JP2009243016A - Pulp-cleaning agent and method for producing pulp - Google Patents

Pulp-cleaning agent and method for producing pulp Download PDF

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JP2009243016A
JP2009243016A JP2008094128A JP2008094128A JP2009243016A JP 2009243016 A JP2009243016 A JP 2009243016A JP 2008094128 A JP2008094128 A JP 2008094128A JP 2008094128 A JP2008094128 A JP 2008094128A JP 2009243016 A JP2009243016 A JP 2009243016A
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pulp
washing
cleaning agent
builder
aromatic ring
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JP5181783B2 (en
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Yuji Sonoda
雄二 園田
Kenji Kobata
賢二 木幡
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Kurita Water Industries Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a pulp-cleaning agent excellent in a function for removing organic matters from a pulp material, and to provide a method for producing pulp with the pulp-cleaning agent. <P>SOLUTION: The pulp-cleaning agent contains a nonionic surfactant having an aromatic ring in a hydrophobic portion. The method for producing the pulp has a digesting step of digesting the pulp material in a digesting zone 211 to obtain the pulp, a washing step of washing the pulp in a washing zone 212 or in a pulp-washing portion 30, and a bleaching step of bleaching the washed pulp in a bleaching portion, and further having an adding step of adding a pulp-washing agent containing a nonionic surfactant having an aromatic ring in a hydrophobic portion to the washing zone 212 or the pulp-washing portion 30. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、パルプを洗浄するパルプ洗浄剤及び洗浄されたパルプの製造方法に関する。   The present invention relates to a pulp cleaning agent for cleaning pulp and a method for producing the cleaned pulp.

パルプを製造する工程は、木材チップを蒸解してパルプを得る蒸解手順と、このパルプとリグニンを含む黒液とを分離し、分離されたパルプを洗浄する洗浄手順と、洗浄されたパルプを漂白する漂白手順と、を有する(例えば、特許文献1参照)。このようにして製造される漂白されたパルプは、製紙等に使用されることになる。   The pulp manufacturing process includes cooking procedures for cooking wood chips to obtain pulp, a cleaning procedure for separating the pulp and black liquor containing lignin, washing the separated pulp, and bleaching the washed pulp. Bleaching procedure (see, for example, Patent Document 1). The bleached pulp produced in this way is used for papermaking and the like.

パルプの洗浄系(酸素脱リグニン工程を含む)において、リグニン等の抽出成分を効率よくパルプから除去することは、プロセスの生産性向上に大きく寄与する。これまでは、主に洗浄機の改良によってパルプの洗浄効率の改善がなされてきたが、これには多くのコストがかかることから、設備改造を伴わない薬品による実用的な改善も試みられている。   In a pulp cleaning system (including an oxygen delignification step), efficiently removing extracted components such as lignin from pulp greatly contributes to an improvement in process productivity. Until now, the washing efficiency of pulp has been improved mainly by improving the washing machine. However, since this requires a lot of cost, practical improvements using chemicals without remodeling are also being attempted. .

例えば、パルプの洗浄効率の高める薬品としては界面活性剤が挙げられるが、その中でも、非イオン系界面活性剤が広く適用されている(例えば、特許文献2参照)。
特公昭48−39763号公報 特開2003−161491号公報
For example, as a chemical | medical agent which raises the washing | cleaning efficiency of a pulp, surfactant is mentioned, Among these, a nonionic surfactant is widely applied (for example, refer patent document 2).
Japanese Patent Publication No. 48-39963 JP 2003-161491 A

しかしながら、従来から広く適用されている非イオン系界面活性剤の洗浄力は、満足のいくものではない。   However, the detergency of nonionic surfactants that have been widely applied conventionally is not satisfactory.

そこで、本発明は、従来の非イオン系界面活性剤に比して、パルプに付着しているリグニン分解物や樹脂等の有機物(汚れ成分)を取り除く機能に優れた界面活性剤を含有するパルプ洗浄剤、及び該パルプ洗浄剤を用いたパルプ製造方法を提供することを目的とする。   Accordingly, the present invention provides a pulp containing a surfactant that has an excellent function of removing organic substances (soil components) such as lignin degradation products and resins adhering to the pulp, as compared with conventional nonionic surfactants. It is an object of the present invention to provide a cleaning agent and a pulp manufacturing method using the pulp cleaning agent.

本発明のパルプ洗浄剤は、疎水性部分に芳香族環を有する非イオン系界面活性剤を含有することを特徴とする。   The pulp cleaning agent of the present invention is characterized by containing a nonionic surfactant having an aromatic ring in a hydrophobic portion.

本発明のパルプ洗浄剤では、芳香族環は1個のベンゼン環であることが好ましい。   In the pulp cleaning agent of the present invention, the aromatic ring is preferably one benzene ring.

本発明のパルプ洗浄剤では、ビルダーを更に含有することが好ましい。   In the pulp cleaning agent of this invention, it is preferable to further contain a builder.

本発明のパルプ洗浄剤では、ビルダーはキレート性化合物又は水溶性ポリマーであることが好ましい。   In the pulp cleaning agent of the present invention, the builder is preferably a chelating compound or a water-soluble polymer.

本発明のパルプ製造方法は、蒸解部においてパルプ材料を蒸解してパルプを得る蒸解手順と、前記パルプをパルプ洗浄系において洗浄する洗浄手順と、洗浄されたパルプを漂白部において漂白する漂白手順と、を有し、前記パルプ洗浄系に、疎水性部分に芳香族環を有する非イオン系界面活性剤を含有するパルプ洗浄剤を添加する添加手順を更に有することを特徴とする。   The pulp production method of the present invention includes a cooking procedure for cooking pulp material in a cooking section to obtain pulp, a washing procedure for washing the pulp in a pulp washing system, and a bleaching procedure for bleaching the washed pulp in a bleaching section, The pulp cleaning system further includes an addition procedure for adding a pulp cleaning agent containing a nonionic surfactant having an aromatic ring in the hydrophobic portion.

本発明のパルプ製造方法では、芳香族環は1個のベンゼン環であることが好ましい。   In the pulp manufacturing method of the present invention, the aromatic ring is preferably one benzene ring.

本発明のパルプ製造方法では、パルプ洗浄剤はビルダーを更に含有することが好ましい。   In the pulp manufacturing method of the present invention, the pulp detergent preferably further contains a builder.

本発明のパルプ製造方法では、ビルダーはキレート性化合物又は水溶性ポリマーであることが好ましい。   In the pulp manufacturing method of the present invention, the builder is preferably a chelating compound or a water-soluble polymer.

本発明によれば、疎水性部分に芳香族環を有する非イオン系界面活性剤をパルプ洗浄剤に含有させたので、かかるパルプ洗浄剤の洗浄度が向上する。これは、パルプ洗浄剤に含まれる非イオン系界面活性剤の疎水性部分の構造がパルプに付着しているリグニン分解物や樹脂等の有機物(汚れ成分)の構造と近くなることで、パルプ洗浄剤と有機物との親和力が高まり、かかる有機物が効果的に可溶化されたためと推測される。   According to the present invention, since the non-ionic surfactant having an aromatic ring in the hydrophobic portion is contained in the pulp cleaning agent, the cleaning degree of the pulp cleaning agent is improved. This is because the structure of the hydrophobic part of the nonionic surfactant contained in the pulp cleaner is close to the structure of organic substances (dirt components) such as lignin degradation products and resins that are attached to the pulp. It is presumed that the affinity between the agent and the organic substance increased, and the organic substance was effectively solubilized.

以下、本発明の実施形態について説明するが、本発明はこれに特に限定されるものではない。   Hereinafter, although embodiment of this invention is described, this invention is not specifically limited to this.

[パルプ製造系・パルプ製造方法]
図1は、本発明に係る洗浄剤が適用されるパルプ製造系の一例を示すブロック図である。パルプ製造系10は、上流から順に、蒸解洗浄系20と、パルプ洗浄部30と、漂白部とを備える。
[Pulp production system and pulp production method]
FIG. 1 is a block diagram showing an example of a pulp production system to which a cleaning agent according to the present invention is applied. The pulp production system 10 includes a digestion cleaning system 20, a pulp cleaning unit 30, and a bleaching unit in order from the upstream.

蒸解洗浄系20は蒸解釜21を有し、この蒸解釜21においてパルプ材料を蒸解し、予備的に洗浄する。具体的には、蒸解釜21の蒸解ゾーン211において、パルプ材料である木材チップと、水酸化ナトリウム等を含有する溶液とを混合し加圧蒸煮することで、木材チップ中の非繊維成分を溶解し、蒸解釜21の洗浄ゾーン212において、予備的に洗浄する。洗浄ゾーン212を経て得られ、非繊維成分が溶解された黒液と、パルプとが混在するパルプスラリーは、図示しないブロータンクを経て、次のパルプ洗浄部30に移送される。本発明の蒸解部は蒸解ゾーン211で構成され、本発明のパルプ製造方法を構成する蒸解手順は、洗浄ゾーン212の上流までの作業を指す。   The digester cleaning system 20 has a digester 21 in which the pulp material is digested and preliminarily cleaned. Specifically, in the cooking zone 211 of the digester 21, the non-fiber components in the wood chips are dissolved by mixing wood chips that are pulp materials and a solution containing sodium hydroxide or the like, and steaming under pressure. Then, preliminary cleaning is performed in the cleaning zone 212 of the digester 21. The pulp slurry obtained through the washing zone 212 and mixed with the black liquor in which the non-fiber components are dissolved and the pulp is transferred to the next pulp washing unit 30 through a blow tank (not shown). The cooking section of the present invention is constituted by the cooking zone 211, and the cooking procedure constituting the pulp manufacturing method of the present invention refers to the work up to the upstream of the washing zone 212.

パルプ洗浄部30は、パルプスラリーからパルプを分離し洗浄するものである。具体的には、蒸解釜21から移送されたパルプスラリーは、ディフュージョン洗浄装置31に導入され、向流洗浄を施された後、ノッタ32に移送される。蒸解液は、ノッタ32で残留する未蒸解物が除去された後、第1前置ドラム洗浄装置33、第2前置ドラム洗浄装置34にて置換洗浄される。これにより、リグニンを含む黒液が回収される。回収された黒液から水酸化ナトリウムを分離し再利用してもよい。   The pulp cleaning unit 30 separates and cleans the pulp from the pulp slurry. Specifically, the pulp slurry transferred from the digester 21 is introduced into the diffusion cleaning device 31, subjected to countercurrent cleaning, and then transferred to the knotter 32. The cooking liquor is subjected to replacement washing in the first pre-drum washing device 33 and the second pre-drum washing device 34 after the undistilled material remaining in the knotter 32 is removed. Thereby, the black liquor containing lignin is collect | recovered. Sodium hydroxide may be separated from the recovered black liquor and reused.

続いて、黒液除去後のパルプは、スチームミキサ35で蒸気を供給されることで所定温度に加温された後、図示しない前置貯蔵槽に貯蔵される。そして、前置貯蔵槽に貯蔵されたパルプは、酸素を供給された後、酸素リアクタ36に導入され、この酸素リアクタ36にて更なる脱リグニン化が行われる。酸素リアクタ36から排出されたパルプはブロータンク37に移送され、第1後置ドラム洗浄装置38、第2後置ドラム洗浄装置39に導入される。これら第1後置ドラム洗浄装置38、第2後置ドラム洗浄装置39では、パルプが更に洗浄され、リグニン等が除去される。第2後置ドラム洗浄装置39からのパルプは、図示しない後置貯蔵槽に貯蔵された後、漂白部へと移送される。本発明のパルプ洗浄系は、洗浄ゾーン212及びパルプ洗浄部30で構成され、本発明のパルプ製造方法を構成する洗浄手順は、以上の洗浄ゾーン212から漂白部の上流までの作業を指す。   Subsequently, the pulp after the black liquor is removed is heated to a predetermined temperature by being supplied with steam by the steam mixer 35 and then stored in a front storage tank (not shown). The pulp stored in the pre-storage tank is supplied with oxygen and then introduced into the oxygen reactor 36 where further delignification is performed. The pulp discharged from the oxygen reactor 36 is transferred to a blow tank 37 and introduced into a first rear drum cleaning device 38 and a second rear drum cleaning device 39. In the first post-drum cleaning device 38 and the second post-drum cleaning device 39, the pulp is further cleaned and lignin and the like are removed. Pulp from the second post-drum cleaning device 39 is stored in a post-storage tank (not shown) and then transferred to the bleaching section. The pulp washing system of the present invention is constituted by the washing zone 212 and the pulp washing unit 30, and the washing procedure constituting the pulp manufacturing method of the present invention refers to the operation from the washing zone 212 to the upstream of the bleaching unit.

続いて漂白部においてパルプが漂白されることで、製紙に好ましく使用される良質のパルプが製造される。漂白部及び使用される漂白剤は、従来周知のものであってよい。以上は、本発明のパルプ製造方法を構成する漂白手順の一例である。   Subsequently, the pulp is bleached in the bleaching section to produce a high-quality pulp that is preferably used for papermaking. A bleaching part and the bleaching agent used may be a conventionally well-known thing. The above is an example of the bleaching procedure which comprises the pulp manufacturing method of this invention.

前述したように、酸素脱リグニン工程を含むパルプの洗浄系(洗浄ゾーン212及びパルプ洗浄部30)において、リグニン等の抽出成分を効率よくパルプから除去することは、プロセスの生産性向上に大きく寄与する。   As described above, in the pulp washing system including the oxygen delignification step (washing zone 212 and pulp washing unit 30), efficiently removing extracted components such as lignin from the pulp greatly contributes to the improvement of process productivity. To do.

本発明のパルプ製造方法は、蒸解手順、洗浄手順、及び漂白手順に加え、洗浄ゾーン212及びパルプ洗浄部30に本発明のパルプ洗浄剤を添加する添加手順を更に有することで、プロセスの生産性向上を図る。本発明で使用されるパルプ洗浄剤については、以下に説明する。   The pulp manufacturing method of the present invention further includes an addition procedure for adding the pulp cleaning agent of the present invention to the washing zone 212 and the pulp washing unit 30 in addition to the cooking procedure, the washing procedure, and the bleaching procedure, thereby improving the productivity of the process. Improve. The pulp cleaner used in the present invention will be described below.

[パルプ洗浄剤]
本発明のパルプ洗浄剤は、疎水性部分に芳香族環を有する非イオン系界面活性剤を含有する。本発明のパルプ洗浄剤では、非イオン系界面活性剤の含有量は特に限定されない。例えば、パルプに付着しているリグニン分解物や樹脂等の有機物(汚れ成分)の除去に影響を与える程度の量であればよく、後述するビルダーの種類や量によっても変動する場合があり、また、パルプの種類、付着している有機物の程度、洗浄条件等に応じて適宜設定されてもよい。
[Pulp cleaning agent]
The pulp cleaner of the present invention contains a nonionic surfactant having an aromatic ring in the hydrophobic portion. In the pulp cleaning agent of the present invention, the content of the nonionic surfactant is not particularly limited. For example, it may be an amount that affects the removal of organic substances (dirt components) such as lignin degradation products and resins adhering to the pulp, and may vary depending on the type and amount of the builder described later. Depending on the type of the pulp, the degree of the organic matter adhering thereto, the washing conditions, etc., it may be set appropriately.

本発明に用いられる非イオン系界面活性剤は、疎水性部分に芳香族環を有していれば、特に限定されるものではない。本発明では、芳香族環はベンゼン環であっても、ナフタレン環であってもよいが、ベンゼン環がより好ましい。なお、芳香族環の数は特に限定されないが、1個のベンゼン環を有しているものが、パルプに付着しているリグニン分解物や樹脂等の有機物(汚れ成分)を取り除く洗浄力に優れているという点において好ましい。本発明に用いられる非イオン系界面活性剤では、芳香族環をその主鎖に有していても、側鎖に有していてもよいが、主鎖がより好ましい。本発明に用いられる非イオン系界面活性剤としては、例えば、ポリオキシアルキレンアリールエーテル又はポリオキシアルキレンスチレン化アリールエーテルが挙げられる。ここで、アルキレンの炭素数は1〜3が好ましく、2がより好ましい。また、アリールとしては、フェニル基、ナフチル基等が挙げられるが、フェニル基がより好ましい。置換基の有無は特に問わない。具体的には、ポリオキシエチレンフェニルエーテル、ポリオキシエチレンスチレン化フェニルエーテル、ポリオキシエチレンナフチルエーテル等が挙げられる。なお、有機物を可溶化してパルプから取り除くためには、かかる有機物と非イオン系界面活性剤の疎水性部分との構造が近く、親和力が高い方が好ましいと推測される。   The nonionic surfactant used in the present invention is not particularly limited as long as it has an aromatic ring in the hydrophobic portion. In the present invention, the aromatic ring may be a benzene ring or a naphthalene ring, but a benzene ring is more preferable. The number of aromatic rings is not particularly limited, but those having one benzene ring are excellent in detergency to remove organic substances (dirt components) such as lignin degradation products and resins adhering to the pulp. It is preferable in that it is. The nonionic surfactant used in the present invention may have an aromatic ring in its main chain or a side chain, but the main chain is more preferable. Examples of the nonionic surfactant used in the present invention include polyoxyalkylene aryl ether and polyoxyalkylene styrenated aryl ether. Here, the number of carbon atoms of the alkylene is preferably 1 to 3, and more preferably 2. Examples of aryl include a phenyl group and a naphthyl group, and a phenyl group is more preferable. The presence or absence of a substituent is not particularly limited. Specific examples include polyoxyethylene phenyl ether, polyoxyethylene styrenated phenyl ether, polyoxyethylene naphthyl ether, and the like. In order to solubilize and remove organic matter from the pulp, it is presumed that the structure of the organic matter and the hydrophobic portion of the nonionic surfactant are close to each other and preferably have a high affinity.

本発明のパルプ洗浄剤は、ビルダーを更に含有することが好ましい。ビルダーとは、界面活性剤の洗浄効果を上げる無機配合剤(洗浄助剤)であって、一般にビルダーと称されるものに限定されず、ビルダー機能を有する化合物であってもよい。好ましくは、金属を錯体化する作用を有するキレート性化合物、水溶性ポリマー等が挙げられる。本発明のパルプ洗浄剤では、ビルダーの含有量は特に限定されない。例えば、洗浄ゾーン212及びパルプ洗浄部30内を流通する液中に多量に含まれるカルシウムによって、リグニン抽出が阻害されない程度であればよく、状況に応じて適宜設定されてよい。   The pulp cleaner of the present invention preferably further contains a builder. A builder is an inorganic compounding agent (cleaning aid) that increases the cleaning effect of a surfactant, and is not limited to what is generally referred to as a builder, and may be a compound having a builder function. Preferable examples include a chelating compound having a function of complexing a metal, a water-soluble polymer, and the like. In the pulp cleaning agent of the present invention, the builder content is not particularly limited. For example, it is sufficient that the lignin extraction is not hindered by calcium contained in a large amount in the liquid flowing through the washing zone 212 and the pulp washing unit 30, and may be set as appropriate according to the situation.

本発明に用いられるビルダーとしては、例えば、エチレンジアミン四酢酸(EDTA)、ジエチレントリアミン五酢酸(DTPA)、ヒドロキシエチレンジアミン四酢酸(HEDTA)、エチレンジアミンコハク酸(EDDS)、トリエチレンテトラアミン六酢酸(TTHA)、ヒドロキシエタンホスホン酸(HEDP)、ニトリロトリスメチレンホスホン酸(NTMP)、ホスホノブタントリカルボン酸(PBTC)、ジエチレントリアミンペンタメチレンホスホン酸(DTPMPA)等のキレート性化合物、及びポリアクリル酸(AA)、アクリル酸と2−ヒドロキシ−3−アリルオキシ−1−プロパンスルホン酸との共重合体(AA/HAPS)、アクリル酸とアクリル酸メチルとの共重合体(AA/MA)、アクリル酸メチルとイソブチレンとの共重合体(MA/IB)、及びアクリル酸メチルとアクリル酸と酢酸ビニルとの共重合体等の水溶性ポリマーが挙げられる。これらは、1種単独で使用されてもよく、複数種で併用されてもよい。   Examples of the builder used in the present invention include ethylenediaminetetraacetic acid (EDTA), diethylenetriaminepentaacetic acid (DTPA), hydroxyethylenediaminetetraacetic acid (HEDTA), ethylenediaminesuccinic acid (EDDS), triethylenetetraaminehexaacetic acid (TTHA), Chelating compounds such as hydroxyethanephosphonic acid (HEDP), nitrilotrismethylenephosphonic acid (NTMP), phosphonobutanetricarboxylic acid (PBTC), diethylenetriaminepentamethylenephosphonic acid (DTPMPA), and polyacrylic acid (AA), acrylic acid And 2-hydroxy-3-allyloxy-1-propanesulfonic acid (AA / HAPS), acrylic acid and methyl acrylate copolymer (AA / MA), methyl acrylate and iso Copolymers of styrene (MA / IB), and include water-soluble polymers such as a copolymer of methyl acrylate and of acrylic acid and vinyl acetate. These may be used individually by 1 type and may be used together by multiple types.

本発明のパルプ製造方法では、パルプ洗浄剤は、洗浄ゾーン212及びパルプ洗浄部30の一箇所又は複数箇所に添加されてもよく、非イオン系界面活性剤及びビルダー等の成分ごとに同一箇所又は別箇所に添加されてもよい。   In the pulp manufacturing method of the present invention, the pulp cleaning agent may be added to one or a plurality of locations in the cleaning zone 212 and the pulp cleaning section 30, or the same location or every component such as a nonionic surfactant and a builder. You may add to another location.

[洗浄剤の評価1]
<対照区>
洗浄装置38の出口のパルプシート(パルプ濃度:約14質量%〜約30質量%)を10g採取した。これを0.002質量%のカルシウム水溶液(20mgのカルシウム(和光純薬社製)を1Lの蒸留水に溶解したもの:実際の洗浄水レベル)300mlに分散させ、60℃の水浴中で5分間攪拌した(以下、この溶液を溶液1とする)。次いで、溶液1を5分間静置後、その上澄みを一部採取し、0.45μmのフィルターで濾過した濾液をブランク1とした。一方、溶液1を60℃に保温した状態で更に15分間攪拌し、次いで、5分間静置後、その上澄みを一部採取し、0.45μmのフィルターで濾過した濾液をブランク2とした。そして、ブランク2のTOC(全有機体炭素)からブランク1のTOCを差し引いたものを対照区におけるTOC量の増加とした。なお、TOCは、TOC計(全有機体炭素計:島津製作所社製)を用いて測定した。
[Evaluation of cleaning agent 1]
<Control Zone>
10 g of a pulp sheet (pulp concentration: about 14 mass% to about 30 mass%) at the outlet of the cleaning device 38 was collected. This was dispersed in 300 ml of a 0.002 mass% calcium aqueous solution (20 mg of calcium (manufactured by Wako Pure Chemical Industries, Ltd. dissolved in 1 L of distilled water: actual washing water level)) in a water bath at 60 ° C. for 5 minutes. The solution was stirred (hereinafter, this solution is referred to as Solution 1). Next, after leaving the solution 1 to stand for 5 minutes, a part of the supernatant was collected, and the filtrate filtered through a 0.45 μm filter was used as a blank 1. On the other hand, the solution 1 was further stirred for 15 minutes while being kept at 60 ° C., and then allowed to stand for 5 minutes, and then a part of the supernatant was collected, and the filtrate filtered through a 0.45 μm filter was designated as blank 2. And what subtracted TOC of blank 1 from TOC (total organic carbon) of blank 2 was made into the increase in the amount of TOC in a control section. The TOC was measured using a TOC meter (total organic carbon meter: manufactured by Shimadzu Corporation).

<実施例1>
上記方法により調製した溶液1に、本発明の疎水性部分に芳香族環を有する非イオン系界面活性剤を1質量%含有する洗浄剤を50mg/Lとなるように添加し、対照区と同様の操作によりTOCを測定した。
<Example 1>
To the solution 1 prepared by the above method, a detergent containing 1% by mass of a nonionic surfactant having an aromatic ring in the hydrophobic portion of the present invention was added to 50 mg / L, and the same as in the control group The TOC was measured by the operation.

<実施例2〜7>
上記方法により調製した溶液1に、本発明の疎水性部分に芳香族環を有する非イオン系界面活性剤とビルダーとが表1の規定濃度になるように調製した洗浄剤を添加し、対照区と同様の操作によりTOCを測定した。
<Examples 2 to 7>
To the solution 1 prepared by the above method, a detergent prepared so that the nonionic surfactant having an aromatic ring in the hydrophobic portion of the present invention and the builder have the prescribed concentrations shown in Table 1 was added, and the control group TOC was measured by the same operation.

<比較例1〜3>
上記方法により調製した溶液1に、疎水性部分に芳香族環を有さない非イオン系界面活性剤とビルダーとが表1の規定濃度になるように調製した洗浄剤を添加し、対照区と同様の操作によりTOCを測定した。
<Comparative Examples 1-3>
To the solution 1 prepared by the above method, a nonionic surfactant that does not have an aromatic ring in the hydrophobic part and a cleaning agent prepared so that the builder has a specified concentration shown in Table 1 are added, TOC was measured by the same operation.

<比較例4及び5>
上記方法により調製した溶液1に、ビルダーが表1の規定濃度になるように調製した洗浄剤を添加し、対照区と同様の操作によりTOCを測定した。
<Comparative Examples 4 and 5>
To the solution 1 prepared by the above method, a cleaning agent prepared so that the builder had the specified concentration shown in Table 1 was added, and the TOC was measured by the same operation as in the control group.

これらの結果を表1に示す。なお、添加したパルプ洗浄剤の組成及び規定濃度は、表1に示した通りである。TOCは比較のため、あらかじめ洗浄剤の値を測定した上で補正を行った。   These results are shown in Table 1. The composition and specified concentration of the added pulp cleaning agent are as shown in Table 1. For comparison, the TOC was corrected after measuring the value of the cleaning agent in advance.

Figure 2009243016
Figure 2009243016

本発明のパルプ洗浄剤(実施例1〜7)は、いずれも良好なTOC増加率を示した。また、本発明のパルプ洗浄剤(実施例2、4及び6)は、芳香族環を有しない非イオン系界面活性剤を含有するパルプ洗浄剤(比較例1、2及び3)よりもTOC増加率が高かった。このことから、本発明のパルプ洗浄剤は、芳香族環を有しない非イオン系界面活性剤を含有するパルプ洗浄剤に比して、優れた洗浄効果を発揮することがわかった。
ビルダーを含有する本発明のパルプ洗浄剤(実施例2〜7)は、ビルダーを含有しない本発明のパルプ洗浄剤に比して、TOCの増加率が非常に高かった。このことから、ビルダーを更に含有することで、更に洗浄力が高まることがわかった。
また、ベンゼン環を有するPOEフェニルエーテルを含有する本発明のパルプ洗浄剤(実施例2及び3)は、ナフタレン環を有するPOEナフチルエーテルを含有する本発明のパルプ洗浄剤(実施例6及び7)に比して、TOC増加率が高かった。このことから、ナフタレン環よりもベンゼン環を有する非イオン系界面活性剤を含有する方が、パルプ洗浄効果が高いことがわかった。
更に、2個のベンゼン環を有するPOEスチレン化フェニルエーテルを含有する本発明のパルプ洗浄剤(実施例4及び5)は、1個のベンゼン環を有するPOEフェニルエーテルを含有する本発明のパルプ洗浄剤(実施例2及び3)よりも、TOC増加率が低かった。このことから、ベンゼン環を2個有するよりも1個有する非イオン系界面活性剤を含有する方が、パルプ洗浄効果が高いことがわかった。
The pulp cleaning agents of the present invention (Examples 1 to 7) all showed a good TOC increase rate. Moreover, the pulp cleaning agent of the present invention (Examples 2, 4 and 6) has a higher TOC than the pulp cleaning agent (Comparative Examples 1, 2 and 3) containing a nonionic surfactant having no aromatic ring. The rate was high. From this, it was found that the pulp cleaning agent of the present invention exhibits an excellent cleaning effect as compared with a pulp cleaning agent containing a nonionic surfactant having no aromatic ring.
The pulp detergent of the present invention containing the builder (Examples 2 to 7) had a very high TOC increase rate compared to the pulp detergent of the present invention not containing the builder. From this, it was found that the detergency was further increased by further containing a builder.
In addition, the pulp cleaner of the present invention containing POE phenyl ether having a benzene ring (Examples 2 and 3) is the pulp cleaner of the present invention containing POE naphthyl ether having a naphthalene ring (Examples 6 and 7). The TOC increase rate was higher than that. From this, it was found that the pulp cleaning effect was higher when a nonionic surfactant having a benzene ring was contained than a naphthalene ring.
Further, the pulp cleaning agent of the present invention containing POE styrenated phenyl ether having two benzene rings (Examples 4 and 5) is a pulp cleaning of the present invention containing POE phenyl ether having one benzene ring. The TOC increase rate was lower than the agent (Examples 2 and 3). From this, it was found that the pulp cleaning effect was higher when a nonionic surfactant having one benzene ring was contained rather than having two benzene rings.

[洗浄剤の評価2]
<実施例8及び9>
上記洗浄剤の評価方法1により調製した溶液1に、本発明の疎水性部分に芳香族環を有する非イオン系界面活性剤とビルダーとが表2の規定濃度になるように調製した洗浄剤を添加し、評価方法1の対照区と同様の操作によりTOCを測定した。
[Evaluation of cleaning agent 2]
<Examples 8 and 9>
To the solution 1 prepared by the evaluation method 1 of the above-mentioned cleaning agent, the cleaning agent prepared so that the nonionic surfactant having an aromatic ring in the hydrophobic portion and the builder in the hydrophobic part of the present invention have the prescribed concentrations shown in Table 2. The TOC was measured by the same operation as in the control group of Evaluation Method 1.

<比較例6〜11>
上記洗浄剤の評価方法1により調製した溶液1に、疎水性部分に芳香族環を有さない非イオン系界面活性剤とビルダーとが表2の規定濃度になるように調製した洗浄剤を添加し、評価方法1の対照区と同様の操作によりTOCを測定した。
<Comparative Examples 6-11>
To the solution 1 prepared by the above-described cleaning agent evaluation method 1, the cleaning agent prepared so that the nonionic surfactant having no aromatic ring in the hydrophobic portion and the builder have the prescribed concentrations shown in Table 2 is added. Then, the TOC was measured by the same operation as that in the control section of the evaluation method 1.

これらの結果を表2に示す。なお、添加したパルプ洗浄剤の組成及び規定濃度は、表2に示した通りである。TOCは比較のため、あらかじめ洗浄剤の値を測定した上で補正を行った。   These results are shown in Table 2. In addition, the composition and specified concentration of the added pulp cleaning agent are as shown in Table 2. For comparison, the TOC was corrected after measuring the value of the cleaning agent in advance.

Figure 2009243016
Figure 2009243016

ビルダーを含有する本発明のパルプ洗浄剤(実施例8及び9)は、同様にビルダーを含有する、芳香族環を有しない非イオン系界面活性剤含有パルプ洗浄剤(比較例6〜11)に比して、TOCの増加率が高かった。このことから、パルプ洗浄剤は芳香族環を有する非イオン系界面活性剤を含有することで、その洗浄力が向上すると考えられる。   The pulp cleaning agent of the present invention containing builder (Examples 8 and 9) is a nonionic surfactant-containing pulp cleaning agent (Comparative Examples 6 to 11) that similarly contains a builder and does not have an aromatic ring. In comparison, the rate of increase in TOC was high. From this, it is considered that the pulp cleaning agent improves the detergency by containing a nonionic surfactant having an aromatic ring.

本発明に係る洗浄剤が適用されるパルプ製造系の一例を示すブロック図である。It is a block diagram which shows an example of the pulp manufacturing system with which the cleaning agent which concerns on this invention is applied.

符号の説明Explanation of symbols

10 パルプ製造系
20 蒸解洗浄系
211 蒸解ゾーン(蒸解部)
212 洗浄ゾーン(パルプ洗浄系)
30 パルプ洗浄部(パルプ洗浄系)
10 Pulp production system 20 Cooking cleaning system 211 Cooking zone (cooking part)
212 Washing zone (pulp washing system)
30 Pulp washing section (pulp washing system)

Claims (8)

疎水性部分に芳香族環を有する非イオン系界面活性剤を含有するパルプ洗浄剤。   A pulp cleaner comprising a nonionic surfactant having an aromatic ring in a hydrophobic portion. 前記芳香族環は1個のベンゼン環である請求項1記載のパルプ洗浄剤。   The pulp cleaner according to claim 1, wherein the aromatic ring is one benzene ring. ビルダーを更に含有する請求項1又は2記載のパルプ洗浄剤。   The pulp cleaning agent according to claim 1 or 2, further comprising a builder. 前記ビルダーは、キレート性化合物又は水溶性ポリマーである請求項3記載のパルプ洗浄剤。   The pulp builder according to claim 3, wherein the builder is a chelating compound or a water-soluble polymer. 蒸解部においてパルプ材料を蒸解してパルプを得る蒸解手順と、前記パルプをパルプ洗浄系において洗浄する洗浄手順と、洗浄されたパルプを漂白部において漂白する漂白手順と、を有するパルプ製造方法であって、
前記パルプ洗浄系に、疎水性部分に芳香族環を有する非イオン系界面活性剤を含有するパルプ洗浄剤を添加する添加手順を更に有するパルプ製造方法。
A pulp production method comprising: a cooking procedure for cooking pulp material in a cooking section to obtain pulp; a washing procedure for washing the pulp in a pulp washing system; and a bleaching procedure for bleaching the washed pulp in a bleaching section. And
The pulp manufacturing method which further has the addition procedure which adds the pulp cleaning agent containing the nonionic surfactant which has an aromatic ring in a hydrophobic part to the said pulp cleaning system.
前記芳香族環は1個のベンゼン環である請求項5記載のパルプ製造方法。   The pulp manufacturing method according to claim 5, wherein the aromatic ring is one benzene ring. 前記パルプ洗浄剤はビルダーを更に含有する請求項5又は6記載のパルプ製造方法。   The pulp manufacturing method according to claim 5 or 6, wherein the pulp cleaning agent further contains a builder. 前記ビルダーは、キレート性化合物又は水溶性ポリマーである請求項7記載のパルプ製造方法。   The pulp builder according to claim 7, wherein the builder is a chelating compound or a water-soluble polymer.
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JP2011201963A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Method for manufacturing hydrophilic resin, and method for manufacturing molded article of pulp fiber composite resin
JP2011201965A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Process for producing hydrophilic resin and molded article of pulp fiber composite resin
JP2011201966A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Method for manufacturing pulp fiber reinforced resin, and pulp fiber reinforced resin
JP2011201964A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Method for manufacturing hydrophilic resin, and molded article of pulp fiber composite resin
JP4799682B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Method for producing pulp fiber reinforced resin
JP4799684B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Method for producing pulp fiber reinforced resin
JP4799683B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Method for producing pulp fiber reinforced resin
JP4799685B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Pulp fiber composite raw material
JP4832593B1 (en) * 2010-11-05 2011-12-07 三菱電機株式会社 Pulp fiber reinforced resin raw material

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011201963A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Method for manufacturing hydrophilic resin, and method for manufacturing molded article of pulp fiber composite resin
JP2011201965A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Process for producing hydrophilic resin and molded article of pulp fiber composite resin
JP2011201966A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Method for manufacturing pulp fiber reinforced resin, and pulp fiber reinforced resin
JP2011201964A (en) * 2010-03-24 2011-10-13 Mitsubishi Electric Corp Method for manufacturing hydrophilic resin, and molded article of pulp fiber composite resin
JP4799682B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Method for producing pulp fiber reinforced resin
JP4799684B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Method for producing pulp fiber reinforced resin
JP4799683B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Method for producing pulp fiber reinforced resin
JP4799685B1 (en) * 2010-11-05 2011-10-26 三菱電機株式会社 Pulp fiber composite raw material
JP4832593B1 (en) * 2010-11-05 2011-12-07 三菱電機株式会社 Pulp fiber reinforced resin raw material

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