JPH03245894A - Treatment of waste water - Google Patents
Treatment of waste waterInfo
- Publication number
- JPH03245894A JPH03245894A JP4119090A JP4119090A JPH03245894A JP H03245894 A JPH03245894 A JP H03245894A JP 4119090 A JP4119090 A JP 4119090A JP 4119090 A JP4119090 A JP 4119090A JP H03245894 A JPH03245894 A JP H03245894A
- Authority
- JP
- Japan
- Prior art keywords
- bentonite
- wastewater
- pulp fibers
- fine fiber
- fiber flocs
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【発明の詳細な説明】 [産業上の利用分野〕 本発明はベントナイトを利用した排水処理法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a wastewater treatment method using bentonite.
さらに詳しくは、浮上したパルプ繊維及び微細繊維フロ
ックを含む排水処理法に関する。More specifically, the present invention relates to a method for treating wastewater containing floated pulp fibers and fine fiber flocs.
〔従来の技術]
現在の各種工場排水の処理方法としては、さまざまな方
法がある。排水中の懸濁物質の除去には、通常凝集沈殿
法が用いられる。排水中の界面活性剤、染料等の除去に
は活性炭による吸着処理方法が有効である。また、アニ
オン性活性剤、カチオン性活性剤に対しては、その反対
のイオン性を持つ物質を添加することにより、該活性剤
を除去する方法・技術等が開示されている。[Prior Art] There are various methods for treating various types of factory wastewater at present. A coagulation-sedimentation method is usually used to remove suspended solids from wastewater. Adsorption treatment using activated carbon is effective for removing surfactants, dyes, etc. from wastewater. Additionally, methods and techniques for removing anionic and cationic activators by adding a substance having the opposite ionicity have been disclosed.
しかし従来技術には、排水中に存在する物質によっては
効果が小さい場合や、排水量が多い時またはその水質に
よっては、処理コストが多大なため実用化できない場合
もある。また、排水中の溶解懸濁物質等の処理方法とし
ては、上記のようなさまざな方法・技術が開示されてい
るが、不溶解物質、例えば製紙会社ではパルプ繊維、微
細繊維等、特に泡(エアー)を包み込んで上層部に浮上
した微細繊維フロックに効果のある報告は無い。However, the conventional techniques may have little effect depending on the substances present in the wastewater, or may not be put to practical use when the amount of wastewater is large or depending on the quality of the water, due to the high treatment cost. In addition, various methods and techniques such as those described above have been disclosed as methods for treating dissolved and suspended substances in wastewater, but insoluble substances, such as pulp fibers and fine fibers in paper manufacturing companies, especially foams ( There are no reports of effectiveness against fine fiber flocs that float to the upper layer by enveloping air).
製紙会社では、しばしば発泡性の高い薬剤を使用し、排
水中のパルプ繊維、微細繊維等が浮上し、その対策に苦
慮している。Paper manufacturing companies often use highly foaming chemicals, causing pulp fibers, fine fibers, etc. to surface in wastewater, and are struggling to find countermeasures.
また、環境問題から白水のクローズド化の進んでいると
ころ、あるいは今後クローズド化の進む恐れのある製紙
会社から、これらの問題の克服が要請されている。In addition, there are demands from paper companies that are increasingly turning white water into closed systems due to environmental issues, or that are at risk of becoming closed systems in the future, to overcome these problems.
本発明は、該排水中の不溶解物質、例えば製紙会社では
パルプ繊維及び微細繊維等、特に泡(エアー)を包み込
んで上層部に浮上した微細繊維フロックの処理方法を提
供するものである。The present invention provides a method for treating insoluble substances in the wastewater, such as pulp fibers and fine fibers in paper manufacturing companies, especially fine fiber flocs that float to the upper layer by enveloping bubbles (air).
本発明者等は、排水中のパルプ繊維及び微細繊維等、特
に泡(エアー)を包み込んで上層部に浮上した微細繊維
フロックの処理方法を開発すべく鋭意検討を重ねた結果
、パルプ繊維及び微細繊維等にベントナイトを添加・混
合し、浮上する該パルプ繊維及び微細繊維等を凝集・沈
殿処理する方法を見い出すに至ったものである。The present inventors have conducted intensive studies to develop a method for treating pulp fibers, fine fibers, etc. in wastewater, especially fine fiber flocs that float to the upper layer by enveloping bubbles (air). We have discovered a method in which bentonite is added and mixed with fibers, etc., and the floating pulp fibers, fine fibers, etc. are coagulated and precipitated.
即ち、浮上したパルプ繊維及び微細繊維フロックを含む
排水に、ベントナイトを添加・混合し、該パルプ繊維及
び微細繊維フロックを凝集・沈殿せしむることを特徴と
する排水処理法。That is, the wastewater treatment method is characterized by adding and mixing bentonite to wastewater containing floated pulp fibers and fine fiber flocs to coagulate and precipitate the pulp fibers and fine fiber flocs.
本発明の詳細な説明する。 The present invention will be described in detail.
本発明において用いるベントナイトは、一般に市販され
工業的に使用されているものであれば十分である。It is sufficient that the bentonite used in the present invention is one that is generally commercially available and used industrially.
ベントナイトは、火山灰または凝灰岩のガラス賞が分解
して生成したもので、主成分はケイ酸アルミニウムで、
組成は5iOz 50〜70%、 AIz(h10〜2
7%のモンモリロン石を主とした粘土であるが、主成分
鉱物のモンモリロン石以外に微量成分としてタンパク石
、セキエイチョウ石、フッ石等の不純物を含む非常に微
細な粒子でかなりの分布に分けることが出来、熱にはき
わめて安定である。Bentonite is produced by the decomposition of volcanic ash or tuff glass, and its main component is aluminum silicate.
The composition is 5iOz 50-70%, AIz (h10-2
The clay is mainly composed of 7% montmorillonite, but in addition to the main mineral montmorillonite, it is divided into very fine particles that contain impurities such as proteinite, redstone, and fluorite as trace components, and it is divided into quite a distribution. It is extremely stable against heat.
ベントナイトの多くは一般に水中で自然と水を吸って1
0倍近くに膨潤・崩壊するが、中にはしないものもある
。Most of bentonite generally absorbs water naturally in water.
It swells and disintegrates to nearly 0 times, but some do not.
本発明におけるベントナイトは、排水上に浮上したパル
プ繊維及び微細繊維フロックを含む排水の凝集沈殿をさ
せるばかりでなく、本発明の必須要件であるパルプ繊維
及び微細繊維フロックの沈降促進剤、フロック生成荊、
及び吸着剤的役割をも果している。The bentonite used in the present invention not only coagulates and precipitates wastewater containing pulp fibers and fine fiber flocs floating on the wastewater, but also serves as an accelerator for sedimentation of pulp fibers and fine fiber flocs, which is an essential requirement of the present invention, and a floc-forming agent. ,
It also plays the role of an adsorbent.
本発明において、ベントナイト以外にも沈降促進剤とし
てカオリン、消石灰、珪カル等、また吸着剤として活性
炭やその他ホワイトカーボン、珪藻上等も使用可能であ
るが、コスト面で大量の排水処理に向かない点や、凝集
沈殿処理能力の一層のスピード化を図る点からもベント
ナイトがより好ましい、さらに、沈降促進剤、フロンク
生成剤、及び吸着剤の能力を併せもつベントナイトの方
が有利である。In the present invention, in addition to bentonite, kaolin, slaked lime, silica, etc. can be used as sedimentation accelerators, and activated carbon, other white carbon, diatoms, etc. can be used as adsorbents, but they are not suitable for large-scale wastewater treatment due to cost. Bentonite is more preferable from the viewpoint of further speeding up the flocculation and sedimentation processing ability, and furthermore, bentonite is more advantageous because it has the abilities of a sedimentation accelerator, flonk generator, and adsorbent.
本発明で排水に添加するベントナイトの量は、通常50
〜100.000ppmであり、好ましくは100〜5
0.000 pp謹、さらに好ましくは100〜10.
000ppmを添加撹拌する。5opp−未満では、ベ
ントナイトの沈降促進能力が、パルプ繊維及び微細繊維
等、特に泡(エアー)を包み込んで上層部に浮上した微
細繊維フロックの浮力が勝り、−船釣に凝集沈殿処理で
きないという不都合がある。The amount of bentonite added to wastewater in the present invention is usually 50
~100.000 ppm, preferably 100-5
0.000 pp, more preferably 100 to 10.
000 ppm and stir. At less than 5 opp, the sedimentation promoting ability of bentonite is overcome by the buoyancy of fine fiber flocs that float to the upper layer by enveloping pulp fibers and fine fibers, especially bubbles (air). There is.
また、100.000ppmを越えると、凝集沈殿処理
したパルプ繊維及び微細繊維等を原料としてリサイクル
した場合、ベントナイトの表面電位はマイナスを帯びて
いるため、系内の電気的バランス(ゼータ電位等)が崩
れ、紙力増強剤、濾水向上剤あるいは歩留向上剤等の使
用時に支障をきたし、経済的にもロスとなることが予想
され不都合である。In addition, if the concentration exceeds 100,000 ppm, when coagulation-sedimentation treated pulp fibers and fine fibers are recycled as raw materials, the surface potential of bentonite will be negative, so the electrical balance in the system (zeta potential, etc.) will be affected. This is inconvenient because it is expected to crumble and cause problems when using paper strength enhancers, drainage improvers, retention aids, etc., and will also result in economic losses.
さらに、凝集沈殿処理したパルプ繊維及び微細繊維等を
原料としてリサイクルした場合の問題として、紙製品中
にベントナイト等が填料的な働きをし、抄紙工程あるい
は紙物性等に支障をきたす恐れが考えられるので好まし
くない。Furthermore, there is a problem with recycling coagulation-sedimentation treated pulp fibers and fine fibers as raw materials, as bentonite, etc. may act as a filler in paper products, causing problems with the paper-making process or paper properties. So I don't like it.
また、製紙会社の排水中には、抄紙時に添加する填料の
定着助剤として硫酸バンド(Alt (SO4) 51
8H20)が溶存しているため、硫酸バンドのプラス効
果によりベントナイトとパルプ繊維及び微細繊維等と作
用して、特に泡(エアー)を包み込んで上層部に浮上し
た微細繊維がフロックを形成し、フロックの沈降促進能
力を一層上げるのに効果的である。In addition, sulfuric acid band (Alt (SO4) 51
8H20) is dissolved, due to the positive effect of sulfuric acid band, bentonite interacts with pulp fibers, fine fibers, etc., and the fine fibers that float to the upper layer, especially enveloping bubbles (air), form flocs. It is effective in further increasing the sedimentation promotion ability of
従って、必要に応じて無機性凝集助剤として硫酸バンド
の他に、ポリ塩化アルミニウム、塩化第二鉄、塩化第−
鉄等を添加すると一層の効果が期待できる。Therefore, in addition to sulfuric acid, polyaluminum chloride, ferric chloride, and ferric chloride may be used as inorganic coagulation aids as needed.
Further effects can be expected by adding iron or the like.
また有機性凝集助剤には非イオン性のものとしてポリア
クリルアミド、アニオン性のものとじてポリアクリルア
ミドの部分加水分解物、アクリルアミドとα、β−不飽
和カルボン酸あるいはそれらのアルカリ金属塩類または
アンモニウム塩類との共重合物、カチオン性のものとし
て、カチオン変性ポリアクリルアミド、アクリルアミド
と第三級アミノ基を有するビニルモノマーまたはそれら
の有機ないし無機の塩類、あるいは該第三級アミノ基を
有するビニルモノマーと四級化剤との反応によって得ら
れる第四級アンモニウム塩類とα、β−不飽和カルボン
酸あるいはそれらのアルカリ金属塩類またはアンモニウ
ム塩類との共重合物、尿素−ホルマリン樹脂、エポキシ
ポリアミド樹脂等を添加しても良い。In addition, organic flocculation aids include polyacrylamide as a nonionic agent, partial hydrolyzate of polyacrylamide as an anionic agent, acrylamide and α, β-unsaturated carboxylic acid, or their alkali metal salts or ammonium salts. Copolymers with cationic polyacrylamide, acrylamide and vinyl monomers having a tertiary amino group or organic or inorganic salts thereof, or copolymers with vinyl monomers having a tertiary amino group and quaternary Copolymers of quaternary ammonium salts obtained by reaction with grading agents and α, β-unsaturated carboxylic acids or their alkali metal salts or ammonium salts, urea-formalin resins, epoxy polyamide resins, etc. are added. It's okay.
ベントナイトを添加する排水の温度、pHはその領域に
かかわらず処理可能である。Treatment is possible regardless of the temperature and pH of the wastewater to which bentonite is added.
以下に実施例で本発明の詳細な説明するが、本発明はこ
れら実施例に限定されるものではない。The present invention will be explained in detail below using Examples, but the present invention is not limited to these Examples.
実施例1
200ccのトールビーカーに、製紙会社で問題となっ
ている泡(エアー)を包み込んで排水上層部に浮上した
パルプ繊維及び微細繊維フロックを50cc取り、全体
で200ccになるよう市水で希釈し、均一に分散する
よう十分に撹拌した。この場合、泡(エアー)を包み込
んでいるパルプ繊維及び微細繊維フロックであるため、
数分後には再度上層部に浮上、2層に分離することが確
認された。Example 1 In a 200cc tall beaker, take 50cc of the pulp fibers and fine fiber flocs that floated to the top of the drainage water by enclosing bubbles (air), which is a problem in paper manufacturing companies, and dilute with city water to make a total of 200cc. and stirred thoroughly to ensure uniform dispersion. In this case, since it is pulp fiber and fine fiber flock that envelops bubbles (air),
After a few minutes, it was confirmed that it floated to the upper layer again and separated into two layers.
次に、上記2層に分離することが確認された、排水に、
ベントナイトを0.08g (400ppm)を添加し
均一に分散するよう2〜3分間十分に撹拌し、懸濁液の
状態を静置して観察した。パルプ繊維及び微細繊維の沈
殿あるいは再浮上するまでの時間を測定した。その結果
を第1表に示した。Next, the wastewater, which was confirmed to separate into the above two layers,
0.08 g (400 ppm) of bentonite was added and thoroughly stirred for 2 to 3 minutes so as to be uniformly dispersed, and the state of the suspension was observed while standing still. The time required for pulp fibers and fine fibers to settle or resurface was measured. The results are shown in Table 1.
実施例2
ベントナイトの添加量を200ppmに変更した以外は
、実施例1と同一の排水を使用し、同一操作で行なった
。その結果を第1表に示した。Example 2 The same waste water as in Example 1 was used and the same operations were carried out, except that the amount of bentonite added was changed to 200 ppm. The results are shown in Table 1.
実施例3
ベントナイトを消石灰に、添加量を400ppmに変更
した以外は、実施例1と同一の排水を使用し、同一操作
で行なった。その結果を第1表に示した。Example 3 The same waste water as in Example 1 was used and the same operations were carried out, except that bentonite was replaced with slaked lime and the amount added was changed to 400 ppm. The results are shown in Table 1.
比較例1
ベントナイトを一般市販凝集剤(アクリルアマイド系)
に変更した以外は、実施例1と同一の排水を使用し、同
一操作で行なった。その結果を第1表に示した。Comparative Example 1 Bentonite was used as a general commercial flocculant (acrylamide type)
The same wastewater as in Example 1 was used and the same operations were performed except for the change. The results are shown in Table 1.
比較例2
ベントナイトを添加しないで、実施例1と同一の排水を
使用し、同一操作で行なった。その結果を第1表に示し
た。Comparative Example 2 The same waste water as in Example 1 was used and the same operation was carried out without adding bentonite. The results are shown in Table 1.
実施例4
実施例1で使用した製紙会社の排水とは、別の製紙会社
で問題となっている、泡(エアー)を包み込んで排水上
層部に浮上したパルプ繊維及び微細繊維フロ7クと、ベ
ントナイトの添加量を1 、 OOOppmに変更した
以外は、実施例1と同一操作で行なった。その結果を第
2表に示した。Example 4 The wastewater from the paper manufacturing company used in Example 1 was different from the pulp fibers and fine fibers that floated to the upper layer of the wastewater by enveloping bubbles (air), which was a problem at another paper manufacturing company. The same operation as in Example 1 was carried out except that the amount of bentonite added was changed to 1.00 ppm. The results are shown in Table 2.
実施例5
ベントナイトを消石灰に変更した以外は、実施例4と同
一の排水を使用し、同一操作で行なった。Example 5 The same wastewater as in Example 4 was used and the same operations were carried out except that bentonite was changed to slaked lime.
その結果を第2表に示した。The results are shown in Table 2.
比較例3
ベントナイトを一般市販凝集剤(アクリルアマイド系)
に変更した以外は、実施例4と同一の排水を使用し、同
一操作で行なった。その結果を第2表に示した。Comparative Example 3 Bentonite was used as a general commercial flocculant (acrylamide type)
The same wastewater as in Example 4 was used and the same operations were performed except that the procedure was changed to . The results are shown in Table 2.
比較例4
ベントナイトを添加しないで、実施例4と同一の排水を
使用し、同一操作で行なった。その結果を第2表に示し
た。Comparative Example 4 The same waste water as in Example 4 was used and the same operation was carried out without adding bentonite. The results are shown in Table 2.
従来の技術では、製紙会社排水中の不溶解物質、例えば
パルプ繊維及び微細繊維等、特に泡(エアー)を包み込
んで上層部に浮上した微細繊維フロックに対しては、十
分に処理できなかった。Conventional techniques have not been able to adequately treat insoluble substances in wastewater from paper manufacturing companies, such as pulp fibers and fine fibers, especially fine fiber flocs that float to the upper layer by enveloping bubbles (air).
しかし、本発明のベントナイトによる排水処理法を用い
ることにより、製紙会社排水中の不溶解物質、例えばパ
ルプ繊維及び微細繊維等、特に泡(エアー)を包み込ん
で上層部に浮上した微細繊維フロックあるいは発泡性の
高い薬剤を使用している製紙会社の排水に対し、すばや
く凝集・沈殿せしめ極めて優れた効果を得ることができ
る。However, by using the wastewater treatment method using bentonite of the present invention, insoluble substances in wastewater from paper manufacturing companies, such as pulp fibers and fine fibers, and especially fine fiber flocks or foams that surround bubbles (air) and float to the upper layer. It quickly coagulates and precipitates wastewater from paper manufacturing companies that use highly toxic chemicals, resulting in extremely excellent effects.
特に、本発明の排水処理法は、排水規制問題、地球環境
問題あるいは資源問題等を背景に製紙会社白水の益々の
クローズド化を考えると、将来的にも極めて重要な方法
である。In particular, the wastewater treatment method of the present invention will be an extremely important method in the future, considering that white water in paper manufacturing companies will become increasingly closed due to wastewater regulation issues, global environmental issues, resource issues, etc.
Claims (1)
水に、ベントナイトを添加・混合し、該パルプ繊維及び
微細繊維フロックを凝集・沈殿せしむることを特徴とす
る排水処理法。1) A wastewater treatment method characterized by adding and mixing bentonite to wastewater containing floated pulp fibers and fine fiber flocs to coagulate and precipitate the pulp fibers and fine fiber flocs.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4119090A JPH03245894A (en) | 1990-02-23 | 1990-02-23 | Treatment of waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4119090A JPH03245894A (en) | 1990-02-23 | 1990-02-23 | Treatment of waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03245894A true JPH03245894A (en) | 1991-11-01 |
Family
ID=12601502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4119090A Pending JPH03245894A (en) | 1990-02-23 | 1990-02-23 | Treatment of waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03245894A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1176706A (en) * | 1997-09-10 | 1999-03-23 | Masujiro Arita | Special solid fine powdery flocculant composition |
-
1990
- 1990-02-23 JP JP4119090A patent/JPH03245894A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1176706A (en) * | 1997-09-10 | 1999-03-23 | Masujiro Arita | Special solid fine powdery flocculant composition |
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