JPH08245701A - Highly transparent hydroxyalkyl cellulose and its production - Google Patents
Highly transparent hydroxyalkyl cellulose and its productionInfo
- Publication number
- JPH08245701A JPH08245701A JP4856295A JP4856295A JPH08245701A JP H08245701 A JPH08245701 A JP H08245701A JP 4856295 A JP4856295 A JP 4856295A JP 4856295 A JP4856295 A JP 4856295A JP H08245701 A JPH08245701 A JP H08245701A
- Authority
- JP
- Japan
- Prior art keywords
- cellulose
- alkali metal
- metal hydroxide
- hydroxyalkyl
- glucose unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920013821 hydroxy alkyl cellulose Polymers 0.000 title claims description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- 229920002678 cellulose Polymers 0.000 claims abstract description 27
- 239000001913 cellulose Substances 0.000 claims abstract description 27
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 claims abstract description 22
- 238000006266 etherification reaction Methods 0.000 claims abstract description 18
- 238000006467 substitution reaction Methods 0.000 claims abstract description 18
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims abstract description 17
- 239000007864 aqueous solution Substances 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000003960 organic solvent Substances 0.000 claims abstract description 10
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000011259 mixed solution Substances 0.000 claims abstract description 8
- 230000003472 neutralizing effect Effects 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims description 15
- 239000002994 raw material Substances 0.000 claims description 7
- 125000002768 hydroxyalkyl group Chemical group 0.000 claims description 3
- 239000003513 alkali Substances 0.000 abstract description 14
- 239000003795 chemical substances by application Substances 0.000 abstract description 8
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 abstract description 5
- 239000000243 solution Substances 0.000 abstract description 4
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 abstract description 2
- 150000001875 compounds Chemical class 0.000 abstract 3
- 230000000397 acetylating effect Effects 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 42
- 238000006243 chemical reaction Methods 0.000 description 14
- 235000011121 sodium hydroxide Nutrition 0.000 description 14
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 12
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 description 9
- 239000004354 Hydroxyethyl cellulose Substances 0.000 description 9
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 9
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 description 9
- 238000006386 neutralization reaction Methods 0.000 description 9
- 229920003086 cellulose ether Polymers 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 239000011521 glass Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000005517 mercerization Methods 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 230000004913 activation Effects 0.000 description 3
- -1 aliphatic alcohols Chemical class 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 230000008961 swelling Effects 0.000 description 3
- GAWIXWVDTYZWAW-UHFFFAOYSA-N C[CH]O Chemical group C[CH]O GAWIXWVDTYZWAW-UHFFFAOYSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 125000001424 substituent group Chemical group 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 1
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000002612 dispersion medium Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000001033 ether group Chemical group 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000001863 hydroxypropyl cellulose Substances 0.000 description 1
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 229920000867 polyelectrolyte Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002522 swelling effect Effects 0.000 description 1
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、塗料、分散剤、化粧品
等の配合剤、さらに各種混合エーテルの基材として極め
て有効なヒドロキシアルキルセルロース及びその製造法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydroxyalkyl cellulose, which is extremely effective as a base material for paints, dispersants, cosmetics and the like, and various mixed ethers, and a method for producing the same.
【0002】[0002]
【従来の技術】セルロースエーテル、特にヒドロキシア
ルキルセルロースの製造については、その用途の多彩
さ、有用性から極めて多くの記述がある。しかし、基本
となる技術は、イソプロピルアルコール(IPA)や第
3級ブタノール(TBA)等の低級脂肪族アルコール、
水、アルカリ金属水酸化物の混合液中、スラリー状態に
てセルロース原料を等モル、あるいはやや過剰のアルカ
リ金属水酸化物で処理し、アルカリセルロースにした
後、エーテル化剤を添加してセルロースエーテルを得る
ことが一般的である。2. Description of the Related Art Regarding the production of cellulose ethers, especially hydroxyalkyl cellulose, there are numerous descriptions due to their versatility and usefulness. However, the basic technology is lower aliphatic alcohols such as isopropyl alcohol (IPA) and tertiary butanol (TBA),
Water, in a mixed solution of alkali metal hydroxide, a cellulose raw material in a slurry state is treated with an equimolar or a slight excess of alkali metal hydroxide to make alkali cellulose, and then an etherifying agent is added to the cellulose ether. Is generally obtained.
【0003】ここで、アルカリ金属水酸化物による前処
理は、アルセル化、あるいはマーセル化と呼ばれる一種
の活性化処理である。一般的にこの前処理では、セルロ
ース中の水酸基がアルコラートの状態になっていると言
われているが、詳細については不明である。ただこの処
理により、セルロース自身の結晶構造が変化し、アルカ
リの濃度によって結晶構造がアルカリセルロースI型、
II型、 III型、IV型と変化することが知られている。Here, the pretreatment with an alkali metal hydroxide is a kind of activation treatment called alcelization or mercerization. In this pretreatment, it is generally said that the hydroxyl groups in cellulose are in an alcoholate state, but the details are unknown. However, this treatment changes the crystal structure of the cellulose itself, and the crystal structure changes depending on the alkali concentration.
It is known to change from type II, type III, and type IV.
【0004】実際のヒドロキシアルキルセルロースの製
造において、このアルカリによる前処理は、単なる活性
化だけのものではない。すなわち、仕込みセルロース原
料はシート状で入手されるが、製造現場においては反応
装置の大きさ、経済性、さらにプロセス的な観点から、
シート状セルロースを裁断し、粉体にした状態で反応系
に投入されるのが一般的である。しかし、この時、粉砕
されることによりセルロース繊維自身がダメージを受
け、裁断された部分が潰れ、薬液の浸透が阻害されるこ
と、さらに摩擦熱によって分子内の水分が消失し、分子
内水素結合が生じることによって、反応性が極めて悪化
することが指摘されている。アルカリによる前処理はこ
れらの劣化因子を除去するために行われるという一面も
ある。In the actual production of hydroxyalkyl cellulose, this pretreatment with alkali is not merely activation. That is, the charged cellulose raw material is obtained in the form of a sheet, but at the manufacturing site, from the viewpoint of the size of the reactor, the economical efficiency and the process,
It is general that the sheet-shaped cellulose is cut and put into a reaction system in a powder state. However, at this time, the cellulose fiber itself is damaged by crushing, the cut part is crushed, the penetration of the chemical solution is hindered, and further the moisture in the molecule disappears due to friction heat, and the intramolecular hydrogen bond is generated. It has been pointed out that the reactivity is extremely deteriorated due to the occurrence of. In one aspect, the pretreatment with alkali is performed to remove these deterioration factors.
【0005】一般的にアルカリ水溶液によるセルロース
の膨潤は極めて良好であるため、高濃度のアルカリで処
理した方が、膨潤効果が大きい。Generally, the swelling of cellulose with an aqueous alkaline solution is extremely good, and therefore the swelling effect is greater when treated with a high-concentration alkali.
【0006】[0006]
【発明が解決しようとする課題】しかしながら、高濃度
のアルカリで処理した場合、劣化部再生、膨潤活性化処
理という点では良好であるが、エーテル化の際に副反応
が激しくなり、エーテル化剤の利用率が著しく低下し経
済的ではなくなる。このため、従来のエーテル化の反応
においては、マーセル化段階のアルカリ濃度はグルコー
ス単位あたり 1.0〜1.4 モル程度が一般的であった。However, when treated with a high-concentration alkali, it is good in terms of regeneration of the deteriorated portion and swelling activation treatment, but side reactions become severe during the etherification, and the etherification agent The utilization rate of will be significantly reduced and it will not be economical. Therefore, in the conventional etherification reaction, the alkali concentration in the mercerization step is generally about 1.0 to 1.4 mol per glucose unit.
【0007】しかるに、パルプ解砕を十分にマイルドな
方法、例えば水中で離解してやる等の処理を行なわない
限り、マーセル化における膨潤が不充分なため、エーテ
ル基の置換度を 2.0以上にしてやらなければ、水溶液に
した場合の透明性に優れたものは得られにくい。However, unless the pulp is crushed sufficiently mildly, for example, if it is disintegrated in water, the swelling in mercerization is insufficient, so the degree of substitution of the ether group must be 2.0 or more. However, when it is made into an aqueous solution, it is difficult to obtain one having excellent transparency.
【0008】[0008]
【課題を解決するための手段】本発明者は、本来、解
砕、裁断され、劣化されたセルロース原料を活性化し、
良好な性状を有するセルロースエーテルを得るために
は、アルセル化の段階で高濃度アルカリ処理を行う方が
好ましいという考えに基づき、鋭意検討した結果、原料
セルロースをエーテル化する際、親水性有機溶剤と水の
混合溶液を用い、アルカリ金属水酸化物がセルロースの
グルコース単位当たり 1.5〜2.0 モル存在する状態で前
処理し、エーテル化の前にアルカリ金属水酸化物の一部
を中和した後にエーテル化するセルロースエーテルの製
造法を見出した。さらに、この方法によって得られるヒ
ドロキシアルキルセルロースは、従来方法によって得ら
れる同一置換度のものに対し、水溶液の透明度が極めて
優れていることを見出し、本発明を完成するに至った。Means for Solving the Problems The present inventor originally intended to activate crushed, cut and deteriorated cellulose raw materials,
In order to obtain a cellulose ether having good properties, based on the idea that it is preferable to carry out a high-concentration alkali treatment in the stage of alcelization, as a result of diligent study, when etherifying the raw material cellulose, a hydrophilic organic solvent Pretreatment with a mixed solution of water and alkali metal hydroxide in an amount of 1.5 to 2.0 mol per glucose unit of cellulose, and prior to etherification, part of the alkali metal hydroxide is neutralized and then etherified. We have found a method for producing cellulose ethers. Furthermore, the hydroxyalkyl cellulose obtained by this method was found to be extremely excellent in the transparency of the aqueous solution as compared with the one having the same degree of substitution obtained by the conventional method, and completed the present invention.
【0009】すなわち本発明は、原料セルロースを、当
該セルロースのグルコース単位(以下、単にグルコース
単位と表記する)当たり 1.5〜2.0 モルのアルカリ金属
水酸化物を含む親水性有機溶剤と水の混合溶液中に分散
させた後、系中のアルカリ金属水酸化物の一部を中和
し、その後当該セルロースをエーテル化することを特徴
とするヒドロキシアルキルセルロースの製造法、及びこ
の方法により製造されたヒドロキシアルキルセルロース
を提供するものである。That is, in the present invention, the raw material cellulose is mixed with a hydrophilic organic solvent and water containing 1.5 to 2.0 mol of alkali metal hydroxide per glucose unit (hereinafter simply referred to as glucose unit) of the cellulose. And then neutralizing a part of the alkali metal hydroxide in the system, and then etherifying the cellulose, and a hydroxyalkyl cellulose produced by this method. It provides cellulose.
【0010】本発明におけるセルロース原料は、パル
プ、リンターのどちらでもよい。さらに一般的にはシー
ト状のものを乾式解砕、裁断を行って使用するが、フラ
ッフ状、ブロック状のものでも適用できる。The cellulose raw material in the present invention may be either pulp or linter. Further, generally, a sheet-shaped material is used after dry crushing and cutting, but a fluff-shaped material or a block-shaped material is also applicable.
【0011】本発明におけるアルカリによる前処理で使
用するアルカリとして、水酸化アルカリ金属、例えば水
酸化ナトリウム、水酸化カリウム等、又は水酸化アルカ
リ土類金属、例えば水酸化カルシウム、水酸化マグネシ
ウム等が用いられる。これらは適当な濃度の水溶液とし
て用いてもよい。一般的なマーセル化は、処理温度を15
℃以下にして行なわれるが、本発明においても同様の方
法で処理される。アルカリ金属水酸化物を添加した後、
所定温度で適当な時間、例えば60〜120 分程度放置して
反応を進行させる。As the alkali used in the pretreatment with alkali in the present invention, alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, or alkaline earth metal hydroxides such as calcium hydroxide and magnesium hydroxide are used. To be These may be used as an aqueous solution having an appropriate concentration. The general mercerization process temperature is 15
It is carried out at a temperature of not more than 0 ° C., but the same method is used in the present invention. After adding the alkali metal hydroxide,
The reaction is allowed to proceed by leaving it at a predetermined temperature for an appropriate time, for example, about 60 to 120 minutes.
【0012】本発明の製造法は、エーテル化の前にアル
カリ金属水酸化物の一部を中和する工程を含むが、その
際の中和剤としては特に限定はなく、酢酸などの有機
酸、及び硝酸などの無機酸が使用できる。The production method of the present invention includes a step of neutralizing a part of the alkali metal hydroxide before the etherification, but the neutralizing agent at that time is not particularly limited, and an organic acid such as acetic acid is used. , And inorganic acids such as nitric acid can be used.
【0013】一般的に、セルロースのエーテル化はスラ
リー状態で行われるが、その際の分散媒として使用され
るのはイソプロピルアルコール、第3級ブタノールなど
の低級アルコール等の親水性有機溶剤と水の混合溶液で
ある。当該混合溶液中の親水性有機溶剤濃度は88〜92重
量%であることが好ましい。また、親水性有機溶剤とし
ては、第3級ブタノールが特に好ましい。なお、水はア
ルカリ金属水酸化物水溶液に由来してもよい。Generally, the etherification of cellulose is carried out in a slurry state, and the dispersion medium used in that case is a hydrophilic organic solvent such as isopropyl alcohol or a lower alcohol such as tertiary butanol, and water. It is a mixed solution. The hydrophilic organic solvent concentration in the mixed solution is preferably 88 to 92% by weight. Further, as the hydrophilic organic solvent, tertiary butanol is particularly preferable. The water may be derived from the alkali metal hydroxide aqueous solution.
【0014】エーテル化の反応方法については、上記の
如く本発明ではアルセル化の際に 1.5〜 2.0モル/グル
コース単位のアルカリで処理した後、エーテル化剤を添
加する前に 0.3〜 0.7モル/グルコース単位のアルカリ
を中和してエーテル化を行う。一般的にはエーテル化剤
の沸点近傍で一定時間反応せしめる方法が採用される。
エーテル化剤としては目的とするヒドロキシアルキルセ
ルロースが得られるものであれば、何れでもよく、例え
ばエチレンオキサイド、プロピレンオキサイド、ブチレ
ンオキサイド等が挙げられる。もちろんこれ以外のエー
テル化剤を用いたエーテル化反応であってもよい。Regarding the reaction method of etherification, in the present invention, as described above, after the treatment with an alkali of 1.5 to 2.0 mol / glucose unit in the case of the alcelization, 0.3 to 0.7 mol / glucose is added before adding the etherifying agent. The unit of alkali is neutralized for etherification. Generally, a method of reacting at a temperature near the boiling point of the etherifying agent for a certain period of time is adopted.
Any etherifying agent may be used as long as it can obtain the intended hydroxyalkyl cellulose, and examples thereof include ethylene oxide, propylene oxide, and butylene oxide. Of course, an etherification reaction using an etherifying agent other than this may be used.
【0015】得られた反応物については、親水性有機溶
剤と水の混合溶液にて洗浄を行い、中和によって生成す
る塩を除去し、乾燥して目的のセルロースエーテルを得
ることができる。The obtained reaction product can be washed with a mixed solution of a hydrophilic organic solvent and water to remove salts produced by neutralization, and dried to obtain the target cellulose ether.
【0016】このようにして得られたヒドロキシアルキ
ルセルロースは、置換度 1.1〜1.9程度ではあるが、非
常に水への溶解性に優れ、一般的な方法で得られた同一
置換度のヒドロキシアルキルセルロースに比べて良好な
透明度を示す。特に置換度が1.4以上のものは更に透明
度が良くなり、1%水溶液が透明度 600mm以上を示すも
のが得られる。The hydroxyalkyl cellulose thus obtained has a degree of substitution of about 1.1 to 1.9, but has a very good solubility in water, and the hydroxyalkyl cellulose having the same degree of substitution obtained by a general method. Shows better transparency than In particular, those having a degree of substitution of 1.4 or more have further improved transparency, and a 1% aqueous solution has a transparency of 600 mm or more.
【0017】この理由としては定かではないが、高濃度
のアルカリによる処理で、非常に連鎖の長い置換基分布
を有するヒドロキシアルキルセルロースが得られるため
と推測される。一般にヒドロキシアルキルセルロースが
水に溶解する機構は、カルボキシメチルセルロースなど
のように高分子電解質になって溶解しているのではな
く、ヒドロキシアルキル基が結合することにより、構造
上、セルロースのもつ結晶構造を崩壊せしめることによ
り、溶解するとされている。この観点から、本発明によ
り得られるヒドロキシアルキルセルロースは、連鎖の長
い置換基を有していることで、比較的置換度が低くて
も、良好な水への溶解性を示すものと推測される。な
お、本発明において透明度とは後述の実施例中に記載し
た方法により得られるものをいう。The reason for this is not clear, but it is presumed that the treatment with a high-concentration alkali gives a hydroxyalkyl cellulose having a distribution of substituents with a very long chain. In general, the mechanism by which hydroxyalkyl cellulose is dissolved in water is not that it is dissolved as a polyelectrolyte like carboxymethyl cellulose, but because hydroxyalkyl groups are bonded, the crystalline structure of cellulose is It is said to dissolve when it is disintegrated. From this viewpoint, it is speculated that the hydroxyalkyl cellulose obtained by the present invention has a long-chain substituent, and therefore exhibits good water solubility even if the degree of substitution is relatively low. . In the present invention, the term “transparency” means that obtained by the method described in Examples below.
【0018】かくして得られた本発明のヒドロキシアル
キルセルロースは、具体的には各種置換度のヒドロキシ
エチルセルロース、ヒドロキシプロピルセルロース、ヒ
ドロキシブチルセルロースなどである。The hydroxyalkyl cellulose of the present invention thus obtained is specifically hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxybutyl cellulose or the like having various substitution degrees.
【0019】[0019]
【実施例】次に本発明を実施例によって説明するが、本
発明はここに挙げる実施例の範囲に限定されるものでは
ない。EXAMPLES The present invention will now be described by way of examples, which should not be construed as limiting the scope of the present invention.
【0020】(透明度の測定法)反応により得られたヒ
ドロキシアルキルセルロースを1重量%になるように水
に溶解した水溶液を作成する。一方、直径30mm、高さ 7
00mmの片側解放のガラス管、及び太さ1mmの直線を1mm
の間隔で2本引いた紙を用意する。ガラス管の閉鎖部分
(底)に直線を引いた紙を貼り、暗室にて40Wの蛍光灯
を点灯し、ガラス管の上部20cmから底に向かって光を当
てる。ガラス管を垂直に立て、準備した水溶液を気泡が
入らないように入れてゆき、2本の直線の間が確認でき
なくなる高さを透明度(mm)として表示する。(Measurement Method of Transparency) An aqueous solution is prepared by dissolving 1% by weight of hydroxyalkyl cellulose obtained by the reaction in water. On the other hand, diameter 30mm, height 7
00mm one side open glass tube and 1mm thick straight line 1mm
Prepare two papers drawn at intervals. Stick a straight line on the closed part (bottom) of the glass tube, turn on a 40W fluorescent lamp in a dark room, and illuminate the top 20 cm of the glass tube toward the bottom. Stand the glass tube vertically, put the prepared aqueous solution in such a way that air bubbles do not enter, and display the height at which the distance between the two straight lines cannot be seen as transparency (mm).
【0021】実施例1 カッターミルで粉砕されたパルプ20g(純分)をセパラ
ブルフラスコにとり、t−ブタノール180gに分散した
後、8.4gの苛性ソーダ(1.7モル/グルコース単位) を
水20gに溶解した苛性ソーダ水溶液を添加して、15℃で
120分、アルセル化を行った後、15℃にした状態で酢酸
を約2分かけて添加し、残存苛性ソーダの量がグルコー
ス単位当たり 1.3モル(即ち中和量は0.4 モル)になる
ように中和を行った。この時、中和による熱で若干反応
系内の温度が上昇するが、中和を均一に行うために、こ
の状態で10分攪拌する。その間に15℃になるように系を
冷却し調整する。得られたアルセル化パルプのスラリー
にグルコース単位当たり3.7モルのエチレンオキシドを
添加して50℃に昇温後90分、さらに70℃に昇温して90分
反応せしめる。得られたヒドロキシエチルセルロースの
性状は、置換度1.68、1%水溶液の透明度 640mm以上で
あった。Example 1 20 g (pure content) of pulp crushed with a cutter mill was placed in a separable flask and dispersed in 180 g of t-butanol, and then 8.4 g of caustic soda (1.7 mol / glucose unit) was dissolved in 20 g of water. Add caustic soda solution at 15 ℃
After performing alcelization for 120 minutes, acetic acid was added to the mixture at 15 ° C over about 2 minutes, and the amount of residual caustic soda was 1.3 mol per glucose unit (that is, the neutralization amount was 0.4 mol). I went to sum. At this time, the temperature in the reaction system rises slightly due to the heat of neutralization, but stirring is performed for 10 minutes in this state in order to uniformly perform the neutralization. In the meantime, cool and adjust the system so that the temperature becomes 15 ° C. 3.7 mol of ethylene oxide per glucose unit was added to the obtained slurry of alcerized pulp, and the temperature was raised to 50 ° C. for 90 minutes, and further raised to 70 ° C. for 90 minutes for reaction. The hydroxyethyl cellulose obtained had a degree of substitution of 1.68 and a transparency of a 1% aqueous solution of 640 mm or more.
【0022】実施例2 実施例1と同様の方法で、アルセル化の段階でグルコー
ス単位当たり 2.0モルの苛性ソーダで処理し、エーテル
化前に残存苛性ソーダの量がグルコース単位当たり 1.3
モル(即ち中和量は0.7 モル)になるように中和して反
応を行った。得られたヒドロキシエチルセルロースの置
換度1.86、1%水溶液の透明度は 640mm以上であった。Example 2 In the same manner as in Example 1, 2.0 mol of caustic soda per glucose unit was treated at the stage of alcerization, and the amount of residual caustic soda was 1.3 per glucose unit before etherification.
The reaction was carried out by neutralizing to a molar amount (that is, a neutralization amount of 0.7 mol). The degree of substitution of the obtained hydroxyethyl cellulose was 1.86, and the transparency of a 1% aqueous solution was 640 mm or more.
【0023】実施例3 実施例1と同様の方法で、アルセル化の段階でグルコー
ス単位当たり 1.7モルの苛性ソーダで処理し、エーテル
化前に残存苛性ソーダの量がグルコース単位当たり 1.3
モル(即ち中和量は0.4 モル)になるように中和した。
また、反応系に添加するエチレンオキシドの量をグルコ
ース単位当たり 2.0モルになるようにして反応を行っ
た。得られたヒドロキシエチルセルロースの置換度1.5
0、1%水溶液の透明度は 640mm以上であった。Example 3 In the same manner as in Example 1, the mixture was treated with 1.7 mol of caustic soda per glucose unit at the stage of alcerization, and the amount of residual caustic soda was 1.3 per glucose unit before etherification.
It neutralized so that it might become a mol (namely, the amount of neutralization is 0.4 mol).
Further, the reaction was carried out so that the amount of ethylene oxide added to the reaction system was 2.0 mol per glucose unit. Substitution degree of the obtained hydroxyethyl cellulose is 1.5
The transparency of the 0% 1% aqueous solution was 640 mm or more.
【0024】比較例1 実施例1と同様の手順で反応を行うが、アルセル化、エ
ーテル化を通じて、系内の苛性ソーダの量はグルコース
単位当たり 1.3モルであった。得られたヒドロキシエチ
ルセルロースの置換度は1.94、1%水溶液の透明度は 1
20mmであった。Comparative Example 1 The reaction was carried out in the same procedure as in Example 1, but the amount of caustic soda in the system was 1.3 mol per glucose unit through the process of alcelization and etherification. The degree of substitution of the obtained hydroxyethyl cellulose is 1.94, and the transparency of a 1% aqueous solution is 1
It was 20 mm.
【0025】比較例2 実施例1と同様の手順で反応を行うが、アルセル化、エ
ーテル化を通じて、系内の苛性ソーダの量はグルコース
単位当たり 1.3モルであり、さらに添加したエチレンオ
キシドはグルコース単位当たり 1.5モルとした。得られ
たヒドロキシエチルセルロースの置換度は1.45、1%水
溶液の透明度は85mmであった。Comparative Example 2 The reaction was carried out by the same procedure as in Example 1, but the amount of caustic soda in the system was 1.3 mol per glucose unit through the addition of alcel and etherification, and the added ethylene oxide was 1.5 mol per glucose unit. Mole. The degree of substitution of the obtained hydroxyethyl cellulose was 1.45, and the transparency of a 1% aqueous solution was 85 mm.
【0026】比較例3 実施例1と同様の手順で反応を行なうが、アルセル化時
の苛性ソーダの量をグルコース単位当たり 1.8モルとし
て処理を行い、エーテル化反応前に残存苛性ソーダの量
がグルコース単位当たり 1.0モル(即ち中和量は0.8 モ
ル)になるよう酢酸で中和した。得られたヒドロキシエ
チルセルロースのヒドロキシエチル置換度は1.91で、1
%水溶液の透明度は 500mmであった。Comparative Example 3 The reaction was carried out in the same procedure as in Example 1, except that the amount of caustic soda at the time of alcelization was 1.8 mol per glucose unit, and the amount of residual caustic soda was changed per glucose unit before the etherification reaction. The solution was neutralized with acetic acid to 1.0 mol (that is, the neutralization amount was 0.8 mol). The hydroxyethyl cellulose thus obtained had a hydroxyethyl substitution degree of 1.91 and was 1
% Aqueous solution had a transparency of 500 mm.
【0027】比較例4 実施例1と同様の手順で反応を行なうが、アルセル化時
の苛性ソーダの量をグルコース単位当たり 1.5モルとし
て処理を行い、エーテル化反応前に残存苛性ソーダがグ
ルコース単位当たり 1.3モル(即ち中和量は0.2 モル)
になるよう酢酸で中和した。得られたヒドロキシエチル
セルロースのヒドロキシエチル置換度は1.96で、1%水
溶液の透明度は25mmであった。Comparative Example 4 The reaction was carried out in the same procedure as in Example 1, except that the amount of caustic soda at the time of alcelization was 1.5 mol per glucose unit, and the treatment was carried out so that the residual caustic soda was 1.3 mol per glucose unit before the etherification reaction. (Ie neutralization amount is 0.2 mol)
It was neutralized with acetic acid. The hydroxyethyl cellulose thus obtained had a hydroxyethyl substitution degree of 1.96 and a 1% aqueous solution had a transparency of 25 mm.
【0028】比較例5 実施例1と同様の手順で反応を行うが、アルセル化後の
中和を行なわずエーテル化した。得られたヒドロキシエ
チルセルロースの置換度は1.72、1%水溶液の透明度は
260mmであった。Comparative Example 5 The reaction was carried out in the same procedure as in Example 1, but the etherification was carried out without neutralization after the alcelization. The degree of substitution of the obtained hydroxyethyl cellulose is 1.72, and the transparency of a 1% aqueous solution is
It was 260 mm.
Claims (7)
ルコース単位当たり1.5〜2.0 モルのアルカリ金属水酸
化物を含む親水性有機溶剤と水の混合溶液中に分散させ
た後、系中のアルカリ金属水酸化物の一部を中和し、そ
の後当該セルロースをエーテル化することを特徴とする
ヒドロキシアルキルセルロースの製造法。1. A raw material cellulose is dispersed in a mixed solution of a hydrophilic organic solvent containing 1.5 to 2.0 mol of an alkali metal hydroxide per glucose unit of the cellulose and water, and then the alkali metal hydroxide in the system is dispersed. A method for producing a hydroxyalkyl cellulose, which comprises neutralizing a part of a product and then etherifying the cellulose.
88〜92重量%である請求項1記載のヒドロキシアルキル
セルロースの製造法。2. The hydrophilic organic solvent concentration in the mixed solution is
The method for producing a hydroxyalkyl cellulose according to claim 1, which is 88 to 92% by weight.
化物をセルロースのグルコース単位当たり 0.3〜0.7 モ
ル中和する請求項1又は2記載のヒドロキシアルキルセ
ルロースの製造法。3. The method for producing a hydroxyalkyl cellulose according to claim 1, wherein the alkali metal hydroxide in the system is neutralized by 0.3 to 0.7 mol per glucose unit of cellulose before etherification.
ることを特徴とする請求項1〜3の何れか1項記載のヒ
ドロキシアルキルセルロースの製造法。4. The method for producing hydroxyalkyl cellulose according to claim 1, wherein the hydrophilic organic solvent is tertiary butanol.
により製造され、ヒドロキシアルキル置換度が 1.1〜1.
9 であるヒドロキシアルキルセルロース。5. The method according to any one of claims 1 to 4, wherein the hydroxyalkyl substitution degree is 1.1 to 1.
A hydroxyalkyl cellulose that is 9.
により製造されたヒドロキシアルキルセルロース。6. A hydroxyalkyl cellulose produced by the production method according to claim 1.
で、1%水溶液の透明度が 600mm以上であるヒドロキシ
アルキルセルロース。7. The hydroxyalkyl substitution degree is 1.4 to 1.9.
A hydroxyalkyl cellulose whose 1% aqueous solution has a transparency of 600 mm or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4856295A JPH08245701A (en) | 1995-03-08 | 1995-03-08 | Highly transparent hydroxyalkyl cellulose and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4856295A JPH08245701A (en) | 1995-03-08 | 1995-03-08 | Highly transparent hydroxyalkyl cellulose and its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08245701A true JPH08245701A (en) | 1996-09-24 |
Family
ID=12806837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4856295A Pending JPH08245701A (en) | 1995-03-08 | 1995-03-08 | Highly transparent hydroxyalkyl cellulose and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08245701A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001354701A (en) * | 2000-06-14 | 2001-12-25 | Shin Etsu Chem Co Ltd | Method for producing powdery pulp and method for producing cellulose ether |
| US6811605B2 (en) * | 2002-03-11 | 2004-11-02 | Shin-Etsu Chemical Co., Ltd. | Admixture and extrudable hydraulic composition |
| WO2006062268A1 (en) | 2004-12-07 | 2006-06-15 | Samsung Fine Chemicals Co., Ltd. | Improved method for preparation of high enzymatic resistance hydroxyalkylcellulose derivatives |
| JP2008535937A (en) * | 2005-02-17 | 2008-09-04 | ハーキュリーズ・インコーポレーテッド | Uneven hydroxyethyl cellulose, their derivatives, their preparation and use |
| JP2008261062A (en) * | 2007-04-10 | 2008-10-30 | Nippon Paper Chemicals Co Ltd | Pulp sheet for dry crushing |
| WO2009063856A1 (en) | 2007-11-14 | 2009-05-22 | Kao Corporation | Method for producing cellulose ether derivative |
| WO2009084452A1 (en) | 2007-12-27 | 2009-07-09 | Kao Corporation | Method for producing methyl cellulose |
| JP2011037924A (en) * | 2009-08-06 | 2011-02-24 | Purex:Kk | Alkali cellulose, and method for producing the same or derivative thereof |
| JP2014139289A (en) * | 2012-12-18 | 2014-07-31 | Kao Corp | Method for improving reaction selectivity of alkylene oxide |
-
1995
- 1995-03-08 JP JP4856295A patent/JPH08245701A/en active Pending
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001354701A (en) * | 2000-06-14 | 2001-12-25 | Shin Etsu Chem Co Ltd | Method for producing powdery pulp and method for producing cellulose ether |
| US6811605B2 (en) * | 2002-03-11 | 2004-11-02 | Shin-Etsu Chemical Co., Ltd. | Admixture and extrudable hydraulic composition |
| WO2006062268A1 (en) | 2004-12-07 | 2006-06-15 | Samsung Fine Chemicals Co., Ltd. | Improved method for preparation of high enzymatic resistance hydroxyalkylcellulose derivatives |
| EP1828252A4 (en) * | 2004-12-07 | 2011-07-13 | Samsung Fine Chemicals Co Ltd | Improved method for preparation of high enzymatic resistance hydroxyalkylcellulose derivatives |
| JP2008535937A (en) * | 2005-02-17 | 2008-09-04 | ハーキュリーズ・インコーポレーテッド | Uneven hydroxyethyl cellulose, their derivatives, their preparation and use |
| KR101276518B1 (en) * | 2005-02-17 | 2013-06-25 | 허큘레스 인코포레이티드 | Blocky hydroxyethylcellulose, derivatives thereof, process of making, and uses thereof |
| JP2008261062A (en) * | 2007-04-10 | 2008-10-30 | Nippon Paper Chemicals Co Ltd | Pulp sheet for dry crushing |
| WO2009063856A1 (en) | 2007-11-14 | 2009-05-22 | Kao Corporation | Method for producing cellulose ether derivative |
| WO2009084452A1 (en) | 2007-12-27 | 2009-07-09 | Kao Corporation | Method for producing methyl cellulose |
| US8440817B2 (en) | 2007-12-27 | 2013-05-14 | Kao Corporation | Method for producing methyl cellulose |
| JP2011037924A (en) * | 2009-08-06 | 2011-02-24 | Purex:Kk | Alkali cellulose, and method for producing the same or derivative thereof |
| JP2014139289A (en) * | 2012-12-18 | 2014-07-31 | Kao Corp | Method for improving reaction selectivity of alkylene oxide |
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