JP2007277563A - Polyacrylamide and method of producing the same - Google Patents

Polyacrylamide and method of producing the same Download PDF

Info

Publication number
JP2007277563A
JP2007277563A JP2007119365A JP2007119365A JP2007277563A JP 2007277563 A JP2007277563 A JP 2007277563A JP 2007119365 A JP2007119365 A JP 2007119365A JP 2007119365 A JP2007119365 A JP 2007119365A JP 2007277563 A JP2007277563 A JP 2007277563A
Authority
JP
Japan
Prior art keywords
acrylamide
aqueous solution
saccharide
polyacrylamide
acrylamide aqueous
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.)
Granted
Application number
JP2007119365A
Other languages
Japanese (ja)
Other versions
JP5132979B2 (en
Inventor
Kozo Murao
耕三 村尾
Masaaki Seya
昌明 瀬谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dianitrix Co Ltd
Original Assignee
Dianitrix Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dianitrix Co Ltd filed Critical Dianitrix Co Ltd
Priority to JP2007119365A priority Critical patent/JP5132979B2/en
Publication of JP2007277563A publication Critical patent/JP2007277563A/en
Application granted granted Critical
Publication of JP5132979B2 publication Critical patent/JP5132979B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method of producing a high quality polyacrylamide. <P>SOLUTION: The method of producing the plyacrylamide comprises polymerizing acrylamide using an acrylamide aqueous solution containing 0.1-100 mg of a saccharide in 1 l of the acrylamide aqueous solution and having an acrylamide content of 40-60 mass% as a raw material. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、高品質なポリアクリルアミド及びその製造方法に関する。   The present invention relates to a high-quality polyacrylamide and a method for producing the same.

アクリルアミド系重合体は、高分子凝集剤、製紙用薬剤、土壌改良剤、石油回収用薬剤、掘削泥水用増粘剤、高分子吸収体等の多くの分野において使用されている。これらの用途に使用するには、非常に高分子量でかつ重合体を水に溶解した場合に水不溶物が少ない等の特性が求められる。   Acrylamide polymers are used in many fields such as polymer flocculants, papermaking agents, soil conditioners, oil recovery agents, drilling mud thickeners, polymer absorbers and the like. For use in these applications, characteristics such as a very high molecular weight and a small amount of water-insoluble matter when the polymer is dissolved in water are required.

このような高分子量かつ溶解性の良好なアクリルアミド系重合体を得る方法として、異常な高分子量の重合体の生成を防止する連鎖移動剤や乾燥時の架橋を防ぐ効果を有する物質を使用する方法等、種々提案されているが、アクリルアミドの品質によるところも大きいとされる。例えば、アクリルアミドの製造において、アクロレインやオキサゾール等の不純物を取り除く方法が、特開平8-157439や特開平10-7638等、種々提案されていることからもそのことが覗える。   As a method for obtaining such an acrylamide polymer having a high molecular weight and good solubility, a method using a chain transfer agent for preventing the formation of an abnormal high molecular weight polymer or a substance having an effect for preventing crosslinking during drying. Although various proposals have been made, it is considered that the quality depends on the quality of acrylamide. For example, this can be seen from the fact that various methods for removing impurities such as acrolein and oxazole in the production of acrylamide have been proposed, such as JP-A-8-157439 and JP-A-10-7638.

しかしこれまで、アクリルアミド重合体物性への糖類が及ぼす影響を検討した例は報告されていない。   However, no examples have been reported so far in which the effects of saccharides on the physical properties of acrylamide polymers have been studied.

アクリルアミドの製造方法は、従来アクリロニトリルから還元状態の銅を触媒として製造されてきたが、近年銅触媒に代えて微生物酵素を用いる方法が開発され実用化されている。微生物酵素を用いる方法は、その反応条件が温和で副生成物も殆ど無く極めてシンプルなプロセスが組めることから工業的製法として極めて有効である。   The method for producing acrylamide has been conventionally produced from acrylonitrile using reduced copper as a catalyst. Recently, a method using a microbial enzyme instead of a copper catalyst has been developed and put into practical use. The method using a microbial enzyme is very effective as an industrial production method because the reaction conditions are mild and there are almost no by-products, and a very simple process can be assembled.

また不純物が少ないためか、微生物酵素を用いて製造したアクリルアミドは、非常に高分子量でかつ不溶性不純物のない高品質なポリアクリルアミドを製造できる(特開平9-118704)という利点から、近頃ではアクリルアミド製造のメインプロセスとなっている。   In addition, acrylamide produced using a microbial enzyme may have a very high molecular weight and can produce high-quality polyacrylamide free from insoluble impurities (Japanese Patent Laid-Open No. 9-118704). Has become the main process.

アクリルアミドは、劇物に指定されている毒性の高い物質である。一般的には、高濃度のアクリルアミド水溶液を用いる方が、より高分子量の重合体が形成され、高粘度のポリアクリルアミド水溶液が得られる。昨今では、環境問題、エネルギー問題への関心から、各種産業において利用されるポリアクリルアミドを製造するために用いられるアクリルアミドの使用量を低減することが望ましく、低濃度のアクリルアミドから高い粘度を有するポリアクリルアミドを製造することへの要望が高まっている。即ち、本発明の課題は、低濃度のアクリルアミド溶液から、より高粘度を示すポリアクリルアミドを製造できるアクリルアミド溶液、およびこのようなアクリルアミド溶液から製造されるポリアクリルアミドを提供することである。   Acrylamide is a highly toxic substance designated as a deleterious substance. In general, a higher-concentration polymer is formed by using a high-concentration acrylamide aqueous solution, and a high-viscosity polyacrylamide aqueous solution is obtained. In recent years, it is desirable to reduce the amount of acrylamide used to produce polyacrylamide used in various industries because of concern for environmental issues and energy issues, and polyacrylamide with high viscosity from low concentration acrylamide. There is a growing demand for manufacturing. That is, the subject of this invention is providing the acrylamide solution which can manufacture the polyacrylamide which shows higher viscosity from the acrylamide solution of a low concentration, and the polyacrylamide manufactured from such an acrylamide solution.

本発明者らは、上記課題を克服するために鋭意検討した結果、糖類が含まれるアクリルアミド水溶液を原料としてポリアクリルアミドを製造すると、糖を含まない等濃度のアクリルアミド水溶液から得られるポリアクリルアミドに比べてより高粘度のポリアクリルアミド水溶液が得られることを見出し、本発明を完成させるに至った。   As a result of intensive studies to overcome the above problems, the present inventors have produced polyacrylamide using an acrylamide aqueous solution containing a saccharide as a raw material, compared with a polyacrylamide obtained from an acrylamide aqueous solution having an equal concentration not containing a saccharide. It has been found that a polyacrylamide aqueous solution having a higher viscosity can be obtained, and the present invention has been completed.

即ち、本発明は以下を包含する:
(1)糖類をアクリルアミド水溶液1L当たり0.1〜100mg含み、かつ40〜60質量%のアクリルアミド含量を有するアクリルアミド水溶液を原料として用いて、アクリルアミド重合化を行うことにより、ポリアクリルアミドを製造する方法;
(2)前記アクリルアミド水溶液が1L当たり1.0〜50mgの糖類を含む、上記(1)記載の方法;
(3)前記アクリルアミド水溶液が1L当たり3.0〜19mgの糖類を含む、上記(1)記載の方法;
(4)前記アクリルアミド水溶液が、微生物から調製した糖類含有液をアクリルアミド水溶液に添加して得られるものである、上記(1)〜(3)のいずれか記載の方法;
(5)微生物がニトリルヒドラターゼ酵素を発現するものである上記(4)記載の方法;
(6)微生物がロドコッカス属細菌である、上記(5)記載の方法;
(7)ロドコッカス属細菌がロドコッカス・ロドクロウスである上記(6)記載の方法;
(8)ニトリルヒドラターゼ活性を有する生体触媒により製造される上記(1)〜(7)のいずれか記載の方法;
(9)前記アクリルアミド水溶液が、ニトリルヒドラターゼ活性を有し糖類を含有する生体触媒を用いて産生されたものである、上記(1)〜(8)のいずれか記載の方法;
(10)上記(1)〜(9)のいずれかに記載の方法により製造されるポリアクリルアミド。
That is, the present invention includes the following:
(1) A method for producing polyacrylamide by performing acrylamide polymerization using an acrylamide aqueous solution containing 0.1 to 100 mg of saccharide per liter of acrylamide aqueous solution and having an acrylamide content of 40 to 60% by mass as a raw material;
(2) The method according to (1) above, wherein the aqueous acrylamide solution contains 1.0 to 50 mg of saccharide per liter;
(3) The method according to (1) above, wherein the acrylamide aqueous solution contains 3.0 to 19 mg of saccharide per liter;
(4) The method according to any one of (1) to (3) above, wherein the acrylamide aqueous solution is obtained by adding a saccharide-containing solution prepared from a microorganism to the acrylamide aqueous solution.
(5) The method according to (4) above, wherein the microorganism expresses a nitrile hydratase enzyme;
(6) The method according to (5) above, wherein the microorganism is a Rhodococcus bacterium;
(7) The method according to (6) above, wherein the Rhodococcus bacterium is Rhodococcus rhodochrous;
(8) The method according to any one of (1) to (7) above, which is produced by a biocatalyst having nitrile hydratase activity;
(9) The method according to any one of (1) to (8) above, wherein the acrylamide aqueous solution is produced using a biocatalyst having nitrile hydratase activity and containing a saccharide;
(10) Polyacrylamide produced by the method according to any one of (1) to (9) above.

本発明により、高品質なアクリルアミド水溶液、および低濃度で高性能なポリアクリルアミド溶液を原料として用いて、物性に優れた高性能なポリアクリルアミドを提供することができる。   According to the present invention, a high-performance polyacrylamide having excellent physical properties can be provided by using a high-quality acrylamide aqueous solution and a low-concentration and high-performance polyacrylamide solution as raw materials.

以下、本発明を詳細に説明する。
本発明でいうアクリルアミド水溶液とは、アクリルアミドを40〜60質量%、好ましくは50質量%含有する水溶液である。該アクリルアミド水溶液に過硫酸アンモニウム等の重合開始剤を添加することにより、アクリルアミドが重合してポリアクリルアミド水溶液となる。
Hereinafter, the present invention will be described in detail.
The acrylamide aqueous solution referred to in the present invention is an aqueous solution containing 40 to 60% by mass, preferably 50% by mass, of acrylamide. By adding a polymerization initiator such as ammonium persulfate to the acrylamide aqueous solution, the acrylamide is polymerized to form a polyacrylamide aqueous solution.

本発明でいう糖類とは、フェノール硫酸法で検出できる糖類であり、硫酸によりフルフラールおよびフルフラール誘導体を生成する、単糖、多糖、およびその混合物であり、多糖においては、糖タンパクや糖脂質など糖複合体も含まれる。糖類は、酵素などの生体触媒などを用いる方法または化学合成法により製造されたものでもよく、また生物体により産生されたものでも、生物材料から分離したものでもよい。   The saccharides referred to in the present invention are saccharides that can be detected by the phenol-sulfuric acid method, and are monosaccharides, polysaccharides, and mixtures thereof that produce furfural and furfural derivatives with sulfuric acid. In polysaccharides, sugars such as glycoproteins and glycolipids are used. Complexes are also included. The saccharide may be produced by a method using a biocatalyst such as an enzyme or a chemical synthesis method, and may be produced by a living organism or separated from a biological material.

本発明で「生物体を用いて糖類含有液」とは、生物体が産生した糖類を含有する液体をいう。生物体を用いて調製した糖類含有液として、例えばin vitroで培養した微生物等の生物体の懸濁液の遠心上清そのもの、または該遠心上清から精製操作等により調製したものが挙げられる。生物体から調製した糖類含有液をアクリルアミド水溶液に添加することにより、本発明の糖類含有液を含むアクリルアミド水溶液を得ることができる。この場合、生物体により産生された糖類の濃度が低いときは、適宜糖類を添加してアクリルアミド水溶液中の糖類の濃度を調整することができる。   In the present invention, “a saccharide-containing liquid using an organism” refers to a liquid containing a saccharide produced by an organism. Examples of the saccharide-containing liquid prepared using the organism include, for example, the centrifugal supernatant itself of a suspension of an organism such as a microorganism cultured in vitro, or a solution prepared from the centrifugal supernatant by a purification operation or the like. An acrylamide aqueous solution containing the saccharide-containing liquid of the present invention can be obtained by adding a saccharide-containing liquid prepared from a living organism to the acrylamide aqueous solution. In this case, when the concentration of the saccharide produced by the organism is low, the concentration of the saccharide in the acrylamide aqueous solution can be adjusted by appropriately adding the saccharide.

本明細書中に記載する生物体とは、単離された動物、植物、微生物など、あらゆる生物を包含し、さらに動物または植物から単離された細胞、および動物または植物に由来する樹立細胞株、単離された微生物、およびこれらの細胞小器官を含む。また、これらの生物体は、自然界に存在するものそのものでもよく、人為的に遺伝子工学的な改変を加えたものでもよい。   The organisms described in this specification include all living organisms such as isolated animals, plants, microorganisms, and cells isolated from animals or plants, and established cell lines derived from animals or plants. Isolated microorganisms, and these organelles. These organisms may be those existing in nature, or may be artificially modified by genetic engineering.

本発明でいう糖類の濃度は、フェノール硫酸法で測定されるグルコース換算値で示している。フェノール硫酸法については、例えば、日本生化学会編「基礎生化学実験法」第5巻118頁に詳細な測定法が記載されている。即ち、グルコースを用いてグルコース濃度と吸光度により検量線を作成し、その検量線に基づいて求められた値である。尚、本明細書中でいうフェノール硫酸法は、前述の日本生化学会編「基礎生化学実験法」第5巻118頁に則って実施したものであり、その詳細を以下に示す。   The concentration of saccharides referred to in the present invention is indicated by a glucose conversion value measured by the phenol-sulfuric acid method. The phenol sulfuric acid method is described in detail in, for example, “Basic Biochemical Experimental Method”, Volume 5, page 118, edited by Japanese Biochemical Society. That is, it is a value obtained based on a calibration curve created by glucose concentration and absorbance using glucose. The phenol sulfuric acid method referred to in the present specification was carried out in accordance with the above-mentioned “Basic Biochemical Experimental Method”, Volume 5, page 118, edited by the Japanese Biochemical Society, and the details thereof are shown below.

(1)特級フェノールと蒸留水を使用して5質量%のフェノール水溶液を作成する。(2)直径16.5mmの試験管に、試料溶液1mLを採取し、それに(1)の溶液1mLを加え、よく混和する。(3)これに特級濃硫酸5mLを速やかに加え、10分間混和しながら振盪する。(4)室温に20分間放置後、490nmの吸光度を測定する。この吸光度の値とグルコースを用いて作成した検量線を用いて、試料溶液中の糖類のグルコース換算濃度を算出する。   (1) A 5 mass% phenol aqueous solution is prepared using special grade phenol and distilled water. (2) Collect 1 mL of the sample solution in a test tube with a diameter of 16.5 mm, add 1 mL of the solution of (1) to it, and mix well. (3) To this, immediately add 5 mL of special grade concentrated sulfuric acid, and shake while mixing for 10 minutes. (4) After standing at room temperature for 20 minutes, the absorbance at 490 nm is measured. Using this absorbance value and a calibration curve created using glucose, the glucose equivalent concentration of the saccharide in the sample solution is calculated.

本発明において、アクリルアミド水溶液中の糖濃度の下限値はアクリルアミド水溶液中0.1mg/L以上が好ましく1mg/L以上がより好ましく、特に好ましくは3mg/L以上である。また上限値は100mg/L以下が好ましく50mg/L以下がより好ましく、特に好ましくは19mg/L以下である。該糖濃度は、十分に粘度向上効果を発揮させるという観点からは高いほうが好ましく、生産コストの観点からは低いほうが好ましい。   In the present invention, the lower limit of the sugar concentration in the acrylamide aqueous solution is preferably 0.1 mg / L or more in the acrylamide aqueous solution, more preferably 1 mg / L or more, and particularly preferably 3 mg / L or more. The upper limit is preferably 100 mg / L or less, more preferably 50 mg / L or less, and particularly preferably 19 mg / L or less. The sugar concentration is preferably high from the viewpoint of sufficiently exerting the effect of improving the viscosity, and is preferably low from the viewpoint of production cost.

本発明のニトリルヒドラターゼ活性を有する生体触媒には、天然または人為的にニトリルヒドラターゼ酵素活性を含有する生物体およびその処理物、ならびにニトリルヒドラターゼ酵素自身が包含される。この場合、生物体は微生物であることが好ましい。ニトリルヒドラターゼ酵素を発現しうる微生物としては、例えば、バチルス(Bacillus)属、バクテリジューム(Bacteridium)属、ミクロコッカス(Micrococcus)属およびブレビバクテリウム(Brevibacterium)属、コリネバクテリウム(Corynebacterium)属およびノカルジア(Nocardia)属、シュードモナス(Pseudomonas)属、ロドコッカス(Rhodococcus)属およびミクロバクテリウム(Microbacterium)属、ロドコッカスロドクロウス(Rhodococcusrhodochrous)種、ロドコッカス(Rhodococcus)属菌株等の微生物を挙げることができる。   The biocatalyst having nitrile hydratase activity of the present invention includes organisms and their treated products that naturally or artificially contain nitrile hydratase enzyme activity, and the nitrile hydratase enzyme itself. In this case, the organism is preferably a microorganism. Examples of microorganisms that can express the nitrile hydratase enzyme include, for example, the genus Bacillus, the genus Bacteridium, the genus Micrococcus, the genus Brevibacterium, the genus Corynebacterium, and the genus Corynebacterium. Examples include microorganisms such as Nocardia, Pseudomonas, Rhodococcus, and Microbacterium, Rhodococcusrhodochrous, and Rhodococcus.

また、近年天然のあるいは人為的に改良したニトリルヒドラターゼ遺伝子を人為的に組込んで発現させた生物体、またはこれらから単離したニトリルヒドラターゼ酵素(精製したものでも粗精製のものでもよい)もまた、本発明に使用可能である。   In addition, in recent years, natural or artificially improved nitrile hydratase genes that have been artificially incorporated and expressed, or nitrile hydratase enzymes isolated from these organisms (purified or crudely purified) may be used. Can also be used in the present invention.

生物体およびその処理物には、必要に応じて洗浄や薬剤処理を行った生物体そのものおよびこれらの破砕物、ならびにこれらを包括法、架橋法、担体結合法等で固定化したものなどが挙げられる。   Examples of organisms and processed products thereof include organisms that have been washed or treated with chemicals as necessary and their crushed materials, and those that have been immobilized by a comprehensive method, a crosslinking method, a carrier binding method, or the like. It is done.

本明細書中における「生体触媒」は、上述の微生物等の生物体そのもの、または該生物体またはその処理物を含む懸濁液や、これを固定化した担体を液体に浸漬させた生体触媒系をも含む。   The “biocatalyst” in the present specification refers to a biocatalyst system in which a living organism such as the above-described microorganism, or a suspension containing the living organism or a processed product thereof, or a carrier on which this is immobilized is immersed in a liquid. Is also included.

ニトリルヒドラーゼ活性を有する生体触媒を用いることにより、還元状態の銅を触媒として使用する必要が無く、その反応条件が温和で副生成物も殆ど無く、極めてシンプルなプロセスで工業的規模でアクリルアミドを製造することができる。   By using a biocatalyst having nitrile hydrase activity, it is not necessary to use reduced copper as a catalyst, the reaction conditions are mild, there are few by-products, and acrylamide can be produced on an industrial scale with a very simple process. Can be manufactured.

本発明の「糖類をアクリルアミド水溶液1L当たり1〜100mg含むアクリルアミド水溶液」は以下のようにして製造することができる。   The “acrylamide aqueous solution containing 1 to 100 mg of saccharide per liter of acrylamide aqueous solution” of the present invention can be produced as follows.

アクリルアミド500gを蒸留水を用いて1Lに溶解し、フェノール硫酸法でグルコース換算糖類濃度がアクリルアミド水溶液1L当たり1〜100mgとなるように糖類の水溶液を添加することで上記アクリルアミド水溶液が得られる。この際、溶解するアクリルアミドの量は、400〜600gの範囲で変えて最終的に得られる水溶液のアクリルアミド含量を40〜60重量%としてもよい。また、ここで添加される糖類は、精製されたものでも、未精製のものでもよい。用いるアクリルアミドは、市販のものでもよく、またはアクリロニトリルから生体触媒を用いて製造したアクリルアミド水溶液を、精製し、または精製せずに、アクリルアミド濃度が40〜60重量%となるように調製したものでもよい。   The acrylamide aqueous solution can be obtained by dissolving 500 g of acrylamide in 1 L using distilled water and adding an aqueous solution of saccharides such that the glucose-converted saccharide concentration is 1 to 100 mg per 1 L of acrylamide aqueous solution by the phenol-sulfuric acid method. At this time, the amount of acrylamide to be dissolved may be changed within the range of 400 to 600 g, and the acrylamide content of the finally obtained aqueous solution may be 40 to 60% by weight. The saccharide added here may be either purified or unpurified. The acrylamide to be used may be a commercially available product, or may be prepared by purifying or not purifying an acrylamide aqueous solution produced from acrylonitrile using a biocatalyst so that the acrylamide concentration is 40 to 60% by weight. .

また、上記糖類を含むアクリルアミド水溶液を、生体触媒を用いてアクリロニトリルから製造する場合は、生体触媒中の糖類の濃度を測定し、その濃度が反応終了後のアクリルアミド水溶液1L当たり1〜100mgとなるように生体触媒を添加し、アクリロニトリルを生体触媒に接触させて反応させることもできる。ここで、生体触媒中の糖類とは、微生物等の生体触媒そのものを懸濁させた液体または担体などに固定化した生体触媒を浸漬している液体中の糖類をいう。より具体的には原料であるアクリロニトリルと水、および糖類を含んだ生体触媒を0から90℃、好ましくは5から50℃で反応槽内で接触させることにより得ることができる。必要に応じて重合防止作用を持つ薬剤や触媒の安定性向上に寄与する薬剤等を反応液あるいは生体触媒懸濁液に添加することも可能である。反応様式としては、固定層、移動層、流動層、撹拌槽等の何れでもよく、また回分反応でも連続反応でも良い。また、反応槽にフェノール硫酸法でグルコース換算糖類濃度が反応終了後のアクリルアミド水溶液1L当たり1〜100mgとなるように糖類水溶液を添加して、生体触媒とアクリロニトリルを該反応槽内で反応させてもよい。   Moreover, when manufacturing the acrylamide aqueous solution containing the said saccharides from acrylonitrile using a biocatalyst, the density | concentration of the saccharide in a biocatalyst is measured, and the density | concentration will be 1-100 mg per liter of acrylamide aqueous solution after completion | finish of reaction. It is also possible to add a biocatalyst to acrylonitrile and bring it into contact with the biocatalyst for reaction. Here, the saccharide in the biocatalyst refers to a saccharide in a liquid in which a biocatalyst such as a microorganism is suspended or in a liquid in which a biocatalyst immobilized on a carrier is immersed. More specifically, it can be obtained by bringing a raw material acrylonitrile, water, and a biocatalyst containing sugars into contact at 0 to 90 ° C., preferably 5 to 50 ° C., in a reaction vessel. If necessary, it is also possible to add a drug having a polymerization-inhibiting action, a drug contributing to improving the stability of the catalyst, or the like to the reaction solution or the biocatalyst suspension. The reaction mode may be any of a fixed bed, a moving bed, a fluidized bed, a stirring tank, etc., and may be a batch reaction or a continuous reaction. Alternatively, an aqueous saccharide solution may be added to the reaction tank so that the glucose-converted saccharide concentration is 1 to 100 mg per liter of the acrylamide aqueous solution after completion of the reaction by the phenol sulfuric acid method, and the biocatalyst and acrylonitrile are reacted in the reaction tank. Good.

さらに、糖類を産生し得る、ニトリルヒドラターゼ活性を有する生体触媒に、アクリルアミドの産生と同時に糖類を産生させることも可能である。   Furthermore, it is also possible to produce a saccharide simultaneously with the production of acrylamide on a biocatalyst having nitrile hydratase activity that can produce a saccharide.

この様にして得られたアクリルアミド水溶液は、その用途に応じて精製工程を経ることも可能である。精製方法としては、フィルターによる濾過(特公平05−49273)や気泡による精製(特願平11−254151)等があげられる。   The acrylamide aqueous solution thus obtained can be subjected to a purification step depending on its use. Examples of the purification method include filtration with a filter (Japanese Patent Publication No. 05-49273), purification with bubbles (Japanese Patent Application No. 11-254151), and the like.

このようにして得られたアクリルアミド水溶液を原料として、公知のアクリルアミド重合化法と同様の方法により、ポリアクリルアミド水溶液を得ることができる。このようにして本発明のアクリルアミド水溶液から得られるポリアクリルアミド水溶液は、アクリルアミド濃度が同一の糖類を含まないアクリルアミド水溶液から得られたポリアクリルアミド水溶液に比べて、粘度が上昇している。該ポリアクリルアミド水溶液は、アクリルアミド系重合体として、高分子凝集剤、製紙用薬剤、土壌改良剤、石油回収用薬剤、掘削泥水用増粘剤、高分子吸収体等などに利用することができる。従って、本発明のアクリルアミド水溶液から得られるポリアクリルアミド重合体も本発明の範囲に包含される。   Using the acrylamide aqueous solution thus obtained as a raw material, a polyacrylamide aqueous solution can be obtained by a method similar to a known acrylamide polymerization method. Thus, the viscosity of the polyacrylamide aqueous solution obtained from the acrylamide aqueous solution of the present invention is higher than that of the polyacrylamide aqueous solution obtained from the acrylamide aqueous solution containing no saccharide having the same acrylamide concentration. The polyacrylamide aqueous solution can be used as an acrylamide polymer for polymer flocculants, papermaking chemicals, soil conditioners, oil recovery chemicals, drilling mud thickeners, polymer absorbers, and the like. Therefore, the polyacrylamide polymer obtained from the acrylamide aqueous solution of the present invention is also included in the scope of the present invention.

得られたポリアクリルアミド水溶液の物性評価は、例えば、粘度計を用いて重合体の粘度を測定して行うことができる。具体的には、B型粘度計を用いて公知の方法で測定することにより評価することができる。   The physical properties of the obtained polyacrylamide aqueous solution can be evaluated, for example, by measuring the viscosity of the polymer using a viscometer. Specifically, it can be evaluated by measuring by a known method using a B-type viscometer.

本発明は、(1)糖類を含むアクリルアミド水溶液、(2)糖類をアクリルアミド水溶液1L当たり0.1〜100mg含むアクリルアミド水溶液、(3)糖類をアクリルアミド水溶液1L当たり1.0〜50mg含むアクリルアミド水溶液、(4)糖類をアクリルアミド水溶液1L当たり3.0〜19mg含むアクリルアミド水溶液、(5)in vitroで培養した生物体を用いて調製した糖類含有液を添加した、上記1〜4のいずれかに記載の糖類を含むアクリルアミド水溶液、(6)生物体がニトリルヒドラターゼ酵素を発現するものである、上記5記載の糖類を含むアクリルアミド水溶液、(7)ニトリルヒドラターゼ酵素を発現するものが微生物である、上記6記載の糖類を含むアクリルアミド水溶液、(8)微生物がロドコッカス属細菌である、上記7記載の糖類を含むアクリルアミド水溶液、(9)ロドコッカス属細菌がロドコッカス・ロドクロウスである、上記8記載の糖類を含むアクリルアミド水溶液、(10)ニトリルヒドラターゼ活性を有する生体触媒により製造される、上記1〜9のいずれか1項に記載の糖類を含むアクリルアミド水溶液、(11)上記1〜10のいずれか1項に記載の糖類を含むアクリルアミド水溶液であって、該アクリルアミド水溶液から得られるポリアクリルアミド溶液の粘度が、該アクリルアミド水溶液と等濃度になるようにアクリルアミドのみを水に溶解させたアクリルアミド水溶液から得られる重合体の粘度より高い、糖類を含むアクリルアミド重合体、(12)上記1〜11のいずれか1項に記載の糖類を含むアクリルアミド水溶液から得られるポリアクリルアミド重合体、(13)ニトリルヒドラターゼ活性を有し糖類を含有する生体触媒を用いてアクリルアミドを産生することを含む、糖類を含むアクリルアミド水溶液の製造方法にも関する。   The present invention includes (1) an acrylamide aqueous solution containing saccharides, (2) an acrylamide aqueous solution containing 0.1 to 100 mg of saccharides per liter of acrylamide aqueous solution, (3) an acrylamide aqueous solution containing 1.0 to 50 mg of saccharides per liter of acrylamide aqueous solution, 4) The saccharide according to any one of 1 to 4 above, wherein an acrylamide aqueous solution containing 3.0 to 19 mg of saccharide per liter of the acrylamide aqueous solution and (5) a saccharide-containing liquid prepared using an organism cultured in vitro are added. (6) An acrylamide aqueous solution containing the saccharide according to 5 above, wherein the organism expresses a nitrile hydratase enzyme, and (7) A microorganism that expresses the nitrile hydratase enzyme is a microorganism. (8) the microorganism is Rhodococcus bacterium, An acrylamide aqueous solution containing the saccharide according to 7 above, (9) an acrylamide aqueous solution containing the saccharide according to 8 above, wherein the Rhodococcus bacterium is Rhodococcus rhodochrous, and (10) a biocatalyst having nitrile hydratase activity. An acrylamide aqueous solution containing the saccharide according to any one of 1 to 9 above, (11) an acrylamide aqueous solution containing the saccharide according to any one of 1 to 10 above, wherein the polyacrylamide is obtained from the acrylamide aqueous solution. An acrylamide polymer containing saccharides, which is higher than the viscosity of a polymer obtained from an acrylamide aqueous solution in which only acrylamide is dissolved in water so that the viscosity of the acrylamide solution is equal to that of the aqueous acrylamide solution, (12) 1 to 11 above An acrylamide aqueous solution containing the saccharide according to any one of And (13) a method for producing an aqueous solution of acrylamide containing saccharides, comprising producing acrylamide using a biocatalyst having nitrile hydratase activity and containing saccharides.

本発明を以下の実施例によって具体的に説明するが、本発明はこれらの実施例によって限定されるものではない。   The present invention will be specifically described by the following examples, but the present invention is not limited to these examples.

実施例1、比較例1に、市販のアクリルアミド水溶液から調製したポリアクリルアミドの場合、実施例2、比較例2にアクリロニトリルから糖類を含む生体触媒を用いて製造したアクリルアミドから調製したポリアクリルアミドの場合を記載した。   In the case of polyacrylamide prepared from a commercially available acrylamide aqueous solution in Example 1 and Comparative Example 1, the case of polyacrylamide prepared from acrylamide produced using a biocatalyst containing saccharides from acrylonitrile in Example 2 and Comparative Example 2. Described.

〔実施例1〕
(糖類含有液の調製)
ロドコッカス・ロドクロウスRhodococcus rhodochrous J1(受託番号FERM BP-1478で、工業技術院生命工学工業技術研究所(現在は、独立行政法人産業技術総合研究所 特許生物寄託センター、茨城県つくば市東1丁目1番1中央第6)に寄託されている)を、グルコース2%、尿素1%、ペプトン0.5%、酵母エキス0.3%、塩化コバルト0.05%(何れも質量%)を含む培地(pH7.0)により30℃で好気的に培養した。これをポリスルホン性の孔径0.1μmのメンブランフィルター(クラレ社製)を用いて、培養液の5倍量の50mMリン酸緩衝液(pH7.0)にて連続的に洗浄した後、菌濃度を乾燥菌体重量で10%となるまで濃縮し菌体懸濁液を得た。
これを50mLの遠心チューブにとり、遠心分離機により15,000×gで30分遠心し、その遠心上清を糖類含有液とした。
[Example 1]
(Preparation of saccharide-containing liquid)
Rhodococcus rhodochrous J1 (accession number FERM BP-1478, Biotechnology Institute of Industrial Technology, National Institute of Advanced Industrial Science and Technology 6), a medium (pH 7) containing 2% glucose, 1% urea, 0.5% peptone, 0.3% yeast extract, 0.05% cobalt chloride (both mass%). 0.0) and aerobically cultured at 30 ° C. Using a polysulfone membrane filter (manufactured by Kuraray Co., Ltd.) having a pore size of 0.1 μm, this was continuously washed with 5 times the amount of 50 mM phosphate buffer (pH 7.0). The cells were concentrated to 10% by dry cell weight to obtain a cell suspension.
This was taken in a 50 mL centrifuge tube and centrifuged at 15,000 × g for 30 minutes with a centrifuge, and the centrifuged supernatant was used as a saccharide-containing solution.

(糖類含有液中の糖濃度の測定)
得られた糖類含有液中の糖濃度をフェノール硫酸法で以下の通り測定した。
(1)特級フェノールと蒸留水を使用して5質量%のフェノール水溶液を作成した。(2)直径16.5mmの試験管に、1000倍に希釈した溶液1mLを採取し、それに(1)の溶液1mLを加え、よく混和した。(3)これに特級濃硫酸5mLを速やかに加え、10分間混和しながら振盪した後、室温に20分間放置後、490nmの吸光度を測定した。一方同様の操作を、2,10,50,100mg/Lに調整したグルコース水溶液を用いて検量線を作成し、その検量線から糖類含有液中の糖濃度を算出したところ、15000mg/Lとなった。該糖類含有液中の糖類は、理論に拘束されることはないが、菌体により産生された多糖類であると推測される。
(Measurement of sugar concentration in sugar-containing liquid)
The sugar concentration in the obtained saccharide-containing liquid was measured by the phenol sulfuric acid method as follows.
(1) A 5% by mass phenol aqueous solution was prepared using special grade phenol and distilled water. (2) Into a test tube having a diameter of 16.5 mm, 1 mL of the 1000-fold diluted solution was sampled, and 1 mL of the solution (1) was added thereto and mixed well. (3) To this, 5 mL of special grade concentrated sulfuric acid was quickly added, shaken while mixing for 10 minutes, and allowed to stand at room temperature for 20 minutes, and then the absorbance at 490 nm was measured. On the other hand, a calibration curve was prepared using a glucose aqueous solution adjusted to 2, 10, 50, and 100 mg / L in the same manner, and the sugar concentration in the saccharide-containing solution was calculated from the calibration curve, which was 15000 mg / L. It was. The saccharide in the saccharide-containing liquid is not limited by theory, but is presumed to be a polysaccharide produced by cells.

(糖類含有アクリルアミド水溶液の調製)
50質量%アクリルアミド水溶液(三菱レイヨン社製)1Lに、調製した糖類含有液0.2mLを添加して糖類含有アクリルアミド水溶液を作成した。
(Preparation of saccharide-containing acrylamide aqueous solution)
A saccharide-containing acrylamide aqueous solution was prepared by adding 0.2 mL of the prepared saccharide-containing liquid to 1 L of a 50 mass% acrylamide aqueous solution (manufactured by Mitsubishi Rayon Co., Ltd.).

(ポリアクリルアミド水溶液の調製)
得られた糖類含有アクリルアミド水溶液を、アクリルアミドの濃度が15質量%となるように蒸留水を用いて希釈し、pH6.1に調整後、フラスコを30℃の水槽にて攪拌しながら保温した。気相部を窒素置換しながら、過硫酸アンモニウム、亜硫酸水素ナトリウムが各々180mg/Lとなるよう加えて重合を開始すると同時に、水槽の温度を80℃にした。約1時間後、25℃まで氷冷した。
(Preparation of polyacrylamide aqueous solution)
The obtained saccharide-containing acrylamide aqueous solution was diluted with distilled water so that the concentration of acrylamide was 15% by mass, adjusted to pH 6.1, and then the flask was kept warm with stirring in a 30 ° C. water bath. While replacing the gas phase with nitrogen, ammonium persulfate and sodium hydrogen sulfite were added to give 180 mg / L each, and the polymerization was started. At the same time, the temperature of the water bath was raised to 80 ° C. After about 1 hour, the mixture was ice-cooled to 25 ° C.

(ポリアクリルアミド水溶液の物性評価)
得られた水溶液の粘度を、B型粘度計にて測定した(No.4ロータ、6rpm、25℃)。その結果を表1に示す。
(Physical property evaluation of polyacrylamide aqueous solution)
The viscosity of the obtained aqueous solution was measured with a B-type viscometer (No. 4 rotor, 6 rpm, 25 ° C.). The results are shown in Table 1.

〔比較例1〕
ポリアクリルアミド水溶液の調製を、糖類含有液を添加していない50質量%アクリルアミド水溶液(三菱レイヨン社製)を用いて実施例1同様に行い、得られたポリアクリルアミド水溶液の評価を実施した。結果を表1に示す。
[Comparative Example 1]
The polyacrylamide aqueous solution was prepared in the same manner as in Example 1 using a 50 mass% acrylamide aqueous solution (Mitsubishi Rayon Co., Ltd.) to which no saccharide-containing solution was added, and the resulting polyacrylamide aqueous solution was evaluated. The results are shown in Table 1.

Figure 2007277563
Figure 2007277563

〔実施例2〕
(微生物酵素によるアクリロニトリルからアクリルアミドへの反応)
内容積5Lのジャケット付きセパラブルフラスコに0.2g/Lのアクリル酸ナトリウム水溶液を3130g入れ、これに実施例1の(糖類含有液の調製)時に得られた菌体懸濁液10g(糖類を約10000mg/L含む)を添加した。これをpH7.0、温度20℃に制御しながら翼長120mm、翼幅20mmの平板の撹拌翼を2枚にて80rpmで攪拌した。アクリロニトリル濃度が常に2質量%となるようにアクリロニトリル(三菱レイヨン社製)を連続的にフィードし、アクリルアミドの濃度が47%となった時点でアクリロニトリルのフィードを停止し、その後アクリロニトリルが0.005%以下になるまで反応を継続した。この液から孔径0.1μmのポリエチレン製中空糸膜(三菱レイヨン製ステラポア−H)にて菌体を分離しアクリルアミド濃度50質量%の反応液5kgを得た。
[Example 2]
(Reaction from acrylonitrile to acrylamide by microbial enzyme)
3130 g of 0.2 g / L sodium acrylate aqueous solution was placed in a jacketed separable flask having an internal volume of 5 L, and 10 g of the bacterial cell suspension obtained in Example 1 (preparation of saccharide-containing liquid) About 10,000 mg / L) was added. Two flat stirring blades having a blade length of 120 mm and a blade width of 20 mm were stirred at 80 rpm while controlling the pH at 7.0 and a temperature of 20 ° C. Acrylonitrile (manufactured by Mitsubishi Rayon Co., Ltd.) is continuously fed so that the acrylonitrile concentration is always 2% by mass. When the acrylamide concentration reaches 47%, the acrylonitrile feed is stopped, and then acrylonitrile is 0.005%. The reaction was continued until: From this solution, the cells were separated with a polyethylene hollow fiber membrane (Mitsubishi Rayon Stellapore-H) having a pore size of 0.1 μm to obtain 5 kg of a reaction solution having an acrylamide concentration of 50 mass%.

(50質量%アクリルアミド中の糖濃度の測定)
実施例1の(糖類含有液中の糖濃度の測定)と同様に、得られた50質量%アクリルアミド水溶液の糖濃度を測定した。ただしグルコース濃度への換算に際しては、既知量のグルコースを市販のアクリルアミド粉末(和光純薬社製)にて作成した50質量%アクリルアミド水溶液に溶解させたものを使用した。その結果、糖濃度は19mg/Lであった。
(Measurement of sugar concentration in 50% by mass acrylamide)
In the same manner as in Example 1 (Measurement of sugar concentration in saccharide-containing liquid), the sugar concentration of the obtained 50 mass% acrylamide aqueous solution was measured. However, when converting into the glucose concentration, a solution obtained by dissolving a known amount of glucose in a 50% by mass acrylamide aqueous solution prepared with a commercially available acrylamide powder (manufactured by Wako Pure Chemical Industries, Ltd.) was used. As a result, the sugar concentration was 19 mg / L.

(ポリアクリルアミド水溶液の物性評価)
得られたアクリルアミド水溶液を用いて、実施例1同様にポリアクリルアミド水溶液を調製しその物性を測定した。
その結果溶液粘度190000mPa・sであった。
(Physical property evaluation of polyacrylamide aqueous solution)
Using the obtained aqueous acrylamide solution, a polyacrylamide aqueous solution was prepared in the same manner as in Example 1 and its physical properties were measured.
As a result, the solution viscosity was 190,000 mPa · s.

Claims (10)

糖類をアクリルアミド水溶液1L当たり0.1〜100mg含み、かつ40〜60質量%のアクリルアミド含量を有するアクリルアミド水溶液を原料として用いて、アクリルアミド重合化を行うことにより、ポリアクリルアミドを製造する方法。   A method for producing polyacrylamide by performing acrylamide polymerization using an acrylamide aqueous solution containing 0.1 to 100 mg of saccharide per liter of acrylamide aqueous solution and having an acrylamide content of 40 to 60% by mass as a raw material. 前記アクリルアミド水溶液が1L当たり1.0〜50mgの糖類を含む、請求項1記載の方法。   The method according to claim 1, wherein the acrylamide aqueous solution contains 1.0 to 50 mg of saccharide per liter. 前記アクリルアミド水溶液が1L当たり3.0〜19mgの糖類を含む、請求項1記載の方法。   The method according to claim 1, wherein the aqueous acrylamide solution contains 3.0 to 19 mg of saccharide per liter. 前記アクリルアミド水溶液が、微生物から調製した糖類含有液をアクリルアミド水溶液に添加して得られるものである、請求項1〜3のいずれか1項記載の方法。   The method according to any one of claims 1 to 3, wherein the acrylamide aqueous solution is obtained by adding a saccharide-containing solution prepared from a microorganism to an acrylamide aqueous solution. 微生物がニトリルヒドラターゼ酵素を発現するものである、請求項4記載の方法。   The method according to claim 4, wherein the microorganism expresses a nitrile hydratase enzyme. 微生物がロドコッカス属細菌である、請求項5記載の方法。   The method according to claim 5, wherein the microorganism is a Rhodococcus bacterium. ロドコッカス属細菌がロドコッカス・ロドクロウスである、請求項6記載の方法。   The method according to claim 6, wherein the Rhodococcus bacterium is Rhodococcus rhodochrous. ニトリルヒドラターゼ活性を有する生体触媒により製造される、請求項1〜7のいずれか1項記載の方法。   The method according to any one of claims 1 to 7, which is produced by a biocatalyst having nitrile hydratase activity. 前記アクリルアミド水溶液が、ニトリルヒドラターゼ活性を有し糖類を含有する生体触媒を用いて産生されたものである、請求項1〜8のいずれか1項記載の方法。   The method according to any one of claims 1 to 8, wherein the acrylamide aqueous solution is produced using a biocatalyst having nitrile hydratase activity and containing a saccharide. 請求項1〜9のいずれか1項に記載の方法により製造されるポリアクリルアミド。   The polyacrylamide manufactured by the method of any one of Claims 1-9.
JP2007119365A 2007-04-27 2007-04-27 Polyacrylamide and method for producing the same Expired - Fee Related JP5132979B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007119365A JP5132979B2 (en) 2007-04-27 2007-04-27 Polyacrylamide and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007119365A JP5132979B2 (en) 2007-04-27 2007-04-27 Polyacrylamide and method for producing the same

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2002081512A Division JP2003277416A (en) 2002-03-22 2002-03-22 Aqueous acrylamide solution containing saccharides

Publications (2)

Publication Number Publication Date
JP2007277563A true JP2007277563A (en) 2007-10-25
JP5132979B2 JP5132979B2 (en) 2013-01-30

Family

ID=38679318

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007119365A Expired - Fee Related JP5132979B2 (en) 2007-04-27 2007-04-27 Polyacrylamide and method for producing the same

Country Status (1)

Country Link
JP (1) JP5132979B2 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0655148B2 (en) * 1987-09-18 1994-07-27 秀明 山田 Biological production method of amide
JPH09118704A (en) * 1995-08-21 1997-05-06 Nitto Chem Ind Co Ltd Production of water-in-oil high-molecular-weight polymer emulsion
JPH10316714A (en) * 1997-05-15 1998-12-02 Mitsubishi Rayon Co Ltd Production of acrylamide polymer
JP2001081697A (en) * 1999-07-13 2001-03-27 Japan Pmc Corp Modifier for paper, paper and production of paper

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0655148B2 (en) * 1987-09-18 1994-07-27 秀明 山田 Biological production method of amide
JPH09118704A (en) * 1995-08-21 1997-05-06 Nitto Chem Ind Co Ltd Production of water-in-oil high-molecular-weight polymer emulsion
JPH10316714A (en) * 1997-05-15 1998-12-02 Mitsubishi Rayon Co Ltd Production of acrylamide polymer
JP2001081697A (en) * 1999-07-13 2001-03-27 Japan Pmc Corp Modifier for paper, paper and production of paper

Also Published As

Publication number Publication date
JP5132979B2 (en) 2013-01-30

Similar Documents

Publication Publication Date Title
WO2016050817A1 (en) Method for producing acrylamide from acrylonitrile in an aqueous solution
JP5750442B2 (en) Low molecular weight hyaluronic acid production method
EP2264003B1 (en) Method for stabilization of aqueous acrylamide solution
RU2343161C2 (en) Acrylamide water solution, which contains saccharide
JP4668444B2 (en) A method for producing acrylamide using a microbial catalyst washed with an aqueous acrylic acid solution.
AU2004227248B2 (en) Process for producing high-quality acrylamide polymer with enzyme
JP5132979B2 (en) Polyacrylamide and method for producing the same
WO2003033716A1 (en) Process for producing acrylamide and/or methacrylamide with microorganism catalyst
JP5430659B2 (en) Method for producing treated bacterial cells
WO2004081212A1 (en) Novel polyvinyl alcohol-digesting bacterium
Khan et al. Simple fed-batch cultivation strategy for the enhanced production of a single-sugar glucuronic acid-based oligosaccharides by a cellulose-producing Gluconacetobacter hansenii strain
JP5975236B2 (en) Biopolymer production method
RU2468084C1 (en) Biotechnological method of obtaining acrylamide
JPH0319695A (en) Preparation of trans-4-cyanocyclohexane carboxylic amide and enzyme used therefor
JP5622894B2 (en) Thickener
JP2012062476A (en) Method for producing thickener
JP2004283128A (en) Method for producing high-quality (meth)acrylamide polymer using biocatalyst
JPH05308985A (en) Production of polyfructan

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100803

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20101004

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20101102

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20110112

A911 Transfer of reconsideration by examiner before appeal (zenchi)

Free format text: JAPANESE INTERMEDIATE CODE: A911

Effective date: 20110209

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20121107

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20151116

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R370 Written measure of declining of transfer procedure

Free format text: JAPANESE INTERMEDIATE CODE: R370

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees