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JPS5823160B2 - water treatment agent - Google Patents
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JPS5823160B2 - water treatment agent - Google Patents

water treatment agent

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Publication number
JPS5823160B2
JPS5823160B2 JP54167128A JP16712879A JPS5823160B2 JP S5823160 B2 JPS5823160 B2 JP S5823160B2 JP 54167128 A JP54167128 A JP 54167128A JP 16712879 A JP16712879 A JP 16712879A JP S5823160 B2 JPS5823160 B2 JP S5823160B2
Authority
JP
Japan
Prior art keywords
water
treatment agent
sawdust
water treatment
polymer
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
Application number
JP54167128A
Other languages
Japanese (ja)
Other versions
JPS5689900A (en
Inventor
新保昭三
福崎裕延
柳生理
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.)
Taki Chemical Co Ltd
Original Assignee
Taki Chemical Co Ltd
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 Taki Chemical Co Ltd filed Critical Taki Chemical Co Ltd
Priority to JP54167128A priority Critical patent/JPS5823160B2/en
Publication of JPS5689900A publication Critical patent/JPS5689900A/en
Publication of JPS5823160B2 publication Critical patent/JPS5823160B2/en
Expired legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 本発明は新規な水処理剤に関し、殊に汚泥の脱水剤とし
て優れた効果を発揮する水処理剤に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel water treatment agent, and particularly to a water treatment agent that exhibits excellent effects as a sludge dewatering agent.

下水または有機性廃水を処理する際発生する汚。Dirt generated when treating sewage or organic wastewater.

泥は脱水性が悪く、水分を多含しているために焼却する
にしても多大のエネルギーが必要となるため、汚泥の脱
水過程でできるだけ多くの水分を除去することが必要で
あり、各種の脱水剤が研究され、使用されている。
Sludge has poor dehydration properties and contains a lot of water, so it requires a lot of energy even if it is incinerated. Therefore, it is necessary to remove as much water as possible during the sludge dewatering process. Dehydrating agents are being researched and used.

例えばポリ塩化アルミニウム、硫酸バンド、塩化第二鉄
等の無機凝集剤と脱水助剤石灰との併用である。
For example, an inorganic flocculant such as polyaluminum chloride, aluminum sulfate, or ferric chloride is used in combination with lime as a dehydration aid.

しかしながら、この方法は一般に薬剤の添加量が多く、
又焼却に際しても可燃性に乏しく、補助燃料を多く必要
とし、更には灰分がかなり多。
However, this method generally requires a large amount of added drug;
Furthermore, when incinerated, it has poor flammability, requires a large amount of auxiliary fuel, and has a considerable ash content.

量発生するなどの欠点がある。There are drawbacks such as the generation of large quantities.

そこで近年、これら無機凝集剤に代えて各種の有機凝集
剤が採用されてきている。
Therefore, in recent years, various organic flocculants have been adopted in place of these inorganic flocculants.

しかしながら、これら有機凝集剤は汚泥の凝集性におい
て優れているが、その後の沢過処理において凝集フロッ
クがつぶれやすく、炉材の目づまりが生起し、実際有機
凝集剤のみでは充分な濾過が行えず、脱水率を向上させ
ることは容易でない。
However, although these organic flocculants are excellent in flocculating sludge, the flocs tend to collapse during the subsequent filtration treatment, clogging the furnace material, and in fact, sufficient filtration cannot be achieved with organic flocculants alone. Improving the dehydration rate is not easy.

そのために、これら有機凝集剤の脱水率を向上させる方
法として、おがくず、もみがらくん炭等を添加、混和す
る方法が散見されるが、充分な脱水性を期待できないの
が現状である。
For this reason, as a method of improving the dehydration rate of these organic flocculants, methods of adding and mixing sawdust, rice husk charcoal, etc. have been seen here and there, but at present, sufficient dehydration performance cannot be expected.

そこで本発明者らはこれらおがくずやもみがらを脱水助
剤として使用する方法が汚泥ケーキの焼却を容易にする
という利点をそこなうことなく、更にすぐれた脱水性を
有する脱水剤を得んと研究した結果、本発明を完成した
ものである。
Therefore, the present inventors conducted research to obtain a dehydrating agent that has even better dehydrating properties without sacrificing the advantage that the method of using these sawdust and rice husks as a dehydrating aid facilitates the incineration of sludge cake. As a result, the present invention has been completed.

即ち、本発明は、おがくずまたはもみがらに水溶性ビニ
ルモノマーをグラフト重合させてなる水処理剤に関する
ものである。
That is, the present invention relates to a water treatment agent obtained by graft polymerizing a water-soluble vinyl monomer to sawdust or rice husk.

本発明に用いる水溶性ビニル七ツマ−としてはジメチル
アミノエチル(メタ)アクリレート、ジエチルアミノエ
チル(メタ)アクリレート、これらの塩酸塩、硫酸塩、
酢酸塩等の第三級塩および塩化メチル、ジメチル硫酸あ
るいはジエチル硫酸で四級化された第4級塩、アクリル
酸、メタクリル酸またはこれらのエステル化合物、アク
リルアミド、メタクリルアミド等を挙げることができる
The water-soluble vinyl hexamers used in the present invention include dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, their hydrochlorides, sulfates,
Examples include tertiary salts such as acetate, quaternary salts quaternized with methyl chloride, dimethyl sulfate or diethyl sulfate, acrylic acid, methacrylic acid or ester compounds thereof, acrylamide, methacrylamide, and the like.

一方、本発明に用いるおがくずおよびもみがらは産業廃
棄物として廃棄されるものであるが、これらは粉砕して
用いることが望ましく、その粉砕度に関しては特に限定
されないが大略20〜500メツシユが好ましい。
On the other hand, the sawdust and rice husk used in the present invention are discarded as industrial waste, but it is desirable to use them after pulverization, and the degree of pulverization is not particularly limited, but it is preferably about 20 to 500 mesh.

又別の態様としてはこれらをいぶして炭化して用いても
よい。
In another embodiment, these may be used after being smoldered and carbonized.

本発明の水処理剤は上記おがくずおよびもみがらに水溶
性ビニルモノマーをグラフト重合させて得られるもので
あるが、本発明水処理剤の製造に於て最も驚くべきこと
は、おがくずまたはもみがらをあるいはこれらをいぶし
たものを単に混合し、放置するのみでグラフト重合でき
るということである。
The water treatment agent of the present invention is obtained by graft polymerizing a water-soluble vinyl monomer to the above-mentioned sawdust and rice husk, but the most surprising thing in the production of the water treatment agent of the present invention is that the sawdust or rice husk is Alternatively, graft polymerization can be carried out by simply mixing these smoked materials and leaving them to stand.

通常水溶性ビニルモノマーを重合させるには、重合手段
として触媒、紫外線あるいは放射線が使用されるが、本
発明に於てはこれらの手段を要することなく、おがくず
またはもみがらに水溶性ビニルモノマーをグラフト重合
させることができる。
Normally, a catalyst, ultraviolet light, or radiation is used as a polymerization means to polymerize a water-soluble vinyl monomer, but in the present invention, these methods are not necessary and the water-soluble vinyl monomer is grafted onto sawdust or rice husk. Can be polymerized.

かかる事実からおがくずまたはもみがらが何らかのラジ
カル発生機能を有するものと推定されるが定かでない。
From this fact, it is presumed that sawdust or rice husk has some kind of radical generating function, but it is not certain.

このようなわけで本発明水処理剤は甚だ安価に製造する
ことができるが重合速度を高めるため、あるいは既存設
備の利用を考慮して触媒、紫外線、放射線を重合に際し
、使用することを防げるものではない。
For this reason, the water treatment agent of the present invention can be produced at a very low cost, but in order to increase the polymerization rate or take into consideration the use of existing equipment, it is possible to prevent the use of catalysts, ultraviolet rays, and radiation during polymerization. isn't it.

この様な重合手段を利用するときは周知の重合方法に従
えばよく、特段配慮すべき事項は存しない。
When using such a polymerization method, a well-known polymerization method may be followed, and there are no particular considerations.

従って、単におがくずまたはもみがらと水溶性ビニルモ
ノマーを混合することによりグラフト重合させる場合に
ついて述べればモクマー濃度は一般に20〜90係の範
囲が適当である。
Therefore, in the case where graft polymerization is carried out simply by mixing sawdust or rice husk with a water-soluble vinyl monomer, the appropriate concentration of mokummer is generally in the range of 20 to 90 parts.

また、おがくずまたはもみがらの添加量に関しては制約
はないが、モノマーに対する添加割合が大きくなる程一
般的に重合度は低下する。
Although there are no restrictions on the amount of sawdust or rice husk added, the degree of polymerization generally decreases as the ratio of sawdust or rice husk added to the monomer increases.

反応温度としては20〜80℃が望ましい。The reaction temperature is preferably 20 to 80°C.

今、本発明の水処理剤の効果を具体的に説明すれは次の
通りである。
The effects of the water treatment agent of the present invention will now be specifically explained as follows.

具体例 1 内容量500rILlの攪拌機、窒素導入管、温度計を
取り付けた反応容器にアクリルアミド13:4g、ジメ
チルアミノエチルメタクリレート塩化メチル塩、27.
2&、イオン交換水10gを採り、窒素置換を行いつつ
攪拌溶解させ、液温を60℃に設定した。
Specific Example 1 13:4 g of acrylamide, dimethylaminoethyl methacrylate methyl chloride salt, 27.
2&, 10 g of ion-exchanged water was taken and dissolved with stirring while purging with nitrogen, and the liquid temperature was set at 60°C.

次いで200メツシユ以下のおがくず100gを加え、
攪拌した後10時間重合を行った。
Next, add 100g of sawdust of 200 mesh or less,
After stirring, polymerization was carried out for 10 hours.

この重合体を60℃の水で十分洗浄し、減圧乾燥してグ
ラフト重合体133gを得た。
This polymer was thoroughly washed with water at 60° C. and dried under reduced pressure to obtain 133 g of a graft polymer.

次いで、このグラフト重合体を用いて活性余剰汚泥(懸
濁固形分2.3重量係、pH7,4)に対する脱水性を
試験した。
Next, this graft polymer was used to test the dewaterability of activated surplus sludge (suspended solid content: 2.3% by weight, pH: 7.4).

上記汚泥500rrLlをビーカーに採り、この懸濁固
形分(以下SSと略記する)に対してグラフト重合体2
重1懸濁水を、グラフト重合体中のポリマー換算で第1
図に示す割合で添加すると共に水を加えて全量を600
rulとした後20Or、p、mで10分間攪拌後、
下記に示す条件下でヌツチェ試験を行った。
500rrL of the above sludge was taken into a beaker, and the graft polymer 2 was added to this suspended solid content (hereinafter abbreviated as SS).
The 1st suspension water is added to the 1st suspension water in terms of the polymer in the graft polymer.
Add in the proportion shown in the figure and add water to bring the total amount to 600.
After stirring at 20 Or, p, m for 10 minutes,
The Nutsche test was conducted under the conditions shown below.

〔ヌツチェ試験条件〕[Nutsche test conditions]

減圧度 400 mmHg 濾過面積 95c111 炉 材 東洋濾紙/I6.5A 比較例として、グララド重合体に代えて脱水性において
優れているアクリルアミド系重合体としてストックハウ
ゼン社(ドイツ)の製造に係る商品名“ブレストール4
33K“とおがくずとを本発明水処理剤と同量比、即ち
3:10の割合で用いて同様に試験を行った。
Degree of vacuum: 400 mmHg Filtration area: 95c111 Furnace material: Toyo Roshi/I6.5A As a comparative example, the product name "Bless" manufactured by Stockhausen (Germany) is an acrylamide polymer that has excellent dehydration properties in place of Grarad polymer. Thor 4
A similar test was conducted using 33K'' and sawdust in the same ratio as the water treatment agent of the present invention, that is, at a ratio of 3:10.

その結果を第1図に示す。The results are shown in FIG.

〈ブレストール433にの分析値〉 0.5係水溶液粘度* 190Cp カチオン化率 41係 *粘度はBH型粘度計/1620−ター、30r、p、
m30℃の条件下で測定した。
<Analytical values for Brestall 433> 0.5 coefficient Aqueous solution viscosity * 190Cp Cationation rate 41 coefficient *Viscosity is BH type viscometer / 1620-ter, 30r, p,
The measurement was carried out at 30°C.

第1図から明らかな様に本発明の水処理剤は従来方法即
ち、高分子凝集剤とおがくず等を別々に使用する場合に
比較して少ない添加量で、しかも脱水濾過速度を非常に
高めることができる。
As is clear from Figure 1, the water treatment agent of the present invention can greatly increase the dewatering filtration rate with a smaller amount added than in the conventional method, that is, when a polymer flocculant and sawdust, etc. are used separately. I can do it.

。本発明の水処理剤の利点を列記すると■濾過脱水性が
良好で、濾過速度が速い。
. The advantages of the water treatment agent of the present invention are as follows: (1) Good filtration and dehydration properties and high filtration speed.

◎脱水ケーキの含水率低下が大きい。◎The moisture content of the dehydrated cake decreases significantly.

◎焼却が容易である。等を挙げることができる。◎Easy to incinerate. etc. can be mentioned.

以下に本発明の実施例を掲げ更に説明する。Examples of the present invention are listed below and will be further explained.

実施例 1 内容量500m1の攪拌機、窒素導入管、温度計を取り
付けた反応容器にジメチルアミノエチルメタクリレート
塩化メチル塩40g、イオン交換水10gを採り、窒素
置換を行いつつ攪拌溶解させ、液温を60℃に設定した
Example 1 40 g of dimethylaminoethyl methacrylate methyl chloride salt and 10 g of ion-exchanged water were placed in a reaction vessel with a capacity of 500 ml and equipped with a stirrer, a nitrogen inlet tube, and a thermometer, and dissolved with stirring while purging with nitrogen. It was set at ℃.

次いで300メツシユ以下のもみがら100gを加え、
攪拌した後10時間重合を行った。
Next, add 100g of rice husks of 300 mesh or less,
After stirring, polymerization was carried out for 10 hours.

この重合体を60°Cの水で十分洗浄し、減圧乾燥して
グラフト重合体120gを得た。
This polymer was thoroughly washed with water at 60°C and dried under reduced pressure to obtain 120 g of a graft polymer.

このグラフト重合体2重1懸濁水37m1を具体例1で
用いた活性余剰汚泥500m1に添加して脱水性試験を
行ったところ、その濾過速度は3.4゜・kl/m″、
hrであった。
When 37 ml of this graft polymer 2-ply 1-suspended water was added to 500 ml of activated surplus sludge used in Example 1 and a dewatering test was conducted, the filtration rate was 3.4°·kl/m''.
It was hr.

尚、比較例として商品名“ブレストール444K“(0
,5%水水溶液塵550 cp1カチオン化率100
% )ともみがらとを本発明水処理剤と同量比、即ち3
:10の割合で併用した場合のそれは0.7 kl/
m 、 h rであつた。
As a comparative example, the product name “Breastall 444K” (0
, 5% aqueous solution dust 550 cp1 cationization rate 100
%) The same ratio of rice hulls and the water treatment agent of the present invention, i.e. 3
: When used together at a ratio of 10, it is 0.7 kl/
It was m, hr.

)実施例 2 実施例1で用いた反応容器にアクリルアミド27.9&
、アクリル酸ソーダ(80重量係水溶液)19.7g、
イオン交換水10gを採り、窒素置換を行いつつ攪拌溶
解させ、液温を60°Cに設定した。
) Example 2 In the reaction vessel used in Example 1, acrylamide 27.9 &
, 19.7 g of sodium acrylate (80% aqueous solution by weight),
10 g of ion-exchanged water was taken and dissolved with stirring while purging with nitrogen, and the liquid temperature was set at 60°C.

次いで300メツシユ以下のおが<floogを加え、
攪拌した後20時間重合を行った。
Next, add less than 300 mesh of sawdust,
After stirring, polymerization was carried out for 20 hours.

この重合体を60℃の水で十分洗浄し、減圧乾燥してグ
ラフト重合体132gを得た。
This polymer was thoroughly washed with water at 60° C. and dried under reduced pressure to obtain 132 g of a graft polymer.

このグラフト重合体とポリ塩化アルミニウム(A120
310,2係、塩基度50.3係)とを用いて含油廃水
(油分677ppm、SS323ppm)を処理する試
験を行った。
This graft polymer and polyaluminum chloride (A120
A test was conducted in which oil-containing wastewater (oil content: 677 ppm, SS: 323 ppm) was treated using the following method.

上記含油廃水500m1にポリ塩化アルミニウム200
0ppmを添加し、2分間混合した後、更に上記グラフ
ト重合体2重量係懸濁液2.5 mlを添加、混合した
200ml of polyaluminum chloride to 500ml of the above oil-containing wastewater
After adding 0 ppm and mixing for 2 minutes, 2.5 ml of the above graft polymer 2 weight suspension was further added and mixed.

次いで生成したスカムを除去して油分8ppm、SS6
.6ppmの処理水を得た。
Next, the generated scum was removed and the oil content was 8 ppm, SS6
.. 6 ppm treated water was obtained.

比較例として、グラフト重合体に代えてアクリルアミド
とアクリル酸ソーダを用いて製造した高分子凝集剤(分
子量1000万、アニオン化率30係)とおがくずとを
重量比3:10の割合で併用し、同様に試験した結果、
油分26ppm、8832.5 ppmの処理水を得た
As a comparative example, a polymer flocculant (molecular weight 10 million, anionization ratio 30) produced using acrylamide and sodium acrylate instead of the graft polymer was used in combination with sawdust at a weight ratio of 3:10. As a result of the same test,
Treated water with an oil content of 26 ppm and 8832.5 ppm was obtained.

実施例 3゜ 実施例2のおがくずに代え、もみがらくん炭を用いて同
様に重合を行い、グラフト重合体124gを得た。
Example 3 Polymerization was carried out in the same manner as in Example 2, using rice husk charcoal instead of sawdust, to obtain 124 g of a graft polymer.

このグラフト重合体2重量係懸濁液5.5 mlを実施
例2で用いた含油廃水500m1に添加・混合し、同様
に処理を行った結果、油分71)I)m) S88.2
ppmの処理水を得た。
5.5 ml of this graft polymer 2 weight suspension was added and mixed with 500 ml of oil-containing wastewater used in Example 2 and treated in the same manner, resulting in an oil content of 71)I)m)S88.2
ppm treated water was obtained.

実施例 4゜ 実施例1で用いた反応器にアクリルアミド13.4g1
ジメチルアミン工チルメタクリレート塩化メチル塩27
2g、イオン交換水10gを採り、窒素置換を行いつつ
攪拌溶解させ、液温を60°Cに設定した。
Example 4゜Acrylamide 13.4g1 was added to the reactor used in Example 1.
Dimethylamine methyl methacrylate methyl chloride salt 27
2 g and 10 g of ion-exchanged water were taken and dissolved with stirring while purging with nitrogen, and the liquid temperature was set at 60°C.

次いで200メヅシユ以下のもみがら100gと2.2
−アゾビス(2−アミジノプロパン)2塩酸塩1%水溶
液2.0rnlとを加え、攪拌し後10時間重合を行っ
た。
Next, 100g of rice husks weighing less than 200 medus and 2.2
-Azobis(2-amidinopropane) dihydrochloride 1% aqueous solution (2.0 rnl) was added, stirred, and then polymerized for 10 hours.

この重合体を60℃の水で十分洗浄し、減圧乾燥してグ
ラフト重合体128を得た。
This polymer was thoroughly washed with water at 60°C and dried under reduced pressure to obtain graft polymer 128.

このグラフト重合体2重量係懸濁液43m1を具体例1
で用いた活性余剰汚泥500m1に添加して同様に脱水
性試験を行ったところ、その瀘過速度は3.5 k17
’ m・hrであった。
Specific example 1: 43 ml of this graft polymer 2 weight suspension
When a similar dewatering test was carried out by adding it to 500ml of activated surplus sludge used in
' It was m・hr.

尚、比較例として前記の“ブレストール433K“とも
みがらとを重量比3:10の割合で併用した場合のそれ
は0.9kl/ m” ・h rであった。
As a comparative example, when the above-mentioned "Breastall 433K" and rice hulls were used together at a weight ratio of 3:10, the yield was 0.9 kl/m"·hr.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は具体例の実験結果を示す。 FIG. 1 shows the experimental results of a specific example.

Claims (1)

【特許請求の範囲】 1 おがくずまたはもみがらに水溶性ビニルモノマーを
グラフト重合させてなる水処理剤。 “
[Claims] 1. A water treatment agent obtained by graft polymerizing a water-soluble vinyl monomer to sawdust or rice husk. “
JP54167128A 1979-12-20 1979-12-20 water treatment agent Expired JPS5823160B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54167128A JPS5823160B2 (en) 1979-12-20 1979-12-20 water treatment agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54167128A JPS5823160B2 (en) 1979-12-20 1979-12-20 water treatment agent

Publications (2)

Publication Number Publication Date
JPS5689900A JPS5689900A (en) 1981-07-21
JPS5823160B2 true JPS5823160B2 (en) 1983-05-13

Family

ID=15843946

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54167128A Expired JPS5823160B2 (en) 1979-12-20 1979-12-20 water treatment agent

Country Status (1)

Country Link
JP (1) JPS5823160B2 (en)

Also Published As

Publication number Publication date
JPS5689900A (en) 1981-07-21

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