JP4189072B2 - Felt cleaning method for papermaking - Google Patents
Felt cleaning method for papermaking Download PDFInfo
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- JP4189072B2 JP4189072B2 JP02881499A JP2881499A JP4189072B2 JP 4189072 B2 JP4189072 B2 JP 4189072B2 JP 02881499 A JP02881499 A JP 02881499A JP 2881499 A JP2881499 A JP 2881499A JP 4189072 B2 JP4189072 B2 JP 4189072B2
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- Prior art keywords
- felt
- acid
- papermaking
- cleaning
- water
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Description
【0001】
【発明の属する技術分野】
本発明は製紙工業の脱水工程で使用される抄紙用フェルトの洗浄方法に関するものである。
【0002】
【従来の技術】
製紙工程は、パルプ調成、抄造、脱水、乾燥等の工程から成り立っている。パルプは抄造して、抄き網部において大部分の水を取り去り湿紙とするが、この湿紙は、なお多くの水分を有している。このまま加熱乾燥すると多量の蒸気を必要とするので、脱水工程を設けプレス脱水してから乾燥工程へ送られる。脱水工程は、上下2段のロールからなるプレスロールと、湿紙を運搬するフェルトの組み合わせからなり、フェルトに載せられた湿紙はロールの間を通してプレス脱水される。プレスにおける脱水は、フェルトの搾水性に大きく依存しており、フェルトに汚れが付着し目詰まりがあると脱水が十分に行われず、また均一な脱水ができないため、ドライヤー工程での蒸気消費量が増えたり、また紙切れの原因となる。従って、フェルトを常に清浄な状態に保つことが生産性を増大させる上で極めて重要である。
【0003】
パルプ調成工程では、サイズ剤や染料等のパルプ繊維への定着、歩留まり、濾水向上あるいはピッチコントロールを目的として硫酸バンドが多量に添加されている。硫酸バンドはpH条件によって種々の形態のアルミナ種を形成し、酸性抄紙条件である白水のpHが4〜5においては、一部は3価のアルミニウムイオンもしくは水溶性のアルミナ種として存在する。
【0004】
脱水工程のフェルトは、搾水効率を良好に維持するためシャワー水がかけられている。しかし、シャワー水は清水を用いるので、そのpHは白水より高いことから、湿紙水分中のアルミナ種はpH上昇により水酸化アルミニウムとなってフェルト表面およびその内部に析出し、フェルトの搾水性に悪影響を及ぼすことがある。
【0005】
そこで、従来、シャワー水に塩酸、硫酸等の無機酸を連続添加し、pHの上昇を抑える方法が行われているが、取り扱い上の危険性や系内の腐食性の問題点があるほか、フェルトを劣化させることがあった。
【0006】
また、クエン酸、リンゴ酸等のキレート作用を有する有機酸を連続添加する方法(特開平4−348195号公報)、1−ヒドロキシエチリデン−1,1−ジホスホン酸を連続添加する方法(特開平4−202299号公報)が提案されているが、白水pHが低く、白水中の溶解アルミニウム濃度が高い抄紙系においては、多量の薬剤が必要となり、経済面および腐食性の面で問題点があった。
【0007】
また、上述したような連続洗浄のほか、紙の抄き換え時等に抄造を一旦停止して10〜30分間間欠洗浄が行われる。間欠洗浄時には、通常、フェルトに付着したサイズ剤や木材樹脂のケン化、デンプンや微生物代謝物の水和膨潤、水酸化アルミニウムスケールの溶解等を目的として苛性ソーダ水溶液が使用されるが、洗浄時間が短いため、水酸化アルミニウムスケールに対して十分な溶解効果が得られていない。
【0008】
【発明が解決しようとする課題】
本発明の目的は、製紙工業の脱水工程で使用される抄紙用フェルトを清浄な状態に保つための効果的な洗浄方法を提供することにある。
【0009】
【課題を解決するための手段】
本発明者らは、抄紙用フェルトを清浄な状態に保つ洗浄について鋭意検討した結果、特定のヒドロキシカルボン酸を含む苛性アルカリ水溶液を抄紙用フェルトの洗浄液として用いた場合には、該フェルトの汚れ、特に水酸化アルミニウムスケールを主体とする汚れに対して優れた洗浄効果を示すことを見い出し本発明を完成するに至った。
【0010】
すなわち、本請求項1の発明は、ムチン酸、ガラクトン酸、グルカル酸、グルコン酸、へプトン酸およびそれらの塩から選ばれた1種以上のヒドロキシカルボン酸を0.1〜100g/L含む苛性アルカリ水溶液を洗浄液として用いることを特徴とするフェルトの汚れ成分が水酸化アルミニウムスケールを主体とするものである抄紙用フェルトの洗浄方法であり、請求項2の発明はヒドロキシカルボン酸としてグルコン酸ソーダを用いる抄紙用フェルトの洗浄方法であり、請求項3の発明はヒドロキシカルボン酸としてヘプトン酸ソーダを用いる抄紙用フェルトの洗浄方法である。
【0011】
【発明の実施形態】
以下、本発明について詳細に説明する。
本発明における抄紙用フェルト洗浄液は、ムチン酸、ガラクトン酸、グルカル酸、グルコン酸、ヘプトン酸およびそれらの塩から選ばれた1種以上のヒドロキシカルボン酸を含む苛性アルカリ水溶液である。
【0012】
ヒドロキシカルボン酸には、構造上右旋性のもの、左旋性のものと区別される場合があるが、本発明においてはこれら光学異性体の種類は限定されず、どちらか一方でもよく、あるいは両方の混合物であってもよい。ヒドロキシカルボン酸の塩としては、ソーダ塩、カリウム塩、アンモニウム塩等を挙げることができ、中でも入手しやすいソーダ塩が好ましい。また、ヒドロキシカルボン酸は1種類を単独に、あるいは2種以上組み合わせて用いてもよい。
【0013】
苛性アルカリ水溶液の苛性アルカリとしては、例えば苛性ソーダ、苛性カリ等を挙げることができ、中でも安価な苛性ソーダが好ましい。
【0014】
本発明における洗浄液中のムチン酸、ガラクトン酸、グルカル酸、グルコン酸、ヘプトン酸およびそれらの塩の濃度は、0.1〜100g/L、好ましくは1〜50g/L、さらに好ましくは5〜30g/Lである。0.1g/L未満では本発明の意図する効果が十分でなく、また100g/Lを越えた濃度では効果は十分に認められるが、経済的見地から好ましくない。
【0015】
本発明における洗浄液中の苛性アルカリの濃度は特に限定されるものではないが、通常5〜50g/L、好ましくは10〜30g/Lである。
【0016】
本発明洗浄液は、ヒドロキシカルボン酸と苛性アルカリを溶解させた水溶液であり、その適用方法は特に限定されるものではない。たとえば、ヒドロキシカルボン酸と苛性アルカリを所定濃度に溶解した洗浄液を調製し、これを抄紙用フェルトにシャワーする方法、あるいはシャワー水にヒドロキシカルボン酸と苛性アルカリを所定濃度になるように連続注入する方法がある。
【0017】
本発明により抄紙用フェルトを洗浄するには、例えば抄造工程を停止した後、本発明洗浄液をフェルト上にシャワーすればよい。洗浄頻度は工程の必要度により任意に決められるが、2〜3日に1回、紙の抄き換え時等に10〜30分間程度行う間欠洗浄、10〜20日に1回、1〜2日間かけて抄紙機全体を洗浄する停抄洗浄が行われる。
【0018】
本発明洗浄液には、本発明の効果を損なわない範囲において、界面活性剤やスケール除去剤等その他の種類の添加剤を併用することに何ら制限を加えるものではない。
【0019】
【実施例】
以下に、実施例により本発明を具体的に説明するが、本発明はこれに限定されるものではない。
【0020】
実施例1
酸性上質紙の抄造工程から採取した抄紙用フェルト(材質:ナイロン)を用いてフェルト洗浄試験を行った。
【0021】
(試験方法)
1.洗浄前の採取したフェルトを5cm×15cmの大きさに切ったフェルトを電気炉で900℃、3時間焼いた。フェルト上の無機スケール成分を灰分として求めた。
【0022】
2.採取したフェルトを5cm×15cmの大きさに切って試験用のフェルトとし、これを所定濃度の洗浄液中に浸漬し、30℃にて20分間保った。次いでフェルトを取り出し、水洗して薬品を取り除いた後、乾燥した。このフェルトを電気炉で900℃で3時間加熱し、灰化させた。下式にて洗浄率を求めた。
【0023】
【数1】
【0024】
(試験結果)
結果を表1に示した。
【0025】
【表1】
【0026】
実施例2
ライナー抄造工程から採取した抄紙用フェルトを使用し、実施例1と同様にしてフェルトに付着している無機分を灰分として求めた。
【0027】
【0028】
2.採取したフェルトを10cm×20cmの大きさに切って試験用フェルトとした。このフェルトを所定濃度の洗浄液に浸漬し、30℃にて30分間保った。浸漬後のフェルトについて、ガラス製セパラブル濾過器(容量500mL、濾過面35mmφ)にセットし、差圧10mmHgに吸引しつつ、水500mLを濾過器に注ぎ、水がフェルトを通過するのに要した時間を測定し、この時間を通水時間とした。通水時間はフェルトの搾水能力を評価する特性値であり、フェルトに付着あるいは目詰まりしている汚れの量との間に相関関係があることに基づいている。
【0029】
(試験結果)
結果を表2に示した。
【0030】
【表2】
【0031】
表1、2の結果から、本発明の抄紙用フェルト洗浄方法は、水酸化アルミニウムスケールを主体とする抄紙フェルト汚れに対して極めて高い洗浄効果を奏することが認められた。
【0032】
【発明の効果】
本発明によれば、製紙工業の脱水工程で使用される抄紙用フェルトの汚れ成分である水酸化アルミニウムスケールに対し、十分な洗浄効果を有するため、フェルトの搾水性が保持される。その結果、フェルトの汚れに起因する操業性の低下や製品の品質を損なうことがなくなり、紙パルプ工業に益するところが大である。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for cleaning a papermaking felt used in a dewatering process in the paper industry.
[0002]
[Prior art]
The papermaking process is composed of processes such as pulp preparation, papermaking, dehydration, and drying. Pulp is made into paper and most of the water is removed from the paper making net to make wet paper, which still has a lot of water. If heat drying is performed as it is, a large amount of steam is required, so a dehydration step is provided and press dehydration is performed before sending to the drying step. The dewatering step includes a combination of a press roll composed of two upper and lower rolls and a felt for transporting the wet paper, and the wet paper placed on the felt is press-dehydrated between the rolls. Dehydration in the press greatly depends on the squeezing ability of the felt. If the felt is soiled and clogged, the dehydration will not be performed sufficiently, and uniform dehydration will not be possible. It may increase or cause a piece of paper. Therefore, it is extremely important to keep the felt clean at all times in order to increase productivity.
[0003]
In the pulp preparation process, a large amount of a sulfuric acid band is added for the purpose of fixing to a pulp fiber such as a sizing agent or dye, yield, improving drainage, or controlling the pitch. The sulfuric acid band forms various types of alumina species depending on the pH conditions, and partly exists as trivalent aluminum ions or water-soluble alumina species when the pH of white water, which is acidic papermaking conditions, is 4-5.
[0004]
The felt in the dehydration process is showered with water in order to maintain good water extraction efficiency. However, since the shower water uses fresh water, its pH is higher than that of white water. Therefore, the alumina species in the wet paper moisture becomes aluminum hydroxide and precipitates on the felt surface and inside thereof due to the increase in pH. May have adverse effects.
[0005]
Therefore, conventionally, a method of continuously adding an inorganic acid such as hydrochloric acid or sulfuric acid to shower water to suppress an increase in pH has been performed, but there are problems of handling and corrosive problems in the system, The felt could be deteriorated.
[0006]
In addition, a method of continuously adding an organic acid having a chelating action such as citric acid and malic acid (JP-A-4-348195), a method of continuously adding 1-hydroxyethylidene-1,1-diphosphonic acid (JP-A-4) -202299) has been proposed, but in the papermaking system where the pH of white water is low and the concentration of dissolved aluminum in white water is high, a large amount of chemicals is required, which is problematic in terms of economy and corrosivity. .
[0007]
In addition to the continuous cleaning as described above, the papermaking is temporarily stopped at the time of paper changing and the intermittent cleaning is performed for 10 to 30 minutes. During intermittent cleaning, an aqueous caustic soda solution is usually used for the purpose of saponifying the sizing agent and wood resin adhering to the felt, hydrating and swelling starch and microbial metabolites, and dissolving aluminum hydroxide scale. Since it is short, a sufficient dissolution effect on the aluminum hydroxide scale is not obtained.
[0008]
[Problems to be solved by the invention]
An object of the present invention is to provide an effective cleaning method for keeping a papermaking felt used in a dewatering process in the paper industry in a clean state.
[0009]
[Means for Solving the Problems]
As a result of intensive studies on cleaning that keeps the papermaking felt in a clean state, when a caustic aqueous solution containing a specific hydroxycarboxylic acid is used as a cleaning solution for the papermaking felt, dirt on the felt, In particular, the present invention has been completed by finding that it exhibits an excellent cleaning effect against dirt mainly composed of aluminum hydroxide scale.
[0010]
That is, the invention of claim 1 includes caustic containing 0.1 to 100 g / L of one or more hydroxycarboxylic acids selected from mucinic acid, galactonic acid, glucaric acid, gluconic acid, heptonic acid and salts thereof. a felt soil components method of cleaning papermaking felt is mainly formed of aluminum hydroxide scale, which comprises using an alkaline aqueous solution as a cleaning liquid, the invention of claim 2 gluconate as a hydroxy carboxylic acid a method of cleaning a papermaking felt using a soda, the invention of claim 3 is a method of cleaning a papermaking felt using a heptonic sodium as the hydroxycarboxylic acids.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail.
The felt washing liquid for papermaking in the present invention is a caustic aqueous solution containing one or more hydroxycarboxylic acids selected from mucinic acid, galactonic acid, glucaric acid, gluconic acid, heptonic acid and salts thereof.
[0012]
Hydroxycarboxylic acid may be distinguished from dextrorotatory and levorotatory in structure, but in the present invention, the type of these optical isomers is not limited and either one or both may be used. It may be a mixture of Examples of the salt of hydroxycarboxylic acid include soda salt, potassium salt, ammonium salt, etc. Among them, an easily available soda salt is preferable. Moreover, you may use hydroxycarboxylic acid individually by 1 type or in combination of 2 or more types.
[0013]
Examples of the caustic alkali in the caustic aqueous solution include caustic soda and caustic potash, and among them, inexpensive caustic soda is preferable.
[0014]
In the present invention, the concentration of mucin acid, galactonic acid, glucaric acid, gluconic acid, heptonic acid and their salts is 0.1-100 g / L, preferably 1-50 g / L, more preferably 5-30 g. / L. If the concentration is less than 0.1 g / L, the intended effect of the present invention is not sufficient, and if the concentration exceeds 100 g / L, the effect is sufficiently recognized, but this is not preferable from an economic viewpoint.
[0015]
The concentration of the caustic alkali in the cleaning liquid in the present invention is not particularly limited, but is usually 5 to 50 g / L, preferably 10 to 30 g / L.
[0016]
The cleaning liquid of the present invention is an aqueous solution in which hydroxycarboxylic acid and caustic are dissolved, and the application method is not particularly limited. For example, a method of preparing a cleaning solution in which hydroxycarboxylic acid and caustic are dissolved at a predetermined concentration and showering the solution on papermaking felt, or a method of continuously injecting hydroxycarboxylic acid and caustic alkali to shower water to a predetermined concentration There is.
[0017]
In order to clean the papermaking felt according to the present invention, for example, after the papermaking process is stopped, the cleaning liquid of the present invention may be showered on the felt. The washing frequency is arbitrarily determined depending on the necessity of the process, but once every 2 to 3 days, intermittent washing performed for about 10 to 30 minutes, for example, when changing paper, once every 10 to 20 days, 1 to 2 Stopping cleaning is performed to clean the entire paper machine over a period of days.
[0018]
In the cleaning liquid of the present invention, there is no limitation on the combined use of other types of additives such as surfactants and scale removers, as long as the effects of the present invention are not impaired.
[0019]
【Example】
Hereinafter, the present invention will be specifically described by way of examples. However, the present invention is not limited thereto.
[0020]
Example 1
A felt washing test was performed using a felt for papermaking (material: nylon) taken from the papermaking process of acidic fine paper.
[0021]
(Test method)
1. The felt collected before washing was cut into a size of 5 cm × 15 cm and baked in an electric furnace at 900 ° C. for 3 hours. The inorganic scale component on the felt was determined as ash.
[0022]
2. The collected felt was cut into a size of 5 cm × 15 cm to obtain a test felt, which was immersed in a cleaning solution having a predetermined concentration and kept at 30 ° C. for 20 minutes. Next, the felt was taken out, washed with water to remove the chemicals, and then dried. This felt was incinerated by heating at 900 ° C. for 3 hours in an electric furnace. The washing rate was determined by the following formula.
[0023]
[Expression 1]
[0024]
(Test results)
The results are shown in Table 1.
[0025]
[Table 1]
[0026]
Example 2
Using the papermaking felt collected from the liner papermaking process, the inorganic content adhering to the felt was determined as ash in the same manner as in Example 1.
[0027]
[0028]
2. The collected felt was cut into a size of 10 cm × 20 cm to obtain a test felt. This felt was immersed in a cleaning solution having a predetermined concentration and kept at 30 ° C. for 30 minutes. About the felt after immersion, it was set in a glass separable filter (capacity 500 mL, filtration surface 35 mmφ), and while sucking to a differential pressure of 10 mmHg, 500 mL of water was poured into the filter, and the time required for water to pass through the felt Was measured, and this time was defined as the water passing time. The water passage time is a characteristic value for evaluating the squeezing ability of the felt, and is based on a correlation with the amount of dirt adhering to or clogging the felt.
[0029]
(Test results)
The results are shown in Table 2.
[0030]
[Table 2]
[0031]
From the results shown in Tables 1 and 2, it was confirmed that the papermaking felt cleaning method of the present invention has an extremely high cleaning effect on papermaking felt stains mainly composed of an aluminum hydroxide scale.
[0032]
【The invention's effect】
According to the present invention, since the aluminum hydroxide scale, which is a soil component of the papermaking felt used in the dewatering process of the paper industry, has a sufficient cleaning effect, the felt water squeezability is maintained. As a result, there is no significant loss in operability and product quality due to felt dirt, which greatly benefits the pulp and paper industry.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02881499A JP4189072B2 (en) | 1999-02-05 | 1999-02-05 | Felt cleaning method for papermaking |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02881499A JP4189072B2 (en) | 1999-02-05 | 1999-02-05 | Felt cleaning method for papermaking |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000226786A JP2000226786A (en) | 2000-08-15 |
| JP4189072B2 true JP4189072B2 (en) | 2008-12-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP02881499A Expired - Lifetime JP4189072B2 (en) | 1999-02-05 | 1999-02-05 | Felt cleaning method for papermaking |
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| Country | Link |
|---|---|
| JP (1) | JP4189072B2 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP5334597B2 (en) * | 2009-01-13 | 2013-11-06 | 伯東株式会社 | Antifouling agent composition and antifouling method |
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- 1999-02-05 JP JP02881499A patent/JP4189072B2/en not_active Expired - Lifetime
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|---|---|
| JP2000226786A (en) | 2000-08-15 |
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