[go: up one dir, main page]

JPH03245894A - Treatment of waste water - Google Patents

Treatment of waste water

Info

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
Application number
JP4119090A
Other languages
Japanese (ja)
Inventor
Hideki Kajikuri
梶栗 英輝
Yoshinori Nakajima
中島 嘉教
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP4119090A priority Critical patent/JPH03245894A/en
Publication of JPH03245894A publication Critical patent/JPH03245894A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PURPOSE:To treat fine fiber flocs enclosing bubbles to float to an upper layer part by a method wherein bentonite is added to and mixed with waste water containing floated pulp fibers and fine fiber flocs to flocculate and settle the pulp fibers and the fine fiber flocs. CONSTITUTION:By the use of bentonite, the insoluble substances in waste water, for example, pulp fibers, especially, fine fiber flocs enclosing bubbles (air) to float to an upper layer part or highly foamable chemicals are rapidly flocculated and settled to make it possible to obtain extremely excellent effect.

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.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

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).

〔課題を解決するための手段〕[Means to solve the problem]

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.

〔発明を実施するための具体的条件〕[Specific conditions for carrying out the invention]

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.

〔実施例〕〔Example〕

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.

〔発明の効果〕〔Effect of the invention〕

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)

【特許請求の範囲】[Claims] 1)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。
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.
JP4119090A 1990-02-23 1990-02-23 Treatment of waste water Pending JPH03245894A (en)

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)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1176706A (en) * 1997-09-10 1999-03-23 Masujiro Arita Special solid fine powdery flocculant composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1176706A (en) * 1997-09-10 1999-03-23 Masujiro Arita Special solid fine powdery flocculant composition

Similar Documents

Publication Publication Date Title
US3677940A (en) Method of treating scouring and dyeing waste water
US4096061A (en) Recovery and reuse of paint solids from waste water
JP4508600B2 (en) Method and apparatus for treating fluorine-containing wastewater
JPH03245894A (en) Treatment of waste water
JP2834492B2 (en) Papermaking white water treatment method
JPS6349291A (en) Flotation separation of waste water of silicon-polishing
JPH02111407A (en) Waste liquid treatment method
JPH06165993A (en) Decoloring chemical for waste water of dye and dyeing industry and dyeing method therefor
JP4786786B2 (en) Floor cleaning waste liquid treatment agent, floor cleaning waste liquid processing method, and reuse method of floor cleaning waste liquid
CN108503007A (en) A kind of removing arsenic in water material and its application in arsenic-containing waste water processing
CN113149168A (en) Water treatment composition and preparation method thereof
JP2010075928A (en) Treatment method and treatment device for fluorine-containing waste water
KR100209302B1 (en) Wastewater treatment method using fly ash
JPH07106355B2 (en) Waste liquid treatment method
US2301429A (en) Method of and composition for treating water
US4200527A (en) Treating chrome tanning bath recycle stream
JP2008055357A (en) Wastewater treatment method
JP2938270B2 (en) Waste paper pulp wastewater treatment method
JPH1043770A (en) Treatment of waste water containing suspended particle
Johnson Polyelectrolytes as coagulants and coagulation aids
EP0082571B1 (en) A method for clarifying coal liquors with water-soluble, high molecular weight polymers having low concentration of cationic moieties
JP2002079262A (en) Equipment for flocculation and separation treatment
JP3501843B2 (en) Treatment of oil-containing wastewater
JPS6380805A (en) Waste liquid treatment method
JPH0130560B2 (en)