JPH0429794B2 - - Google Patents
Info
- Publication number
- JPH0429794B2 JPH0429794B2 JP63314408A JP31440888A JPH0429794B2 JP H0429794 B2 JPH0429794 B2 JP H0429794B2 JP 63314408 A JP63314408 A JP 63314408A JP 31440888 A JP31440888 A JP 31440888A JP H0429794 B2 JPH0429794 B2 JP H0429794B2
- Authority
- JP
- Japan
- Prior art keywords
- pitch
- pulp
- enzyme
- mechanical pulp
- fatty acid
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 claims abstract description 35
- 229920001131 Pulp (paper) Polymers 0.000 claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 claims abstract description 12
- 108090000790 Enzymes Proteins 0.000 claims description 32
- 102000004190 Enzymes Human genes 0.000 claims description 32
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 18
- 239000000194 fatty acid Substances 0.000 claims description 18
- 229930195729 fatty acid Natural products 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 10
- 244000005700 microbiome Species 0.000 claims description 8
- 241000228245 Aspergillus niger Species 0.000 claims description 3
- 241000589540 Pseudomonas fluorescens Species 0.000 claims description 3
- 241000589538 Pseudomonas fragi Species 0.000 claims description 3
- 241000179532 [Candida] cylindracea Species 0.000 claims description 3
- 241000159512 Geotrichum Species 0.000 claims description 2
- 230000008569 process Effects 0.000 abstract description 20
- 239000004367 Lipase Substances 0.000 abstract description 3
- 102000004882 Lipase Human genes 0.000 abstract description 3
- 108090001060 Lipase Proteins 0.000 abstract description 3
- 235000019421 lipase Nutrition 0.000 abstract description 3
- 239000011347 resin Substances 0.000 abstract description 3
- 229920005989 resin Polymers 0.000 abstract description 3
- 239000011295 pitch Substances 0.000 description 56
- 229940088598 enzyme Drugs 0.000 description 31
- 239000000123 paper Substances 0.000 description 18
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 8
- 238000004537 pulping Methods 0.000 description 8
- 239000002023 wood Substances 0.000 description 8
- 230000002209 hydrophobic effect Effects 0.000 description 7
- -1 polyoxyethylene Polymers 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 150000003626 triacylglycerols Chemical class 0.000 description 6
- 108090000604 Hydrolases Proteins 0.000 description 5
- 102000004157 Hydrolases Human genes 0.000 description 5
- 239000004698 Polyethylene Substances 0.000 description 5
- 238000009825 accumulation Methods 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000000593 degrading effect Effects 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 229920000573 polyethylene Polymers 0.000 description 5
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 5
- 240000006055 Dacrydium cupressinum Species 0.000 description 4
- 235000018782 Dacrydium cupressinum Nutrition 0.000 description 4
- 235000013697 Pinus resinosa Nutrition 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- 235000011194 food seasoning agent Nutrition 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- 239000000523 sample Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000002411 adverse Effects 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 235000000405 Pinus densiflora Nutrition 0.000 description 2
- 240000008670 Pinus densiflora Species 0.000 description 2
- 238000005411 Van der Waals force Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 241000222120 Candida <Saccharomycetales> Species 0.000 description 1
- 108010059892 Cellulase Proteins 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 244000168141 Geotrichum candidum Species 0.000 description 1
- 235000017388 Geotrichum candidum Nutrition 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 101001096190 Homo sapiens Pleckstrin homology domain-containing family A member 1 Proteins 0.000 description 1
- 241000498617 Mucor javanicus Species 0.000 description 1
- 108091005804 Peptidases Proteins 0.000 description 1
- 102100037862 Pleckstrin homology domain-containing family A member 1 Human genes 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 241000589516 Pseudomonas Species 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- 241000235527 Rhizopus Species 0.000 description 1
- 241000303962 Rhizopus delemar Species 0.000 description 1
- 241000588264 Rhizopus javanicus Species 0.000 description 1
- 241000235545 Rhizopus niveus Species 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000002156 adsorbate Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 125000005037 alkyl phenyl group Chemical group 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
- 239000003093 cationic surfactant Substances 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 229940059442 hemicellulase Drugs 0.000 description 1
- 108010002430 hemicellulase Proteins 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010297 mechanical methods and process Methods 0.000 description 1
- 230000005226 mechanical processes and functions Effects 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000011312 pitch solution Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000013055 pulp slurry Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011122 softwood Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
- D21C5/005—Treatment of cellulose-containing material with microorganisms or enzymes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/02—Agents for preventing deposition on the paper mill equipment, e.g. pitch or slime control
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Biochemistry (AREA)
- Microbiology (AREA)
- Paper (AREA)
- Working-Up Tar And Pitch (AREA)
- Diaphragms For Electromechanical Transducers (AREA)
- Making Paper Articles (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Mechanical Treatment Of Semiconductor (AREA)
- Materials For Medical Uses (AREA)
- Encapsulation Of And Coatings For Semiconductor Or Solid State Devices (AREA)
Abstract
Description
(産業上の利用分野)
本発明は、グラウンドウツドパルプ(以下GP
と略)等の機械パルプの製造工程あるいは機械パ
ルプを使用する製紙工程で生ずるピツチトラブル
を防止する方法に関するものものである。
(従来の技術)
GP等の機械パルプは、丸太あるいはチツプを
グラインダーあるいはリフアイナーで磨砕すると
いう簡単な機械的処理でパルプ化されるもので、
アルカリ等の化学薬品を使う化学パルプに比較し
て、強度では劣るが、収率が高く、コストも安
く、不透明度が高いという長所を有する。しか
し、その反面、機械的な磨砕をパルプ化の手段と
するために、木材成分がほとんど変化せずにパル
プ中に残留することになる。一般に木材はセスロ
ース、ヘミセルロース及びリグニンの主要3成分
の他に、有機溶媒抽出物であるピツチ成分を1〜
10%程度含んでいる。樹種によりピツチ成分は量
的、質的に異なるが、機械パルプの主原料である
針葉樹材は、脂肪酸、樹脂酸、脂肪酸グリセライ
ド等のピツチ成分を多量に含有していることが知
られている。これらピツチ成分はパルプ化の際に
一部がパルプから離脱して、浮遊状態になつた
り、繊維表面に付着し又は被覆した形となり、パ
ルプ化前の固定された状態から解き放たれた状態
となる。脱離し、白水中に浮遊しているピツチは
0.2〜2ミクロン程度の微粒子で、いわゆるコロ
イダルピツチといわれている。
一般に紙は各種パルプ化工程で製造されたパル
プが、精撰工程を経て製紙用資材と混合された
後、抄紙工程に送られて製品となる。この一連の
工程の中で、遊離の浮遊ピツチあるいは付着ピツ
チがパルプ、タンク、ワイヤー部あるいはロール
部等に堆積し、紙汚れや紙切れ等を起こし、いわ
ゆるピツチトラブルを生ずるのであり、機械パル
プが多量に配合された場合はピツチトラブルが頻
発し易い。
ピツチトラブルを防ぐ方法として従来から行わ
れてきた代表的な方法の一つは、原木の丸太を伐
採した後、屋外に積み上げて長期にわたつて放
置・枯化させるいわゆるシーズニングと呼ばれる
処理である。他の方法としては、例えば特公昭50
−22606号公報に記載されているように、パルプ
化及び抄紙工程で種々の付加モル数を有するポリ
オキシエチレンのアルキルエーテルあるいはアル
キルフエニル誘導体やそれらを主成分とする界面
活性剤を添加する方法が知られている。
(発明が解決しようとする課題)
上記シーズニング法によれば、材中のピツチ成
分は主に空気酸化により変質し減少するが、シー
ズニングには広大な土地と3ケ月から6ケ月、場
合によつてはそれ以上の期間を要するという問題
を抱えており、現状ではシーズニングのみによつ
てピツチトラブルを防止するのは困難である。一
方、界面活性剤を添加する方法は、微粒子ピツチ
を分散させ、堆積を阻止する効果があるとされて
いるが、根本的なピツチトラブル防止法とはなつ
ていない。
本発明は、機械パルプの製造工程あるいは機械
パルプを使用する抄紙工程において、依然として
大きな問題となつているピツチトラブルを防止す
る方法を提供しようとするものである。
(課題を解決するための手段)
本発明者らは、ピツチトラブル防止の有効手段
を見出すために、先ず機械パルプの代表的な原木
であるアカマツ材から抽出されたピツチ成分と、
アカマツを原木としてGPを製造する工程あるい
はアカマツGPを使用する抄紙工程で堆積したピ
ツチ成分を詳細に検索した結果、堆積したピツチ
の主成分は材由来の成分であり、特にトリグリセ
ライド及び脂肪酸、樹脂酸とその金属塩が多いこ
とが明らかになり、又堆積ピツチには常に多量の
トリグリセライドが含まれていることも明らかに
なつた。これらの結果から、トリグリセライドが
ピツチトラブルの主な原因物質の一つと推定され
る。
本発明者らは、ピツチトラブルの防止にはトリ
グリセライドを何等かの方法で分解・除去するこ
とが有効であるとの観点から種々の化学的、生化
学的方法を試みた結果、実際の工程におけるパル
プや紙の品質及び操業条件に悪影響を及ぼすこと
なく、トリグリセライドを分解し、ピツチの堆積
を防止するには、脂肪酸グリセライド加水分解酵
素を使用することが最適であることを見出し、本
発明を完成した。
即ち、本発明に係るピツチトラブルの防止方法
は、機械パルプの製造工程及び/又は機械パルプ
を使用する製紙工程において、製紙原料及び/又
は白水を脂肪酸グリセライド加水分解酵素で処理
して製紙原料及び/又は白水中のピツチを除去す
ることを請求項1の特徴とし、酵素として、アス
ペルギルス・ニガー(Aspergillus niger),シユ
ードモナス・フルオレツセンス(Pseudomonas
fluorescens),シユードモナス・フラジ(Pseudo
−monas fragi)、ゲオトリクム・カンデイデウ
ム(Geotrichum candidum),又はカンデイダ・
シリンドラセア(Candida cylindracea)から選
択される1種以上の微生物が生産する脂肪酸グリ
セライド加水分解酵素を使用することを請求項2
の特徴とするものである。
本発明に用いる酵素は、ピツチの主たる成分の
1つであるトリグリセライドを加水分解する酵素
である。脂肪酸グリセライド加水分解酵素であれ
ばどの種類でも効果があり、この酵素を生産する
微生物としてアスペルギルス・ニガー(Aspergi
−llus niger),シユードモナス・フルオレツセ
ンス(Pseudomonas fluorescens),シユードモ
ナス・フラジ(Pseudomonas fragi)、ゲオトリ
クム・カンデイデウム(Geotrichum
candidum)、カンデイダ・シリンドラセア
(Candida cylindracea),ムコール・ジヤワニク
ス(Mucor javanicus),リゾプス・ジヤワニク
ス(Rhizopus javanicus),リゾプス・デレマ
(Rhizopus delemar),リゾプス・ニベウス
(Rhizopus niveus),リゾプス(Rhizopus)属糸
状菌を例示することがきるが、上記例示中1〜5
番目に記載の微生物が生産する脂肪酸グリセライ
ド加水分解酵素は特に有効である。
また、上記の微生物が生産する脂肪酸グリセラ
イド分解酵素は、純粋なものほど効果があるが、
複数の酵素を併用しても良い。更に、本発明に用
いる脂肪酸グリセライド分解酵素は、セルラー
ゼ、ヘミセルラーゼ、プロテアーゼ等の他の分解
酵素と組合わせて使用しても十分な効果を発揮す
る。
機械パルプの製造工程或いは機械パルプを使用
する製紙工程において、これらの酵素を用いるに
は、グラインダー又はリフアイナーで磨砕して得
られる機械パルプを含有する製紙原料スラリーに
対して、前記酵素を機械パルプに対し重量比0.1
〜10000ppmを添加し、静置又は静かに攪拌する。
この場合、温度は10〜70℃が適当で、35〜55℃が
最適である。10℃以下では酵素の作用が鈍く、反
応速度が遅くなり、70℃以上では酵素が失活する
おそれがある。又、一般に酵素の添加量が多いほ
ど反応速度も大きくなるが、この場合、基質とな
るトリグリセライドの量から計算して機械パルプ
に対し10000ppmあれば充分であり、それ以上の
添加は経済的にも不利となる。さらに、PH範囲は
3〜11が適切で、この範囲以外では酵素の活性が
著しく阻害されてしまう。
又、パルプ化及び製紙工程では、多量の水を使
用しているが、大部分は循環・再使用している。
これらの循環白水はピツチ成分を含んでいるの
で、循環白水に対して酵素を適用することによつ
ても、ピツチトラブルを防止することができる。
この場合、前記脂肪酸グリセライド加水分解酵素
を白水に直接添加したり、酵素及び酵素を菌体外
に生産する微生物を担体結合法、架橋法及び包埋
法などの公知の方法で固定化したいわゆる固定化
酵素や固定化微生物を使用しても優れた効果が得
られる。本発明に係る方法は、処理対象トリグリ
セライドに対して酵素反応という極めて選択性の
高い反応を起すものであり、しかも反応そのもの
が温和であるので、処理された製紙原料に変質が
なく、既存の操業に対しても不都合な影響を与え
ることがない。
なお、本発明の方法においては、酵素に対して
アニオン、ノニオン及びカチオン系の界面活性剤
を併用してもよい。
(作 用)
ピツチトラブルの原因となるピツチ堆積のメカ
ニズムについては、パルプ繊維、ピツチ、金属イ
オン、填料等が混在する複雑な系であり、ピツチ
濃度、パルプ濃度、PH、温度、金属イオン濃度及
び種類等の因子が関連するとされているが、未だ
完全に明らかにはなつていない。
一般に固体表面への吸着現象は、固体表面に吸
着物を固定させるフアンデルワールス力が働くこ
とに起因する。両者の間の相互作用には多くの型
があるが、疎水結合または双極子同志の相互作用
などが重要である。また、疎水性あるいは非極性
の分子あるいは分子の部分は、疎水性あるいは非
極性の表面に吸引され易く、逆に親水性あるいは
極性分子は親水性あるいは極性表面に吸引され易
い。従つて、パルプ化工程や製紙工程におけるピ
ツチ堆積メカニズムにおいて、トリグリセライド
の果たす役割は次のように考えられる。タンクや
パイプ等の金属表面、製紙工程プレス部センター
ロールなどの疎水性あるいは非極性表面に、コロ
イダルピツチ中の非極性成分であるトリグリセラ
イドがフアンデルワールス力により付着し、この
部分が核となり、ピツチ成分中の疎水性あるいは
非極性の分子あるいは分子の部分が次々と付着し
てピツチの堆積物となる。
本発明のピツチ堆積防止の機構としては、機械
パルプ表面や循環白水中のピツチやコロイダルピ
ツチ中の疎水性、非極性表面に付着性の高い非極
性の脂肪酸トリグリセライドに対して、脂肪酸グ
リセライド分解酵素が作用し、水溶性のグリセロ
ールと極性基を有する脂肪酸とに加水分解するこ
とにより、疎水性の金属性パイプやタンク壁等へ
の堆積を阻害するものと考えられる。従つて、堆
積の最初の段階で付着が阻害されることになるの
で、ピツチ堆積の成長が進まず、ピツチトラブル
が防止される。
(発明の効果)
本発明によれば、機械パルプ製造工程又は機械
パルプを使用する製紙工程で、ピツチ成分の堆積
を阻害し、堆積ピツチにより引き起こされる紙汚
れや紙切れ等のピツチトラブルを防止することが
できる。しかも、本発明の方法は製品の品質や実
操業に悪影響を及ぼすこともなく、処理方法も簡
単で、特別の装置・設備も必要でなく、既存のパ
ルプ化工程及び製紙工程にそのまま適用できるも
のである。
(実施例)
以下に、実施例に従つて本発明を説明する。
尚、各実施例に於いて酵素処理を施さない場合を
ブランクとして示した。
実施例 1
伐採直後のアカマツ材チツプをソツクスレー抽
出器で、メタノールにより抽出して得た抽出物10
gをイソプロパノール100ml、アセトン60ml及び
水5mlの混合液に溶解させた。このピツチ溶解液
10mlを水1の入つたビーカーに添加し、激しく
攪拌して懸濁・分散させた。得られたメタノール
抽出ピツチは対乾燥チツプ重量4.7%の収率で得
られ、このピツチのトリグリセライド含有率は
37.8%であつた。
次に、調製されたピツチ分散液を塩酸及び水酸
化ナトリウムでPH7に調整し、表1に示すように
各種微生物が生産する脂肪酸グリセライド分解酵
素を各種濃度で加えて各種温度で4時間静かに攪
拌し反応処理した。
ピツチの付着量を測定するために、TAPP1
RC−324に従つて、上記の反応処理液に流酸バン
ドと塩酸を加えてPH4に調整し、約横22cm、縦7
cmのポリエチレン板を丸めて円筒状として水面か
ら2.5cm出るようにセツトし、バイブロミキサー
(米ヘイドン社製リニテーター)で30分攪拌した。
その後、ポリエチレン板を引き出し、乾燥して付
着ピツチ量を求め、ブランクに対する百分率と共
に表1に示した。
(Industrial Application Field) The present invention is based on groundwood pulp (hereinafter referred to as GP).
The present invention relates to a method for preventing pitch troubles that occur in the manufacturing process of mechanical pulp such as (abbreviated) or in the papermaking process that uses mechanical pulp. (Prior art) Mechanical pulp such as GP is made into pulp by a simple mechanical process of grinding logs or chips with a grinder or refiner.
Although it is inferior in strength to chemical pulp that uses chemicals such as alkali, it has the advantages of high yield, low cost, and high opacity. However, on the other hand, since mechanical grinding is used as a means of pulping, the wood components remain in the pulp almost unchanged. In general, wood contains 1 to 1 to 100% of pituti component, which is an organic solvent extract, in addition to the three main components of setrose, hemicellulose, and lignin.
Contains about 10%. Pitch components vary quantitatively and qualitatively depending on the tree species, but softwood, which is the main raw material for mechanical pulp, is known to contain large amounts of pitch components such as fatty acids, resin acids, and fatty acid glycerides. During pulping, some of these pitch components separate from the pulp and become floating, or become attached to or coated on the fiber surface, and are released from the fixed state before pulping. . Pituchi is detached and floating in white water.
It is a fine particle of about 0.2 to 2 microns and is called colloidal pitch. In general, paper is produced by pulp produced in various pulping processes, passed through a sorting process, mixed with papermaking materials, and then sent to a papermaking process to become a product. During this series of processes, free floating pitches or attached pitches accumulate on the pulp, tank, wire section, roll section, etc., causing paper stains and paper breaks, resulting in so-called pitch trouble. If it is mixed with other substances, pitch trouble is likely to occur frequently. One of the typical methods that has traditionally been used to prevent pitch trouble is a process called seasoning, in which logs are felled, piled up outdoors, and left to wither over a long period of time. As another method, for example,
As described in Publication No. 22606, a method of adding polyoxyethylene alkyl ether or alkyl phenyl derivatives having various addition mole numbers or surfactants containing these as main components during pulping and paper making processes. It has been known. (Problems to be Solved by the Invention) According to the above seasoning method, the pitch component in the wood changes and decreases mainly due to air oxidation, but seasoning requires a vast area and 3 to 6 months, depending on the case. has the problem that it takes longer than that, and it is currently difficult to prevent pitch trouble by seasoning alone. On the other hand, the method of adding a surfactant is said to be effective in dispersing fine particle pitches and preventing their accumulation, but it has not been used as a fundamental method for preventing pitch troubles. The present invention aims to provide a method for preventing pitch trouble, which is still a major problem in the manufacturing process of mechanical pulp or the papermaking process using mechanical pulp. (Means for Solving the Problems) In order to find an effective means for preventing pitch trouble, the present inventors first used a pitch component extracted from Japanese red pine wood, which is a typical raw wood for mechanical pulp, and
As a result of a detailed search for the pituti components deposited in the process of manufacturing GP using red pine logs or in the paper making process using red pine GP, the main components of the deposited pitch were found to be components derived from the wood, especially triglycerides, fatty acids, and resin acids. It has become clear that there are a lot of metal salts of these, and it has also become clear that the deposited pit always contains a large amount of triglycerides. From these results, triglycerides are presumed to be one of the main causative substances of piti trouble. The present inventors have tried various chemical and biochemical methods from the viewpoint that it is effective to decompose and remove triglycerides in some way to prevent pit trouble. The present invention was completed based on the discovery that the use of a fatty acid glyceride hydrolase is optimal for decomposing triglycerides and preventing the accumulation of pits without adversely affecting the quality of pulp and paper and operating conditions. did. That is, the method for preventing pitch trouble according to the present invention is to treat papermaking raw materials and/or white water with a fatty acid glyceride hydrolyzing enzyme in a mechanical pulp manufacturing process and/or a papermaking process using mechanical pulp. or removing pitch in white water, and the enzyme is Aspergillus niger, Pseudomonas fluorescens.
fluorescens), Pseudomonas flagi (Pseudo
-monas fragi), Geotrichum candidum, or Candida candidum.
Claim 2: Use of a fatty acid glyceride hydrolase produced by one or more microorganisms selected from Candida cylindracea.
This is the characteristic of The enzyme used in the present invention is an enzyme that hydrolyzes triglyceride, which is one of the main components of pitch. Any type of fatty acid glyceride hydrolase is effective, and the microorganism that produces this enzyme is Aspergillus niger.
-llus niger), Pseudomonas fluorescens, Pseudomonas fragi, Geotrichum candideum
candidum), Candida cylindracea, Mucor javanicus, Rhizopus javanicus, Rhizopus delemar, Rhizopus niveus, Rhizopus filamentous fungi Examples 1 to 5 of the above examples can be given.
The fatty acid glyceride hydrolase produced by the microorganism described in item 3 is particularly effective. In addition, the fatty acid glyceride degrading enzyme produced by the above microorganisms is more effective as it is purified.
Multiple enzymes may be used together. Furthermore, the fatty acid glyceride degrading enzyme used in the present invention exhibits sufficient effects even when used in combination with other degrading enzymes such as cellulase, hemicellulase, and protease. In order to use these enzymes in a mechanical pulp production process or a papermaking process using mechanical pulp, the enzymes are added to a papermaking raw material slurry containing mechanical pulp obtained by grinding with a grinder or refiner. weight ratio 0.1
Add ~10000ppm and let stand or stir gently.
In this case, the temperature is suitably 10 to 70°C, most preferably 35 to 55°C. If the temperature is below 10°C, the action of the enzyme will be slow and the reaction rate will be slow, and if it is above 70°C, the enzyme may be deactivated. Generally, the larger the amount of enzyme added, the faster the reaction rate will be, but in this case, 10,000 ppm based on mechanical pulp is sufficient, calculated from the amount of triglyceride as a substrate, and adding more than that is not economically viable. It will be disadvantageous. Furthermore, a pH range of 3 to 11 is appropriate; outside this range, enzyme activity is significantly inhibited. Also, large amounts of water are used in the pulping and papermaking processes, but most of it is recycled and reused.
Since these circulating white waters contain pitch components, pitch troubles can also be prevented by applying enzymes to the circulating white waters.
In this case, the fatty acid glyceride hydrolase is directly added to white water, or the enzyme and the microorganism that produces the enzyme are immobilized by known methods such as carrier binding, crosslinking, and embedding. Excellent effects can also be obtained by using enzymes or immobilized microorganisms. The method according to the present invention causes an extremely highly selective enzymatic reaction with respect to the triglyceride to be treated, and the reaction itself is mild, so there is no deterioration of the treated papermaking raw materials and existing operations can be carried out. It does not have any adverse effects on. In addition, in the method of the present invention, anionic, nonionic, and cationic surfactants may be used together with the enzyme. (Function) The mechanism of pitch accumulation, which causes pitch trouble, is a complex system in which pulp fibers, pitch, metal ions, fillers, etc. coexist. It is thought that factors such as type are related, but it is not completely clear yet. In general, the phenomenon of adsorption onto a solid surface is caused by the Van der Waals force that fixes the adsorbate to the solid surface. There are many types of interactions between the two, but important ones include hydrophobic bonds and dipole-dipole interactions. Additionally, hydrophobic or nonpolar molecules or portions of molecules tend to be attracted to hydrophobic or nonpolar surfaces, and conversely, hydrophilic or polar molecules tend to be attracted to hydrophilic or polar surfaces. Therefore, the role played by triglycerides in the pitch accumulation mechanism in the pulping process and papermaking process is considered to be as follows. Triglyceride, which is a non-polar component in colloidal pitch, adheres to metal surfaces such as tanks and pipes, and hydrophobic or non-polar surfaces such as center rolls in paper manufacturing presses due to van der Waals forces, and this part becomes the nucleus, forming a pitch. Hydrophobic or non-polar molecules or portions of molecules in the components adhere one after another to form a pitch deposit. The mechanism for preventing pitch deposits of the present invention is that a fatty acid glyceride-degrading enzyme is used to treat non-polar fatty acid triglycerides that are highly adhesive to hydrophobic and non-polar surfaces in mechanical pulp surfaces, pitch in circulating white water, and colloidal pits. It is thought that this action inhibits deposition on hydrophobic metal pipes, tank walls, etc. by hydrolyzing it into water-soluble glycerol and fatty acids having polar groups. Therefore, since adhesion is inhibited at the initial stage of deposition, the growth of pitch deposits is inhibited and pitch troubles are prevented. (Effects of the Invention) According to the present invention, it is possible to inhibit the accumulation of pitch components in a mechanical pulp manufacturing process or a paper manufacturing process using mechanical pulp, and to prevent pitch troubles such as paper stains and paper breaks caused by accumulated pitches. I can do it. Furthermore, the method of the present invention does not have any adverse effect on product quality or actual operations, is simple, does not require any special equipment or equipment, and can be applied directly to existing pulping and papermaking processes. It is. (Example) The present invention will be described below according to Examples.
In addition, in each Example, the case where enzyme treatment was not performed was shown as a blank. Example 1 Extract 10 obtained by extracting red pine wood chips immediately after felling with methanol using a Soxhlet extractor
g was dissolved in a mixture of 100 ml of isopropanol, 60 ml of acetone and 5 ml of water. This pitch solution
10ml was added to a beaker containing 1 part of water and stirred vigorously to suspend and disperse. The resulting methanol-extracted pitch was obtained at a yield of 4.7% based on the dry chip weight, and the triglyceride content of this pitch was
It was 37.8%. Next, the prepared pitch dispersion was adjusted to pH 7 with hydrochloric acid and sodium hydroxide, and fatty acid glyceride degrading enzymes produced by various microorganisms were added at various concentrations as shown in Table 1, and the mixture was gently stirred at various temperatures for 4 hours. and reaction treatment. To measure the adhesion amount of pitch, TAPP1
According to RC-324, add hydrochloric acid band and hydrochloric acid to the above reaction treatment solution to adjust the pH to 4, and make a
A cylindrical polyethylene plate of 1.5 cm was rolled into a cylindrical shape, set so that 2.5 cm protruded from the water surface, and stirred for 30 minutes using a vibromixer (Linitator, manufactured by Haydon, USA).
Thereafter, the polyethylene plate was pulled out, dried, and the amount of adhered pitch was determined, which is shown in Table 1 along with the percentage relative to the blank.
【表】
実施例 2
実施例1で調製されたピツチ分散液を用いて、
この分散液を塩酸及び水酸化ナトウムでPH7に調
整し、脂肪酸グリセライド分解酵素を対ピツチ
500ppm加えて、液温を40℃に保持したまま静か
に攪拌した。所定時間経過後実施例1と同様にし
て付着ピツチ量を求め表2に示した。[Table] Example 2 Using the pitch dispersion prepared in Example 1,
This dispersion was adjusted to pH 7 with hydrochloric acid and sodium hydroxide, and a fatty acid glyceride degrading enzyme was added to the solution.
500 ppm was added, and the solution was stirred gently while maintaining the temperature at 40°C. After a predetermined period of time had elapsed, the amount of adhesion pitches was determined in the same manner as in Example 1 and is shown in Table 2.
【表】
リクム・カンデイデウム
が生産。
実施例 3
アカマツ材から製造されたカナダ標準フリーネ
ス(CSF)63mlGP10g含むスラリー1を試料
として、実施例1に準じて酵素を各種濃度で加え
て各種PH条件下で処理した後、実施例1と同様に
してポリエチレン板へのピツチ付着量を測定し、
表3に示した。[Table] Produced by Licum Candeideum.
Example 3 Slurry 1 containing 63ml GP10g of Canadian Standard Freeness (CSF) manufactured from red pine wood was used as a sample, and enzymes were added at various concentrations according to Example 1 and treated under various PH conditions. Measure the amount of pitch adhered to the polyethylene plate using
It is shown in Table 3.
【表】
実施例 4
実施例3と同じ試料料を用いて、実施例1に準
じて対パルプ50ppmの酵素を加えて、各種温度、
各種処理時間のピツチ付着量を測定し表4に示し
た。[Table] Example 4 Using the same sample material as in Example 3, 50 ppm of enzyme was added to the pulp according to Example 1, and the mixture was heated at various temperatures.
The amount of pitch adhesion was measured for various treatment times and is shown in Table 4.
【表】
実施例 5
新聞古紙パルプ(CSF 105ml)20、GP(CSF
63ml)25、サーモメカニカルパルプ(CSF 107
ml)25及びクラフトパルプ30の割合で混合された
1%パルプスラリー1を試料として、実施例1
に準じて対パルプ50ppmの酵素を加えて温度40℃
で4時間の酵素処理を行い、引続きポリエチレン
板をセツトしバイブロミキサーで120分間攪拌し
た後ピツチ付着量を測定し、結果を表5に示し
た。[Table] Example 5 Newspaper pulp (CSF 105ml) 20, GP (CSF
63ml) 25, Thermomechanical Pulp (CSF 107
Example 1 Using 1% pulp slurry 1 mixed at a ratio of 25 ml) and 30 kraft pulp as a sample,
Add 50ppm of enzyme to the pulp according to the temperature 40℃
After enzymatic treatment for 4 hours, a polyethylene plate was set and stirred for 120 minutes using a vibromixer, and the amount of pitch adhered was measured. The results are shown in Table 5.
【表】
実施例 6
アカマツGP製造の磨砕工程後の洗浄工程でパ
ルプをフイルターかけた際に得られる白水3を
試料として、実施例1に準じて、対白水0.5ppm
濃度の酵素を加えて温度40℃で2時間の酵素処理
を行い、バイブロミキサーで120分間攪拌した後、
ポリエチレン板へのピツチ付着量を測定し、表6
に示した。[Table] Example 6 Using white water 3 obtained when pulp is filtered in the washing process after the grinding process of Akamatsu GP production as a sample, the white water 0.5 ppm was prepared according to Example 1.
After adding a concentrated amount of enzyme and performing enzyme treatment at a temperature of 40°C for 2 hours, stirring with a vibromixer for 120 minutes,
The amount of pitch adhered to the polyethylene plate was measured and shown in Table 6.
It was shown to.
【表】
実施例 7
抄幅5080mm、抄紙速度830m/分のベルベフオ
ーマー多筒式抄紙機において、原料パルプ配合を
GP:新聞DIP:NKP:TMP=30:45:10:15
として、坪量約46g/m2の新聞用紙を抄紙した。
上記原料のうちGPは、アカマツから製造された
ものであり、ポストリフアイニングによりフリー
ネス60〜70に整えられ、完成パルプとして一時ス
トツクされた後、必要に応じて他の原料と混合さ
れ、再度ストツクされて抄紙工程に送られる。
ポストリフアイナー通過後、各チエスト・タン
クを通つて抄紙工程に到達するまで約90分程度の
保持時間を有するので、酵素の添加は、ポストリ
フアイナー前にGP濃度3.8%のスラリーに対し、
リパーゼOFを3ppm濃度で行つた。2週間に渡つ
て連続添加を行い、抄紙機ワイヤー及びプレス部
に付着たピツチ量と、センターロールに付着した
ピツチの掻き取り作業の頻度を調べた。こ抄紙機
の操業生産高は日産約270トンであつた。なお、
上記のピツチ掻き取り作業は、円滑な操業のため
にセンターロールに過剰なピツチが付着するのを
防止するたに、人的にピツチを掻き取るものであ
り、付着ピツチ量が増えれば作業頻度が増す。
比較のために、酵素無添加の場合についても、
ピツチ量と作業頻度を調べた。結果は、表7の通
りである。[Table] Example 7 In a Verbeformer multi-tube paper machine with a paper making width of 5080 mm and a paper making speed of 830 m/min, the raw material pulp composition was
GP: Newspaper DIP: NKP: TMP = 30:45:10:15
Newspaper with a basis weight of approximately 46 g/m 2 was made.
Among the raw materials mentioned above, GP is manufactured from Japanese red pine, and after being adjusted to a freeness of 60 to 70 by post-refining and temporarily stocked as finished pulp, it is mixed with other raw materials as needed and then reused. It is stocked and sent to the paper making process. After passing through the post-refiner, the retention time is approximately 90 minutes until it passes through each CHEST tank and reaches the papermaking process.
Lipase OF was carried out at a concentration of 3 ppm. Continuous addition was carried out for two weeks, and the amount of pitches adhering to the paper machine wire and press section and the frequency of scraping off the pitches adhering to the center roll were investigated. The operating output of this paper machine was approximately 270 tons per day. In addition,
The above-mentioned pitch scraping work is performed manually to prevent excessive pitch from adhering to the center roll for smooth operation, and as the amount of adhering pitch increases, the frequency of work increases. Increase. For comparison, in the case without enzyme addition,
The amount of pitch and work frequency were investigated. The results are shown in Table 7.
【表】
実施例 8
実施例7に準じて、原料パルプ配合をGP:新
聞DIP:NKP:TMP=20:50:15:15として、
坪量34g/m2の軽量印刷紙を抄造するに際して、
リパーゼOFをGPスラリーに対して3ppm添加し
た。この場合の操業生産高は、日産約200トンで
あつた。なお、酵素無添加の場合との比較は、抄
紙機のワイヤー及びプレス部に付着したピツチ
量、並びにブレーカースタツクにピツチが付着し
たために生じた紙の剥ぎ取られ個数によつて行つ
た。結果を表8に示した。[Table] Example 8 According to Example 7, the raw material pulp composition was GP: newspaper DIP: NKP: TMP = 20:50:15:15,
When making lightweight printing paper with a basis weight of 34g/ m2 ,
Lipase OF was added at 3 ppm to the GP slurry. The operating output in this case was approximately 200 tons per day. Comparisons with the case without enzyme addition were made based on the amount of pitches adhering to the wire and press section of the paper machine, and the number of pieces of paper torn off due to pitches adhering to the breaker stack. The results are shown in Table 8.
Claims (1)
を使用する製紙工程において、製紙原料及び/又
は白水を脂肪酸グリセライド加水分解酵素で処理
して製紙原料及び/又は白水中のピツチを除去す
ることを特徴とするピツチトラブル防止法。 2 酵素として、アスペルギルス・ニガー
(Aspergillus niger),シユードモナス・フルオ
レツセンス(Pseudomonas fluorescens),シユ
ードモナス・フラジ(Pseudomonas fragi)、ゲ
オトリクム・カンデイデウム(Geotrichum
candidum),又はカンデイダ・シリンドラセア
(Candida cylindracea)から選択される1種以
上の微生物が生産する脂肪酸グリセライド加水分
解酵素を使用することを特徴とする請求項1記載
のピツチトラブル防止法。[Claims] 1. In a mechanical pulp manufacturing process and/or a paper manufacturing process using mechanical pulp, papermaking raw materials and/or white water are treated with a fatty acid glyceride hydrolase to remove pitch in the papermaking raw materials and/or white water. A method for preventing pitch trouble, which is characterized by removing it. 2 As an enzyme, Aspergillus niger, Pseudomonas fluorescens, Pseudomonas fragi, Geotrichum candidium
2. The method for preventing pitch trouble according to claim 1, characterized in that a fatty acid glyceride hydrolase produced by one or more microorganisms selected from Candidum cylindracea or Candida cylindracea is used.
Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63314408A JPH02160997A (en) | 1988-12-13 | 1988-12-13 | Method for preventing trouble by pitch |
AU45822/89A AU622738B2 (en) | 1988-12-13 | 1989-12-01 | Method for avoiding pitch troubles |
NZ231637A NZ231637A (en) | 1988-12-13 | 1989-12-05 | Avoiding pitch troubles in pulp manufacture by addition of an acylglycerol lipase |
FI895901A FI96520C (en) | 1988-12-13 | 1989-12-11 | Procedure for the prevention of resin difficulties |
CA002005087A CA2005087C (en) | 1988-12-13 | 1989-12-11 | Method for avoiding pitch troubles |
EP89122946A EP0374700B1 (en) | 1988-12-13 | 1989-12-12 | Process for preparing mechanical pulp and for paper containing said pulp |
AT89122946T ATE102667T1 (en) | 1988-12-13 | 1989-12-12 | PROCESS FOR PRODUCTION OF MECHANICAL PULP AND PAPER CONTAINING SUCH PULP. |
ES89122946T ES2052874T3 (en) | 1988-12-13 | 1989-12-12 | PROCEDURE FOR THE MANUFACTURE OF WOODEN MECHANICAL MATTER AND / OR PAPER CONTAINING THIS LAST. |
DE89122946T DE58907179D1 (en) | 1988-12-13 | 1989-12-12 | Process for the production of mechanical wood pulp and paper containing this wood pulp. |
NO894988A NO174433C (en) | 1988-12-13 | 1989-12-12 | Process for avoiding resin problems in the production of mechanical pulp and / or in the production of paper containing such pulp |
US07/684,516 US5176796A (en) | 1988-12-13 | 1991-04-15 | Avoiding pitch troubles using acylgerol lipase |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63314408A JPH02160997A (en) | 1988-12-13 | 1988-12-13 | Method for preventing trouble by pitch |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02160997A JPH02160997A (en) | 1990-06-20 |
JPH0429794B2 true JPH0429794B2 (en) | 1992-05-19 |
Family
ID=18052986
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63314408A Granted JPH02160997A (en) | 1988-12-13 | 1988-12-13 | Method for preventing trouble by pitch |
Country Status (10)
Country | Link |
---|---|
EP (1) | EP0374700B1 (en) |
JP (1) | JPH02160997A (en) |
AT (1) | ATE102667T1 (en) |
AU (1) | AU622738B2 (en) |
CA (1) | CA2005087C (en) |
DE (1) | DE58907179D1 (en) |
ES (1) | ES2052874T3 (en) |
FI (1) | FI96520C (en) |
NO (1) | NO174433C (en) |
NZ (1) | NZ231637A (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ZA904441B (en) * | 1989-06-22 | 1991-03-27 | Int Paper Co | Enzymatic delignification of lignocellulosic material |
NZ235983A (en) * | 1989-11-08 | 1993-01-27 | Novo Nordisk As | Process for hydrolysis of resins in lignocellulosic pulp using enzymes simultaneously with peroxy bleaching; ctmp fluff-pulp and absorbent articles produced therefrom |
FI88315C (en) * | 1990-04-04 | 1993-04-26 | Enso Gutzeit Oy | FOERFARANDE FOER BLEKNING AV CELLULOSAMASSA |
GB9018426D0 (en) * | 1990-08-22 | 1990-10-03 | Sandoz Ltd | Improvements in or relating to novel compounds |
DK249990D0 (en) * | 1990-10-17 | 1990-10-17 | Novo Nordisk As | PROCEDURE FOR ENZYMATIC PULP TREATMENT |
JPH04240286A (en) * | 1991-01-25 | 1992-08-27 | Novo Nordisk As | Method for preventing pitch trouble caused by heat resisting lipase |
FI93230C (en) * | 1991-03-22 | 1995-03-10 | Genencor Int Europ | Method for reducing resin difficulties in mechanical pulp |
JP3103113B2 (en) * | 1991-04-10 | 2000-10-23 | ノボ ノルディスク アクティーゼルスカブ | Lipase-catalyzed ester hydrolysis |
US5616215A (en) * | 1991-04-19 | 1997-04-01 | Novo Nordisk A/S | Method of making paper from pulp treated with lipase and an aluminum salt |
US5667634A (en) * | 1991-05-01 | 1997-09-16 | Novo Nordisk A/S | Method for controlling pitch deposits in papermaking process using lipase and polyelectrolyte |
CA2109112C (en) * | 1991-05-01 | 2003-01-14 | Yuko Fujita | Lipase-catalyzed ester hydrolysis |
US5256252A (en) * | 1992-07-15 | 1993-10-26 | Nalco Chemical Company | Method for controlling pitch deposits using lipase and cationic polymer |
FR2727130B1 (en) * | 1994-11-21 | 1996-12-20 | Elf Aquitaine | PROCESS FOR THE ENZYMATIC PRETREATMENT OF WELLBORE |
AU731707B2 (en) | 1998-10-13 | 2001-04-05 | Mitsui Chemicals, Inc. | Binder composition and process for the production of a board using the same |
ES2588756T3 (en) | 2000-04-28 | 2016-11-04 | Novozymes A/S | Variant of lipolytic enzyme |
CA2431972C (en) | 2001-01-10 | 2012-10-23 | Novozymes A/S | Thermostable lipolytic enzyme variant |
EP1924744A2 (en) * | 2005-09-13 | 2008-05-28 | JohnsonDiversey Inc. | Processes used in the manufacture of paper products |
ES2633731T3 (en) * | 2012-06-22 | 2017-09-25 | Buckman Laboratories International, Inc | Methods of using combinations of a lipase and an oxidant for scale control in papermaking processes and products thereof |
ES2797483T3 (en) | 2013-07-19 | 2020-12-02 | Danisco Us Inc | Compositions and Methods Comprising a Lipolytic Enzyme Variant |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0280686A (en) * | 1988-07-29 | 1990-03-20 | Sannopuko Kk | Pitch attachment-preventing agent |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA758488A (en) * | 1967-05-09 | C. Jenness Lyle | Process for treating paper pulp | |
GB1189604A (en) * | 1965-07-20 | 1970-04-29 | Mo Och Domsjoe Ab | A process for Removing Resin Constituents from Wood Chips |
-
1988
- 1988-12-13 JP JP63314408A patent/JPH02160997A/en active Granted
-
1989
- 1989-12-01 AU AU45822/89A patent/AU622738B2/en not_active Expired
- 1989-12-05 NZ NZ231637A patent/NZ231637A/en unknown
- 1989-12-11 FI FI895901A patent/FI96520C/en active IP Right Grant
- 1989-12-11 CA CA002005087A patent/CA2005087C/en not_active Expired - Lifetime
- 1989-12-12 ES ES89122946T patent/ES2052874T3/en not_active Expired - Lifetime
- 1989-12-12 NO NO894988A patent/NO174433C/en not_active IP Right Cessation
- 1989-12-12 AT AT89122946T patent/ATE102667T1/en not_active IP Right Cessation
- 1989-12-12 DE DE89122946T patent/DE58907179D1/en not_active Expired - Lifetime
- 1989-12-12 EP EP89122946A patent/EP0374700B1/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0280686A (en) * | 1988-07-29 | 1990-03-20 | Sannopuko Kk | Pitch attachment-preventing agent |
Also Published As
Publication number | Publication date |
---|---|
ATE102667T1 (en) | 1994-03-15 |
ES2052874T3 (en) | 1994-07-16 |
CA2005087C (en) | 1998-12-01 |
EP0374700A2 (en) | 1990-06-27 |
NO894988L (en) | 1990-06-14 |
JPH02160997A (en) | 1990-06-20 |
NZ231637A (en) | 1991-06-25 |
EP0374700A3 (en) | 1991-11-21 |
NO174433C (en) | 1994-05-04 |
FI895901A0 (en) | 1989-12-11 |
FI96520B (en) | 1996-03-29 |
DE58907179D1 (en) | 1994-04-14 |
AU622738B2 (en) | 1992-04-16 |
NO174433B (en) | 1994-01-24 |
EP0374700B1 (en) | 1994-03-09 |
NO894988D0 (en) | 1989-12-12 |
CA2005087A1 (en) | 1990-06-13 |
AU4582289A (en) | 1990-06-21 |
FI96520C (en) | 1996-07-10 |
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