JP2021030224A - Adsorption sponge made of plant cellulose, and preparation method and application thereof - Google Patents
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- 239000008104 plant cellulose Substances 0.000 title claims abstract description 73
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 65
- 238000002360 preparation method Methods 0.000 title 1
- 238000004519 manufacturing process Methods 0.000 claims abstract description 45
- 239000012265 solid product Substances 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 239000000243 solution Substances 0.000 claims abstract description 28
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- 230000007935 neutral effect Effects 0.000 claims abstract description 17
- 239000008367 deionised water Substances 0.000 claims abstract description 12
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 12
- 239000002994 raw material Substances 0.000 claims abstract description 7
- 239000012670 alkaline solution Substances 0.000 claims abstract description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 81
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 claims description 54
- 244000025254 Cannabis sativa Species 0.000 claims description 27
- 238000007710 freezing Methods 0.000 claims description 16
- 230000008014 freezing Effects 0.000 claims description 16
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 15
- 238000001291 vacuum drying Methods 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 8
- 230000035484 reaction time Effects 0.000 claims description 6
- 238000004065 wastewater treatment Methods 0.000 claims description 4
- 244000269722 Thea sinensis Species 0.000 claims description 3
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 15
- 150000002500 ions Chemical class 0.000 abstract description 11
- 239000011148 porous material Substances 0.000 abstract description 6
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 abstract description 3
- 239000007795 chemical reaction product Substances 0.000 abstract description 2
- 239000000356 contaminant Substances 0.000 abstract description 2
- 238000004108 freeze drying Methods 0.000 abstract description 2
- 238000005580 one pot reaction Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 238000005057 refrigeration Methods 0.000 abstract 1
- 239000003463 adsorbent Substances 0.000 description 18
- 239000000843 powder Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 11
- 238000001035 drying Methods 0.000 description 9
- 239000012535 impurity Substances 0.000 description 7
- 238000005406 washing Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000002028 Biomass Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000004925 denaturation Methods 0.000 description 2
- 230000036425 denaturation Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 240000003483 Leersia hexandra Species 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 231100000693 bioaccumulation Toxicity 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- DXHPZXWIPWDXHJ-UHFFFAOYSA-N carbon monosulfide Chemical compound [S+]#[C-] DXHPZXWIPWDXHJ-UHFFFAOYSA-N 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000003508 chemical denaturation Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- -1 turfgrass Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
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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
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
-
- 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
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28042—Shaped bodies; Monolithic structures
- B01J20/28045—Honeycomb or cellular structures; Solid foams or sponges
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
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Abstract
Description
本発明は、吸着材及び水処理の技術分野に属し、植物セルロース製吸着スポンジ、その製造方法及びその応用に関する。 The present invention belongs to the technical field of adsorbent and water treatment, and relates to an adsorbent sponge made of plant cellulose, a method for producing the same, and its application.
工業技術の進歩は、人間の生活に便利さをもたらす一方、避けられない環境汚染問題、特に重金属汚染を引き起こしてしまった。重金属は、非生分解性及び生体蓄積性を有するため、水、食物連鎖、呼吸などを通じて人体に入ることができ、体内で蓄積して、更に人体の健康に深刻な害を及ぼす。中国の重工業、電子、航空などのハイテクノロジーの高速発展により、鉱山採掘、金属製錬、化学工業生産、化石燃料の燃焼、農薬と化学肥料の大量使用や家庭ゴミの不法捨てなどの社会活動がますます頻繁になり、重金属の生態環境、特に水生環境への侵入がひどくなっている。水の重金属汚染に対して、吸着法は、効率が高く、コストが低く、操作しやすく及び後処理が簡単であるなどの利点を有するので、最も効果的な処理方法となっている。 While advances in industrial technology have brought convenience to human life, they have caused unavoidable environmental pollution problems, especially heavy metal pollution. Since heavy metals are non-biodegradable and bioaccumulative, they can enter the human body through water, food chain, respiration, etc., accumulate in the body, and further cause serious harm to human health. Due to the rapid development of high technology such as heavy industry, electronics and aviation in China, social activities such as mining, metal smelting, chemical industry production, fossil fuel burning, mass use of pesticides and chemical fertilizers and illegal disposal of household waste are being promoted. Increasingly, heavy metals are invading the ecological environment, especially the aquatic environment. The adsorption method is the most effective treatment method for heavy metal pollution of water because it has advantages such as high efficiency, low cost, easy operation, and easy post-treatment.
吸着材は、吸着技術のコアであり、現在直面している重要な課題は、経済的、効率的、かつ分離・回収が容易な吸着材を製造し、実際応用の必要を満たすように、吸着材の設計・製造において画期的な進歩を実現することである。バイオマス吸着材は、従来の吸着材に比べて、優れる性能を有する。たとえば、草は、再生可能な資源であり、値段がやすくて容易に入手でき、豊富な有機官能基を含有し、重金属イオンと効果的に複合でき、且つ化学変性しやすい。刈り取られた草は廃棄物であり、吸着材の原料とすると、廃棄物の再利用を実現できるとともに、水中の重金属イオンを除去でき、良好な社会的・経済的意味を有する。 Adsorbents are the core of adsorption technology, and the important issue facing us today is to produce adsorbents that are economical, efficient, and easy to separate and recover, and adsorb to meet the needs of practical applications. To achieve breakthroughs in the design and manufacture of materials. The biomass adsorbent has excellent performance as compared with the conventional adsorbent. For example, grass is a renewable resource that is inexpensive, readily available, contains abundant organic functional groups, can be effectively combined with heavy metal ions, and is susceptible to chemical denaturation. The cut grass is a waste, and when it is used as a raw material for an adsorbent, the waste can be reused and heavy metal ions in the water can be removed, which has good social and economic significance.
現在、草系のバイオマス材料の変性処理は、主に鹸化処理、ZnCl2処理、リン酸変性及びバイオ炭への熱分解などの処理方法を有する。上記変性方法で得られた草系の変性吸着材は、ほとんど粉末状であり、重金属イオン例えば鉛、銅、カドミウムなどに対していずれも所定の除去効果を有するが、粉末状の吸着材は、固液分離を実現しにくく、後続処理の難度を増加させ、固定床又は充填柱などの装置を用いて連続流式の廃水処理を行うと、粉末状の材料は、圧力損失及び吸着材損失を引き起こしやすく、処理プロセスのコストを増加させてしまう。 Currently, the denaturation treatment of grass-based biomass materials mainly includes treatment methods such as saponification treatment, ZnCl 2 treatment, phosphoric acid denaturation and thermal decomposition into biochar. The grass-based modified adsorbent obtained by the above modification method is almost in the form of powder, and all have a predetermined removing effect on heavy metal ions such as lead, copper and cadmium. It is difficult to realize solid-liquid separation, the difficulty of subsequent treatment is increased, and when continuous flow type wastewater treatment is performed using a device such as a fixed bed or a filling column, the powdery material causes pressure loss and adsorbent loss. It is easy to cause and increases the cost of the processing process.
特許文献1は、ナノMgO固定化吸着材の製造方法を開示し、金網に対して表面前処理を行い、次にMgイオンを含有するアルカリ性溶液に入れ、一定の温度でその場反応により、水酸化マグネシウムが金網にしっかりと包まれる複合体を得て、熱処理を制御することによって、ナノ酸化マグネシウムが金網に固定化される複合吸着材を形成する。本発明によるナノMgO固定化吸着材の製造方法は、プロセスがシンプルであり、製造される吸着材は、汚水処理に直接使用でき、処理効果が高く、吸着材を回収しやすく、後続の汚水処理プロセスを減少させる。 Patent Document 1 discloses a method for producing a nano-MgO-immobilized adsorbent, performs surface pretreatment on a wire net, then puts it in an alkaline solution containing Mg ions, and water is subjected to an in-situ reaction at a constant temperature. By obtaining a composite in which magnesium oxide is tightly wrapped in the wire mesh and controlling the heat treatment, a composite adsorbent in which nanomagnesium oxide is immobilized on the wire mesh is formed. The method for producing a nano-MgO-immobilized adsorbent according to the present invention has a simple process, and the produced adsorbent can be directly used for sewage treatment, has a high treatment effect, is easy to recover the adsorbent, and subsequently treats sewage. Reduce the process.
従来技術の上記欠陥や不備を解消するために、本発明は、植物セルロース製吸着スポンジ、その製造方法及びその応用を提供することを目的とする。 In order to eliminate the above-mentioned defects and deficiencies of the prior art, it is an object of the present invention to provide an adsorption sponge made of plant cellulose, a method for producing the same, and an application thereof.
上記目的を実現するために、本発明の用いる技術方案は、以下のとおりである。
第1態様では、本発明は、
(1)植物セルロース原料を粉砕又は破砕し、植物セルロース粉末を得るステップと、
(2)ステップ(1)で処理された植物セルロース粉末を秤取し、アルカリ溶液及び二硫化炭素を加えて撹拌しながら反応させ、反応終了後、固体生成物を収集して脱イオン水で洗浄するステップと、
(3)ステップ(2)で処理された固体生成物を混合して所定の形状の容器に入れ、次に完全に固まるまで冷凍した後、冷凍真空乾燥を行って、前記植物セルロース製吸着スポンジを得るステップとを含む植物セルロース製吸着スポンジの製造方法を提供する。前記製造方法は、ステップ(3)で、混合後の固体生成物を要求される形状及びサイズの容器に入れることによって、形状及び大きさが制御可能な植物セルロース製吸着スポンジを製造でき、冷凍乾燥処理によって、植物セルロース製吸着スポンジの互いに連通する多孔質構造の形成を確保する一方、乾燥などの乾燥手段が多孔質構造の形成を実現できない。前記製造方法で製造される植物セルロース製吸着スポンジの1種は、図1に示すように、その機械的性質に優れ、割れにくく、人為的に分けても、良好な形状を維持でき、且つ分け過程で屑が生じることがなく、水に当たっても割れにくく、化学汚泥が生じることがなく、互いに連通する豊富な細孔構造を有し、吸水能力が強いとともに、重金属イオンなどの吸着剤の高速移動に寄与し、重金属イオンと活性吸着部位との接触を加速し、吸着時間を縮み、吸着効果を強化させる。
The technical plan used by the present invention in order to realize the above object is as follows.
In the first aspect, the present invention
(1) A step of crushing or crushing a plant cellulose raw material to obtain a plant cellulose powder, and
(2) The plant cellulose powder treated in step (1) is weighed, an alkaline solution and carbon disulfide are added and reacted with stirring, and after the reaction is completed, the solid product is collected and washed with deionized water. Steps to do and
(3) The solid products treated in step (2) are mixed and placed in a container having a predetermined shape, then frozen until completely solidified, and then subjected to freezing vacuum drying to obtain the plant cellulose adsorption sponge. Provided is a method for producing an adsorption sponge made of plant cellulose, which comprises a step of obtaining. In the production method, a plant cellulose adsorption sponge whose shape and size can be controlled can be produced by putting the mixed solid product in a container having a required shape and size in step (3), and freeze-drying. The treatment ensures the formation of a porous structure in which the adsorption sponges made of plant cellulose communicate with each other, but the drying means such as drying cannot realize the formation of the porous structure. As shown in FIG. 1, one kind of plant cellulose adsorption sponge produced by the above-mentioned production method has excellent mechanical properties, is hard to break, can maintain a good shape even when artificially separated, and is separated. No debris is generated in the process, it is hard to break even when it hits water, no chemical sludge is generated, it has abundant pore structure that communicates with each other, it has strong water absorption capacity, and high-speed movement of adsorbents such as heavy metal ions. Accelerates the contact between heavy metal ions and the active adsorption site, shortens the adsorption time, and strengthens the adsorption effect.
本発明の前記製造方法の好適な実施形態としては、前記ステップ(2)では、アルカリ溶液は、水酸化ナトリウム溶液であり、植物セルロース粉末、水酸化ナトリウム溶液及び二硫化炭素の比率は、植物セルロース粉末:水酸化ナトリウム溶液:二硫化炭素=0.5〜2g:40〜100mL:0.5〜3mLであり、水酸化ナトリウム溶液の濃度は、5%〜30%であり、本発明の前記製造方法のさらに好適な実施形態としては、前記ステップ(2)では、植物セルロース粉末、水酸化ナトリウム溶液及び二硫化炭素の比率は、植物セルロース粉末:水酸化ナトリウム溶液:二硫化炭素=1g:50mL:3mLであり、水酸化ナトリウム溶液の濃度は、14%である。出願者は、試験したところ、植物セルロース粉末、水酸化ナトリウム溶液及び二硫化炭素の比率が植物セルロース粉末:水酸化ナトリウム溶液:二硫化炭素=0.5〜2g:40〜100mL:0.5〜3mLであり、水酸化ナトリウム溶液の濃度が5%〜30%である場合、豊富な細孔構造を有する植物セルロース製吸着スポンジを順調に製造でき、特に、植物セルロース粉末、水酸化ナトリウム溶液及び二硫化炭素の比率が植物セルロース粉末:水酸化ナトリウム溶液:二硫化炭素=1g:50mL:3mLであり、水酸化ナトリウム溶液の濃度が14%である場合、製造される植物セルロース製吸着スポンジは、外観や形態がより美しく、細孔構造がより豊富になり、機械的性質がより良好になり、水中の重金属イオンに対する除去能力がより強いことを発見した。 In a preferred embodiment of the production method of the present invention, in the step (2), the alkaline solution is a sodium hydroxide solution, and the ratio of the plant cellulose powder, the sodium hydroxide solution and the carbon disulfide is the plant cellulose. Powder: Sodium hydroxide solution: Carbon disulfide = 0.5 to 2 g: 40 to 100 mL: 0.5 to 3 mL, and the concentration of the sodium hydroxide solution is 5% to 30%. As a more preferred embodiment of the method, in step (2), the ratio of plant cellulose powder, sodium hydroxide solution and carbon disulfide is: plant cellulose powder: sodium hydroxide solution: carbon disulfide = 1 g: 50 mL: It is 3 mL and the concentration of the sodium hydroxide solution is 14%. Applicants have tested and found that the ratio of plant cellulose powder, sodium hydroxide solution and carbon disulfide is plant cellulose powder: sodium hydroxide solution: carbon disulfide = 0.5-2 g: 40-100 mL: 0.5- When it is 3 mL and the concentration of the sodium hydroxide solution is 5% to 30%, an adsorption sponge made of plant cellulose having abundant pore structure can be smoothly produced, and in particular, plant cellulose powder, sodium hydroxide solution and two. When the ratio of carbon sulfide is plant cellulose powder: sodium hydroxide solution: carbon disulfide = 1 g: 50 mL: 3 mL and the concentration of sodium hydroxide solution is 14%, the produced plant cellulose adsorption sponge has an appearance. We found that the morphology and morphology were more beautiful, the pore structure was richer, the mechanical properties were better, and the ability to remove heavy metal ions in water was stronger.
本発明の前記製造方法の好適な実施形態としては、前記ステップ(2)では、反応の時間は、6〜24hであり、本発明の前記製造方法のさらに好適な実施形態としては、前記ステップ(2)では、反応の時間は、6hである。出願者は、試験したところ、反応時間が6〜24hである場合、形状が規則的な植物セルロース製吸着スポンジを製造でき、反応時間を更に延長させることに比較して、材料の効果的な成形及び低い時間コストを確保でき、特に反応時間が6hである場合、製造される植物セルロース製吸着スポンジは、収率が高く、細孔が豊富で密度が高く、内部構造がより規則的かつ均一になり、弾性がより高いことを発見した。 As a preferred embodiment of the production method of the present invention, the reaction time is 6 to 24 hours in the step (2), and as a more preferred embodiment of the production method of the present invention, the step (2) In 2), the reaction time is 6 hours. Applicants have tested that when the reaction time is 6 to 24 hours, an adsorbent sponge made of plant cellulose having a regular shape can be produced, and the effective molding of the material is compared with further extending the reaction time. And low time cost can be ensured, especially when the reaction time is 6h, the produced plant cellulose adsorption sponge has a high yield, abundant pores and a high density, and a more regular and uniform internal structure. I found that it had higher elasticity.
本発明の前記製造方法の好適な実施形態としては、前記ステップ(2)では、反応を室温で行う。 In a preferred embodiment of the production method of the present invention, in step (2), the reaction is carried out at room temperature.
本発明の前記製造方法の好適な実施形態としては、前記ステップ(2)では、固体生成物を脱イオン水で中性になるまで洗浄する。 In a preferred embodiment of the production method of the present invention, in step (2), the solid product is washed with deionized water until neutral.
本発明の前記製造方法の好適な実施形態としては、前記ステップ(2)では、反応終了後、固体生成物を遠心法で収集し、遠心回転数は、4000〜8000rpmである。 In a preferred embodiment of the production method of the present invention, in step (2), after completion of the reaction, the solid product is collected by a centrifugal method, and the centrifugal rotation speed is 4000 to 8000 rpm.
本発明の前記製造方法の好適な実施形態としては、前記ステップ(3)では、固体生成物を−20℃以下の環境で完全に固まるまで冷凍し、本発明の前記製造方法のさらに好適な実施形態としては、前記ステップ(3)では、固体生成物を−20℃〜−80℃環境で完全に固まるまで冷凍する。 As a preferred embodiment of the production method of the present invention, in the step (3), the solid product is frozen in an environment of −20 ° C. or lower until it is completely solidified, and a more preferred embodiment of the production method of the present invention. In the form, in step (3), the solid product is frozen in an environment of −20 ° C. to −80 ° C. until it is completely solidified.
本発明の前記製造方法の好適な実施形態としては、前記ステップ(1)では、植物セルロース原料は、草又は茶葉である。出願者は、植物セルロースが大量に含まれる、芝草、藁、茶葉などの植物セルロース原料を上記製造方法で吸着スポンジに製造できることを発見した。 In a preferred embodiment of the production method of the present invention, in the step (1), the plant cellulose raw material is grass or tea leaves. The applicant has discovered that a plant cellulose raw material such as turfgrass, straw, and tea leaves, which contains a large amount of plant cellulose, can be produced in an adsorption sponge by the above production method.
本発明の前記製造方法のさらに好適な実施形態としては、前記ステップ(1)では、植物セルロース原料は、刈り取られた芝草である。 As a more preferred embodiment of the production method of the present invention, in the step (1), the plant cellulose raw material is a cut turf grass.
第2態様では、本発明は、上記製造方法で製造される植物セルロース製吸着スポンジを提供する。 In the second aspect, the present invention provides an adsorption sponge made of plant cellulose produced by the above production method.
第3態様では、本発明は、上記植物セルロース製吸着スポンジの、廃水処理における応用を提供する。上記植物セルロース製吸着スポンジは、固定床又は充填柱などの水処理装置の好適なフィラーとして、廃水中の重金属イオンなどの汚染物を吸着することに使用できる。 In a third aspect, the present invention provides an application of the above plant cellulose adsorption sponge in wastewater treatment. The above-mentioned adsorption sponge made of vegetable cellulose can be used for adsorbing contaminants such as heavy metal ions in wastewater as a suitable filler for a water treatment device such as a fixed floor or a filling column.
本発明は、従来技術に比べて、以下の利点及び有益な効果を有する。
(1)本発明の植物セルロース製吸着スポンジの製造方法は、実際のニーズに応じて形状及び大きさが制御可能な植物セルロース製吸着スポンジを製造できる。
The present invention has the following advantages and beneficial effects as compared with the prior art.
(1) The method for producing a plant cellulose adsorption sponge of the present invention can produce a plant cellulose adsorption sponge whose shape and size can be controlled according to actual needs.
(2)本発明の植物セルロース製吸着スポンジの製造方法で製造される植物セルロース製吸着スポンジは、機械的性質に優れ、水に当たっても破砕しにくく、化学汚泥を生じることがない。 (2) The plant cellulose adsorption sponge produced by the method for producing a plant cellulose adsorption sponge of the present invention has excellent mechanical properties, is not easily crushed even when exposed to water, and does not generate chemical sludge.
(3)本発明の植物セルロース製吸着スポンジの製造方法で製造される植物セルロース製吸着スポンジは、互いに連通する豊富の細孔構造を有し、吸着能力が強く、重金属イオンなどの吸着剤の高速移動に寄与し、重金属イオンと活性吸着部位のとの接触を加速し、吸着時間を縮み、吸着効果を強化させ、従来技術の他のバイオマス吸着材に比べて、水中の重金属イオンをよく除去できる。 (3) The plant cellulose adsorption sponge produced by the method for producing the plant cellulose adsorption sponge of the present invention has an abundant pore structure that communicates with each other, has a strong adsorption capacity, and has a high speed of an adsorbent such as heavy metal ion. It contributes to movement, accelerates the contact between heavy metal ions and the active adsorption site, shortens the adsorption time, enhances the adsorption effect, and can remove heavy metal ions in water better than other biomass adsorbents of the prior art. ..
(4)本発明の植物セルロース製吸着スポンジの製造方法で製造される植物セルロース製吸着スポンジは、従来の粉末状変性植物セルロース材料に比べて、固液分離を実現しやすく、操作性が高く、実際の水処理工事に適用され、且つ廃水処理プロセスで、汚泥をぜんぜん生じないことを実現する。 (4) The plant cellulose adsorption sponge produced by the method for producing a plant cellulose adsorption sponge of the present invention is easier to realize solid-liquid separation and has higher operability than the conventional powdery modified plant cellulose material. It is applied to actual water treatment work and realizes that no sludge is generated in the waste water treatment process.
(5)本発明の植物セルロース製吸着スポンジの製造方法は、従来のバイオマス変性処理技術に比べて、アルカリ化前処理を行う必要がなく、ワンステップ反応によって、最終反応生成物を得ることができ、材料の製造工程を大幅に縮み、時間を節約し、経済的コスト及び人件費を削減する。 (5) Compared with the conventional biomass modification treatment technique, the method for producing an adsorption sponge made of plant cellulose of the present invention does not require pre-alkalization, and the final reaction product can be obtained by a one-step reaction. , Significantly reduce the manufacturing process of materials, save time, reduce economic cost and labor cost.
本発明の目的、技術方案及び利点についてよく説明するために、以下、発明を実施するための形態を組み合わせて本発明について更に説明する。 In order to better explain the object, technical plan and advantages of the present invention, the present invention will be further described below in combination with modes for carrying out the invention.
(実施例1)
本発明の植物セルロース製吸着スポンジの製造方法の一実施例は、
(1)収集した芝草を水で洗浄して不純物を除去し、次に乾燥させ、粉砕し、草粉末を得るステップと、
(2)ステップ(1)で処理された草粉末1gを秤取し、質量分率14%の水酸化ナトリウム溶液50mL及び二硫化炭素3mLを加え、室温で6h連続的に撹拌しながら反応させ、反応終了後、8000rpmの回転数で反応後の固体生成物を遠心収集し、固体生成物を中性になるまで脱イオン水で繰り返して洗浄するステップと、
(3)ステップ(2)で処理された中性の固体生成物を混合して所定の形状の容器、例えば50mL、100mLなど、異なる仕様のビーカーに入れ、次に−20℃、−50℃、−80℃又は−198℃で完全に固まるまで急速冷凍した後、冷凍真空乾燥を行って、芝草製吸着スポンジ、すなわち前記植物セルロース製吸着スポンジを得るステップとを含んだ。
(Example 1)
An example of the method for producing an adsorption sponge made of plant cellulose of the present invention is
(1) The steps of washing the collected turf grass with water to remove impurities, then drying and crushing to obtain grass powder,
(2) 1 g of the grass powder treated in step (1) was weighed, 50 mL of a sodium hydroxide solution having a mass fraction of 14% and 3 mL of carbon disulfide were added, and the mixture was reacted at room temperature with continuous stirring for 6 hours. After completion of the reaction, the solid product after the reaction is centrifuged at a rotation speed of 8000 rpm, and the solid product is repeatedly washed with deionized water until it becomes neutral.
(3) The neutral solid product treated in step (2) is mixed and placed in a container of a predetermined shape, for example, a beaker having different specifications such as 50 mL and 100 mL, and then placed at −20 ° C., −50 ° C., After quick freezing at −80 ° C. or −198 ° C. until it was completely solidified, it was subjected to freezing vacuum drying to obtain a turfgrass adsorption sponge, that is, the plant cellulose adsorption sponge.
(実施例2)
本発明の植物セルロース製吸着スポンジの製造方法の一実施例は、
(1)収集した芝草を水で洗浄して不純物を除去し、次に乾燥させ、粉砕し、草粉末を得るステップと、
(2)ステップ(1)で処理された草粉末0.5gを秤取し、質量分率5%の水酸化ナトリウム溶液40mL及び二硫化炭素0.5mLを加え、室温で6h連続的に撹拌しながら反応させ、反応終了後、4000rpmの回転数で反応後の固体生成物を遠心収集し、固体生成物を中性になるまで脱イオン水で繰り返して洗浄するステップと、
(3)ステップ(2)で処理された中性の固体生成物を混合して所定の形状の容器、例えば50mL、100mLなど、異なる仕様のビーカーに入れ、次に−20℃、−50℃、−80℃又は−198℃で完全に固まるまで急速冷凍した後、冷凍真空乾燥を行って、芝草製吸着スポンジ、すなわち前記植物セルロース製吸着スポンジを得るステップとを含んだ。
(Example 2)
An example of the method for producing an adsorption sponge made of plant cellulose of the present invention is
(1) The steps of washing the collected turf grass with water to remove impurities, then drying and crushing to obtain grass powder,
(2) 0.5 g of the grass powder treated in step (1) was weighed, 40 mL of a sodium hydroxide solution having a mass fraction of 5% and 0.5 mL of carbon disulfide were added, and the mixture was continuously stirred at room temperature for 6 hours. After the reaction is completed, the solid product after the reaction is centrifuged at 4000 rpm, and the solid product is repeatedly washed with deionized water until it becomes neutral.
(3) The neutral solid product treated in step (2) is mixed and placed in a container of a predetermined shape, for example, a beaker having different specifications such as 50 mL and 100 mL, and then placed at −20 ° C., −50 ° C., After quick freezing at −80 ° C. or −198 ° C. until it was completely solidified, it was subjected to freezing vacuum drying to obtain a turfgrass adsorption sponge, that is, the plant cellulose adsorption sponge.
(実施例3)
本発明の植物セルロース製吸着スポンジの製造方法の一実施例は、
(1)収集した芝草を水で洗浄して不純物を除去し、次に乾燥させ、粉砕し、草粉末を得るステップと、
(2)ステップ(1)で処理された草粉末0.5gを秤取し、質量分率15%の水酸化ナトリウム溶液70mL及び二硫化炭素2mLを加え、室温で12h連続的に撹拌しながら反応させ、反応終了後、6000rpmの回転数で反応後の固体生成物を遠心収集し、固体生成物を中性になるまで脱イオン水で繰り返して洗浄するステップと、
(3)ステップ(2)で処理された中性の固体生成物を混合して所定の形状の容器、例えば50mL、100mLなど、異なる仕様のビーカーに入れ、次に−20℃、−50℃、−80℃又は−198℃で完全に固まるまで急速冷凍した後、冷凍真空乾燥を行って、芝草製吸着スポンジ、すなわち前記植物セルロース製吸着スポンジを得るステップとを含んだ。
(Example 3)
An example of the method for producing an adsorption sponge made of plant cellulose of the present invention is
(1) The steps of washing the collected turf grass with water to remove impurities, then drying and crushing to obtain grass powder,
(2) 0.5 g of the grass powder treated in step (1) was weighed, 70 mL of a sodium hydroxide solution having a mass fraction of 15% and 2 mL of carbon disulfide were added, and the reaction was carried out at room temperature with continuous stirring for 12 hours. After the reaction is completed, the solid product after the reaction is centrifuged at a rotation speed of 6000 rpm, and the solid product is repeatedly washed with deionized water until it becomes neutral.
(3) The neutral solid product treated in step (2) is mixed and placed in a container of a predetermined shape, for example, a beaker having different specifications such as 50 mL and 100 mL, and then placed at −20 ° C., −50 ° C., After quick freezing at −80 ° C. or −198 ° C. until it was completely solidified, it was subjected to freezing vacuum drying to obtain a turfgrass adsorption sponge, that is, the plant cellulose adsorption sponge.
(実施例4)
本発明の植物セルロース製吸着スポンジの製造方法の一実施例は、
(1)収集した芝草を水で洗浄して不純物を除去し、次に乾燥させ、粉砕し、草粉末を得るステップと、
(2)ステップ(1)で処理された草粉末0.5gを秤取し、質量分率30%の水酸化ナトリウム溶液100mL及び二硫化炭素3mLを加え、室温で24h連続的に撹拌しながら反応させ、反応終了後、4000rpmの回転数で反応後の固体生成物を遠心収集し、固体生成物を中性になるまで脱イオン水で繰り返して洗浄するステップと、
(3)ステップ(2)で処理された中性の固体生成物を混合して所定の形状の容器、例えば50mL、100mLなど、異なる仕様のビーカーに入れ、次に−20℃、−50℃、−80℃又は−198℃で完全に固まるまで急速冷凍した後、冷凍真空乾燥を行って、芝草製吸着スポンジ、すなわち前記植物セルロース製吸着スポンジを得るステップとを含んだ。
(Example 4)
An example of the method for producing an adsorption sponge made of plant cellulose of the present invention is
(1) The steps of washing the collected turf grass with water to remove impurities, then drying and crushing to obtain grass powder,
(2) 0.5 g of the grass powder treated in step (1) is weighed, 100 mL of a sodium hydroxide solution having a mass fraction of 30% and 3 mL of carbon disulfide are added, and the reaction is carried out at room temperature with continuous stirring for 24 hours. After the reaction is completed, the solid product after the reaction is centrifuged at 4000 rpm, and the solid product is repeatedly washed with deionized water until it becomes neutral.
(3) The neutral solid product treated in step (2) is mixed and placed in a container of a predetermined shape, for example, a beaker having different specifications such as 50 mL and 100 mL, and then placed at −20 ° C., −50 ° C., After quick freezing at −80 ° C. or −198 ° C. until it was completely solidified, it was subjected to freezing vacuum drying to obtain a turfgrass adsorption sponge, that is, the plant cellulose adsorption sponge.
(実施例5)
本発明の植物セルロース製吸着スポンジの製造方法の一実施例は、
(1)収集した芝草を水で洗浄して不純物を除去し、次に乾燥させ、粉砕し、草粉末を得るステップと、
(2)ステップ(1)で処理された草粉末2gを秤取し、質量分率5%の水酸化ナトリウム溶液40mL及び二硫化炭素0.5mLを加え、室温で6h連続的に撹拌しながら反応させ、反応終了後、8000rpmの回転数で反応後の固体生成物を遠心収集し、固体生成物を中性になるまで脱イオン水で繰り返して洗浄するステップと、
(3)ステップ(2)で処理された中性の固体生成物を混合して所定の形状の容器、例えば50mL、100mLなど、異なる仕様のビーカーに入れ、次に−20℃、−50℃、−80℃又は−198℃で完全に固まるまで急速冷凍した後、冷凍真空乾燥を行って、芝草製吸着スポンジ、すなわち前記植物セルロース製吸着スポンジを得るステップとを含んだ。
(Example 5)
An example of the method for producing an adsorption sponge made of plant cellulose of the present invention is
(1) The steps of washing the collected turf grass with water to remove impurities, then drying and crushing to obtain grass powder,
(2) Weigh 2 g of the grass powder treated in step (1), add 40 mL of sodium hydroxide solution having a mass fraction of 5% and 0.5 mL of carbon disulfide, and react with continuous stirring at room temperature for 6 hours. After the reaction is completed, the solid product after the reaction is centrifuged at a rotation speed of 8000 rpm, and the solid product is repeatedly washed with deionized water until it becomes neutral.
(3) The neutral solid product treated in step (2) is mixed and placed in a container of a predetermined shape, for example, a beaker having different specifications such as 50 mL and 100 mL, and then placed at −20 ° C., −50 ° C., After quick freezing at −80 ° C. or −198 ° C. until it was completely solidified, it was subjected to freezing vacuum drying to obtain a turfgrass adsorption sponge, that is, the plant cellulose adsorption sponge.
(実施例6)
本発明の植物セルロース製吸着スポンジの製造方法の一実施例は、
(1)収集した芝草を水で洗浄して不純物を除去し、次に乾燥させ、粉砕し、草粉末を得るステップと、
(2)ステップ(1)で処理された草粉末2gを秤取し、質量分率20%の水酸化ナトリウム溶液80mL及び二硫化炭素1.5mLを加え、室温で15h連続的に撹拌しながら反応させ、反応終了後、8000rpmの回転数で反応後の固体生成物を遠心収集し、固体生成物を中性になるまで脱イオン水で繰り返して洗浄するステップと、
(3)ステップ(2)で処理された中性の固体生成物を混合して所定の形状の容器、例えば50mL、100mLなど、異なる仕様のビーカーに入れ、次に−20℃、−50℃、−80℃又は−198℃で完全に固まるまで急速冷凍した後、冷凍真空乾燥を行って、芝草製吸着スポンジ、すなわち前記植物セルロース製吸着スポンジを得るステップとを含んだ。
(Example 6)
An example of the method for producing an adsorption sponge made of plant cellulose of the present invention is
(1) The steps of washing the collected turf grass with water to remove impurities, then drying and crushing to obtain grass powder,
(2) Weigh 2 g of the grass powder treated in step (1), add 80 mL of sodium hydroxide solution having a mass fraction of 20% and 1.5 mL of carbon disulfide, and react with continuous stirring at room temperature for 15 hours. After the reaction is completed, the solid product after the reaction is centrifuged at a rotation speed of 8000 rpm, and the solid product is repeatedly washed with deionized water until it becomes neutral.
(3) The neutral solid product treated in step (2) is mixed and placed in a container of a predetermined shape, for example, a beaker having different specifications such as 50 mL and 100 mL, and then placed at −20 ° C., −50 ° C., After quick freezing at −80 ° C. or −198 ° C. until it was completely solidified, it was subjected to freezing vacuum drying to obtain a turfgrass adsorption sponge, that is, the plant cellulose adsorption sponge.
(実施例7)
本発明の植物セルロース製吸着スポンジの製造方法の一実施例は、
(1)収集した芝草を水で洗浄して不純物を除去し、次に乾燥させ、粉砕し、草粉末を得るステップと、
(2)ステップ(1)で処理された草粉末2gを秤取し、質量分率30%の水酸化ナトリウム溶液100mL及び二硫化炭素3mLを加え、室温で24h連続的に撹拌しながら反応させ、反応終了後、8000rpmの回転数で反応後の固体生成物を遠心収集し、固体生成物を中性になるまで脱イオン水で繰り返して洗浄するステップと、
(3)ステップ(2)で処理された中性の固体生成物を混合して所定の形状の容器、例えば50mL、100mLなど、異なる仕様のビーカーに入れ、次に−20℃、−50℃、−80℃又は−198℃で完全に固まるまで急速冷凍した後、冷凍真空乾燥を行って、芝草製吸着スポンジ、すなわち前記植物セルロース製吸着スポンジを得るステップとを含んだ。
(Example 7)
An example of the method for producing an adsorption sponge made of plant cellulose of the present invention is
(1) The steps of washing the collected turf grass with water to remove impurities, then drying and crushing to obtain grass powder,
(2) 2 g of the grass powder treated in step (1) was weighed, 100 mL of a sodium hydroxide solution having a mass fraction of 30% and 3 mL of carbon disulfide were added, and the mixture was reacted at room temperature with continuous stirring for 24 hours. After completion of the reaction, the solid product after the reaction is centrifuged at a rotation speed of 8000 rpm, and the solid product is repeatedly washed with deionized water until it becomes neutral.
(3) The neutral solid product treated in step (2) is mixed and placed in a container of a predetermined shape, for example, a beaker having different specifications such as 50 mL and 100 mL, and then placed at −20 ° C., −50 ° C., After quick freezing at −80 ° C. or −198 ° C. until it was completely solidified, it was subjected to freezing vacuum drying to obtain a turfgrass adsorption sponge, that is, the plant cellulose adsorption sponge.
なお、以上の実施例は、本発明の技術方案を説明するためのものに過ぎず、本発明の特許請求の範囲を制限するものではなく、好適な実施例を参照しながら、本発明について詳細に説明したが、当業者であれば、本発明の技術方案の実質及び範囲から逸脱することなく、本発明の技術方案に対して補正するか、又は等同置換を行うことができる。
It should be noted that the above examples are merely for explaining the technical plan of the present invention, do not limit the scope of claims of the present invention, and describe the present invention in detail with reference to suitable examples. As described above, a person skilled in the art can make amendments to the technical plan of the present invention, or make the same substitution without departing from the substance and scope of the technical plan of the present invention.
Claims (10)
(2)ステップ(1)で処理された植物セルロース粉末を秤取し、アルカリ溶液及び二硫化炭素を加えて撹拌しながら反応させ、反応終了後、固体生成物を収集して脱イオン水で洗浄するステップと、
(3)ステップ(2)で処理された固体生成物を混合して所定の形状の容器に入れ、次に完全に固まるまで冷凍した後、冷凍真空乾燥を行って、前記植物セルロース製吸着スポンジを得るステップとを含む、ことを特徴とする植物セルロース製吸着スポンジの製造方法。 (1) A step of crushing or crushing plant cellulose to obtain plant cellulose powder, and
(2) The plant cellulose powder treated in step (1) is weighed, an alkaline solution and carbon disulfide are added and reacted with stirring, and after the reaction is completed, the solid product is collected and washed with deionized water. Steps to do and
(3) The solid products treated in step (2) are mixed and placed in a container having a predetermined shape, then frozen until completely solidified, and then subjected to freezing vacuum drying to obtain the plant cellulose adsorption sponge. A method for producing an adsorption sponge made of plant cellulose, which comprises a step of obtaining.
Application of the plant cellulose adsorption sponge according to claim 9 in wastewater treatment.
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CN115301218A (en) * | 2022-06-29 | 2022-11-08 | 江苏宿迁润泰环保科技有限公司 | Waste gas adsorbing material based on lignocellulose sponge and application thereof |
WO2023070185A1 (en) * | 2021-10-25 | 2023-05-04 | Cnpem - Centro Nacional De Pesquisa Em Energia E Materiais | Porous foam for retaining organic and inorganic compounds, method for producing same and uses thereof |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4634470A (en) * | 1983-12-26 | 1987-01-06 | Asahi Kasei Kogyo Kabushiki Kaisha | Cellulose dope, process for preparation and method for application thereof |
JPH0457836A (en) * | 1990-06-27 | 1992-02-25 | Fukui Kagaku Kogyo Kk | Spherical porous cellulose particle comprising chitin or deacetylated chitin and cellulose, and preparation thereof |
CN101224415A (en) * | 2007-09-30 | 2008-07-23 | 南开大学 | Low density lipoprotein adsorbent for extrinsic blood perfusion and preparing method thereof |
JP2008231258A (en) * | 2007-03-20 | 2008-10-02 | Univ Of Tokyo | Cellulose aerogel and method for producing the same |
JP2013023637A (en) * | 2011-07-25 | 2013-02-04 | Nitto Denko Corp | Method for producing cellulosic porous product |
JP2019048987A (en) * | 2013-09-27 | 2019-03-28 | 株式会社カネカ | Support for ligand immobilization, adsorbent, and method for producing support for ligand immobilization |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1034938A (en) * | 1988-01-27 | 1989-08-23 | 中国纺织大学 | The preparation of expansion cellulose sponge |
CN101942112B (en) * | 2010-09-09 | 2012-07-25 | 宁波尼可家用品有限公司 | Bamboo pulp sponge product and preparation method thereof |
CN105061796B (en) * | 2015-08-27 | 2018-07-27 | 中国科学院东北地理与农业生态研究所 | A kind of preparation method and application of modification of chitosan sponge structure material |
CN107417980B (en) * | 2017-06-23 | 2019-05-17 | 天长市博资清洁科技有限公司 | The preparation method of wood pulp sponge |
CN108912328B (en) * | 2018-08-01 | 2021-11-09 | 南方科技大学 | Preparation method of heavy metal ion chelating agent |
-
2019
- 2019-08-15 CN CN201910756381.9A patent/CN110354819B/en active Active
-
2020
- 2020-08-07 JP JP2020134307A patent/JP6871657B2/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4634470A (en) * | 1983-12-26 | 1987-01-06 | Asahi Kasei Kogyo Kabushiki Kaisha | Cellulose dope, process for preparation and method for application thereof |
JPH0457836A (en) * | 1990-06-27 | 1992-02-25 | Fukui Kagaku Kogyo Kk | Spherical porous cellulose particle comprising chitin or deacetylated chitin and cellulose, and preparation thereof |
JP2008231258A (en) * | 2007-03-20 | 2008-10-02 | Univ Of Tokyo | Cellulose aerogel and method for producing the same |
CN101224415A (en) * | 2007-09-30 | 2008-07-23 | 南开大学 | Low density lipoprotein adsorbent for extrinsic blood perfusion and preparing method thereof |
JP2013023637A (en) * | 2011-07-25 | 2013-02-04 | Nitto Denko Corp | Method for producing cellulosic porous product |
JP2019048987A (en) * | 2013-09-27 | 2019-03-28 | 株式会社カネカ | Support for ligand immobilization, adsorbent, and method for producing support for ligand immobilization |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2023070185A1 (en) * | 2021-10-25 | 2023-05-04 | Cnpem - Centro Nacional De Pesquisa Em Energia E Materiais | Porous foam for retaining organic and inorganic compounds, method for producing same and uses thereof |
CN115301218A (en) * | 2022-06-29 | 2022-11-08 | 江苏宿迁润泰环保科技有限公司 | Waste gas adsorbing material based on lignocellulose sponge and application thereof |
CN115301218B (en) * | 2022-06-29 | 2024-03-08 | 江苏宿迁润泰环保科技有限公司 | Lignocellulose sponge-based waste gas adsorption material and application thereof |
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