which may be partially carbamidated. Particularly preferred is 10.0 to 15.7% by weight.
- the phosphorus content is 2.0 to: 17.4 in terms of metal adsorption capacity. weight 0/0, especially 6. 0: 17 ⁇ 4 by weight 0/0 are preferred.
- the power Rubamido rate of the present invention the cellulose derivative phosphoric acid ester, 0 to 9 as a nitrogen content. 7 weight 0/0, especially from 0 to 8.0% by weight.
- the cellulose derivative phosphate of the present invention has a phosphate group as a metal-adsorbing functional group, and is superior in metal adsorbability to a cation exchange resin metal adsorbent having a carboxynole group or a sulfonic group as an adsorbing functional group. .
- the hydroxyl group of the force lpoxinole group which is a weakly acidic cation exchange functional group, dissociates in the weakly acidic region from alkaline, so it cannot adsorb metal ions in the acidic solution, and the adsorption to the sulfonic acid group is not possible with sodium or Monovalent salts such as potassium are mainly used, and they can hardly adsorb divalent metal ions.
- cation exchange functional groups adsorb divalent metal ions with two functional groups, so there are problems such as 1) slow adsorption rate and 2) low adsorption capacity per unit weight.
- metal adsorbents called chelate resins often contain two or more nitrogen loan pairs such as an amino group or imino group, and are limited to adsorption of heavy metals among divalent metal ions.
- This has the advantage of not adsorbing alkaline earth metals such as magnesium, which also has the disadvantage that it cannot be used for soft water treatment where the purpose is to remove calcium and magnesium.
- the metal-adsorbing functional group of the cellulose derivative phosphoric acid ester of the present invention is a phosphoric acid group, which has two hydroxyl groups adjacent to each other, and one functional group alone is divalent. Since metal ions can be adsorbed, the adsorption rate is fast.
- the phosphate group can dissociate metal ions in the acidic solution because hydrogen in the functional group dissociates even in the acidic region.
- it since it can be adsorbed regardless of the type of monovalent alkali metal, divalent alkaline earth metal, or transition metal, it is not only soft water treatment but also wastewater treatment for the purpose of heavy metal removal or a combination treatment of both. Can also be supported.
- the cellulose derivative phosphate ester of the present invention surprisingly has a metal adsorbing ability superior to that of cellulose phosphate ester.
- the cellulose derivative phosphate ester of the present invention Since the cellulose derivative phosphate ester of the present invention has good reusability, the cellulose derivative phosphate ester of the present invention is a material for adsorbing a metal in an aqueous solution as compared with the cellulose phosphate ester. That is, it is excellent as a metal adsorbent.
- the cellulose derivative phosphoric acid ester of the present invention starting from naturally derived cellulose has a knitted fabric, a woven fabric, a nonwoven fabric, a small lump, a powder, a paper, a thread, a fiber, a cotton, etc. It is excellent in workability and suitable for use as an adsorbent.
- the metal adsorbent may be in the form of powder, knitted fabric, woven fabric, non-woven fabric, paper, thread, fiber, cotton or the like. preferable.
- the surface of the fiber is phosphoric acid. Since the groups are localized, various factors such as particle diameter and moisture permeability that affect the adsorption ability such as cation exchange resin beads are preferably eliminated.
- the cellulose derivative phosphate ester of the present invention has not only metal adsorption ability and reusability but also good processability into various shapes and mechanical strength, and further excellent antibacterial properties and is miscible with water. Then, since high viscosity is obtained, it is useful as a metal adsorbent having a wide range of application.
- the metal adsorbent (raw material) containing the cellulose derivative phosphate of the present invention can be equipped in various forms of metal absorbers by utilizing its excellent metal adsorbing ability.
- a metal adsorption device in which the metal adsorbent is packed in a column Fig. 4
- a metal adsorption device having a metal adsorption bag in which the metal adsorbent is processed into a bag shape Fig. 5
- a metal adsorption device (Fig. 6) that has been processed into a cylindrical or cloth shape and installed inside the reservoir.
- the amount of metal adsorption of the metal adsorbent was measured by the following measurement method.
- the concentration (CO) of the metal in the aqueous solution that does not allow the metal adsorbent to be measured is measured in the same way, and the 2, 3 dihydroxy-propyl cellulose phosphate compound or 3- (2, 3 dihydroxypropoxy) 2 -hydroxy
- the metal adsorption amount (Ad mmol / g) per propyl cellulose phosphate compound lg was calculated by the following formula.
- Ad (C0-Cl) XDXV / W
- 2,3-Dihydroxypropylcellulose phosphate C 26.42 wt. 0 /. H 4. 9 8% by weight, P 14.5% by weight
- Cellulose phosphate C 37. 50 weight 0 /. A 5.77 weight 0 /. , P 4. 38 weight 0/0
- the 2,3-dihydroxypropylcellulose phosphate ester of the present invention has a high adsorption rate.
- 2,3-dihydroxypropylcellulose phosphate has an excellent adsorption capacity for heavy metals and alkaline earth metal ions.
- Kanolesum 0.95 1 .8 8 5 .8 8
- Magnesium 0.96 1 .7 3 5 .3 0
- FIG. 3 shows the neutralization titration curves obtained for the obtained cellulose phosphate ester and 2,3-dihydroxypropyl cellulose phosphate ester.
- 2,3-Dihydroxypropyl cellose phosphate ester introduced more phosphate ester groups per unit sugar than cellose phosphate ester.
- Example 4 Production of 3-dihydroxypropylcellulose phosphate ester (phosphoric acid reaction containing urea and phosphoric acid as reactant)
- phosphoric acid solution prepared by dissolving 0.015 mol of phosphoric acid, 0.02 mol of dihydrogen ammonium phosphate, 0.1 mol of urea and 0.1 ml of water to 1,3-dihydroxypropylcellulose lg, and mix well. After standing at room temperature (25 ° C) for 1 hour, it was completely dried at 90 ° C for 6 hours. Next, the mixture was heated to 150 ° C. and reacted for 2 hours, then washed with water and dried (70 ° C.) to obtain 2,3-dihydroxypropylcellulose phosphate (fiber). The phosphorus content was 10.25% by weight and the nitrogen content was 5.74% by weight. The amount of copper adsorbed at pH 5 was 2.03 mmol / g.
- Example 5 Viscosity of aqueous solution
- ⁇ -cellulose and 0.05 g of 2,3-dihydroxypropyl monocellulose phosphate were mixed with 10 mL of water, and their kinematic viscosities were examined using an Ostwald viscometer.
- the kinematic viscosity of Hiichicellulose was 1.07
- that of 2,3-dihydroxypropyl monocellulose phosphate was 1.20.
- the kinematic viscosity is the force that indicates the viscosity per weight. When converted to the viscosity per mole of each material, single cellulose is used. In 1.07, 2,3-dihydroxypropylcellulose phosphate, it became 2.85, and the viscosity at the same number of moles increased remarkably.
- 2,3-Dihydroxypropyl monocellulose phosphate has a high viscosity because it has many hydroxyl groups.
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Abstract
Description
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Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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US11/575,098 US7741424B2 (en) | 2004-09-29 | 2005-09-26 | Phosphoric ester of cellulose derivative and metal adsorbent comprising the same |
JP2006537710A JP4914722B2 (ja) | 2004-09-29 | 2005-09-26 | セルロース誘導体リン酸エステル及びそれを用いた金属吸着材 |
EP05785987A EP1795541A4 (en) | 2004-09-29 | 2005-09-26 | PHOSPHORIC ESTER OF CELLULOSE DERIVATIVES AND METAL ADSORBENT AGENT COMPRISING SAID ESTER |
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US61370504P | 2004-09-29 | 2004-09-29 | |
US60/613,705 | 2004-09-29 |
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WO2006035696A1 true WO2006035696A1 (ja) | 2006-04-06 |
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US (1) | US7741424B2 (ja) |
EP (1) | EP1795541A4 (ja) |
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WO (1) | WO2006035696A1 (ja) |
Cited By (2)
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JP2017066272A (ja) * | 2015-09-30 | 2017-04-06 | 王子ホールディングス株式会社 | 微細繊維状セルロース含有物 |
JP2020019970A (ja) * | 2019-11-07 | 2020-02-06 | 王子ホールディングス株式会社 | 微細繊維状セルロース含有物 |
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CN104984742B (zh) * | 2015-07-15 | 2017-08-15 | 江南大学 | 一种纤维素基吸附剂的制备方法及其应用 |
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- 2005-09-26 JP JP2006537710A patent/JP4914722B2/ja not_active Expired - Fee Related
- 2005-09-26 US US11/575,098 patent/US7741424B2/en not_active Expired - Fee Related
- 2005-09-26 WO PCT/JP2005/017605 patent/WO2006035696A1/ja active Application Filing
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017066272A (ja) * | 2015-09-30 | 2017-04-06 | 王子ホールディングス株式会社 | 微細繊維状セルロース含有物 |
JP2020019970A (ja) * | 2019-11-07 | 2020-02-06 | 王子ホールディングス株式会社 | 微細繊維状セルロース含有物 |
JP2021121674A (ja) * | 2019-11-07 | 2021-08-26 | 王子ホールディングス株式会社 | 微細繊維状セルロース含有物 |
JP7127005B2 (ja) | 2019-11-07 | 2022-08-29 | 王子ホールディングス株式会社 | 微細繊維状セルロース含有物 |
Also Published As
Publication number | Publication date |
---|---|
JP4914722B2 (ja) | 2012-04-11 |
JPWO2006035696A1 (ja) | 2008-05-15 |
US7741424B2 (en) | 2010-06-22 |
EP1795541A4 (en) | 2011-07-06 |
EP1795541A1 (en) | 2007-06-13 |
US20070217974A1 (en) | 2007-09-20 |
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