JPS59173110A - Composition of polymer flocculating agent - Google Patents
Composition of polymer flocculating agentInfo
- Publication number
- JPS59173110A JPS59173110A JP58047618A JP4761883A JPS59173110A JP S59173110 A JPS59173110 A JP S59173110A JP 58047618 A JP58047618 A JP 58047618A JP 4761883 A JP4761883 A JP 4761883A JP S59173110 A JPS59173110 A JP S59173110A
- Authority
- JP
- Japan
- Prior art keywords
- composition
- flocculating agent
- water
- emulsion
- polymer flocculant
- 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
- Treatment Of Sludge (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は汚泥の脱水を良好な作業環境下に効率よく行い
得る高分子凝集剤組成物に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polymer flocculant composition that can efficiently dewater sludge in a favorable working environment.
下水、し尿、各種産業排水の汚泥の脱水剤として高分子
凝集剤が使用されているが、汚泥およびその脱水ケーキ
よシ発生する悪臭は作業環境を悪化し、その恕臭防止対
木が爪秩な課題となっている。Polymer flocculants are used as dehydrating agents for sludge from sewage, human waste, and various industrial wastewater. However, the foul odor generated by the sludge and its dehydrated cake deteriorates the working environment, and it is difficult to prevent the odor from being removed. This has become a major issue.
この問題を解決するために、香料や精油などの消臭剤紮
汚泥に混合または散布する方法が検討されたが、消臭効
果は悪く、これを改善する目的で粉末高分子凝集剤に消
臭剤を配合して汚泥の脱水と消臭とを同時に行うことに
よシ消臭効果を上げる方法が考えられている。In order to solve this problem, methods of mixing or spraying deodorizing agents such as fragrances and essential oils into sludge were considered, but the deodorizing effect was poor, and in order to improve this, powdered polymer flocculants were added to deodorizing agents. A method of increasing the deodorizing effect by simultaneously dewatering and deodorizing the sludge by adding a deodorizing agent has been considered.
しかしながら、この方法においては消臭剤を配合した高
分子凝集剤を0.1〜0.5%濃度の水溶液に調整した
のちに使用する必硬がるるだめ、密閉下で取扱うことは
困難であり、消臭剤自身の強い臭気による作業環境の悪
化が見られる。However, in this method, the polymer flocculant mixed with the deodorant must be used after being adjusted to an aqueous solution with a concentration of 0.1 to 0.5%, and it is difficult to handle it under closed conditions. , the working environment is worsening due to the strong odor of the deodorant itself.
また、消臭剤が同形の場合には水や汚泥との混和性が著
しく悪く、液状の場合には高分子凝集剤の流動性が失な
われるため、例えはホッパーから高分子凝集剤が流下し
なくなる等の問題が生じて、消臭剤の使用量が著しく制
限される。In addition, if the deodorant has the same shape, it will have extremely poor miscibility with water or sludge, and if it is liquid, the fluidity of the polymer flocculant will be lost, so for example, if the polymer flocculant flows down from the hopper, This causes problems such as the deodorant's deodorizing effect, which significantly limits the amount of deodorant that can be used.
本発明右前はこのような問題に対し、汚泥の消臭と脱水
とを良好な作業環境で効率よく行い得る高分子凝集剤に
ついて鋭意研究した結果、本発明を児成した。すなわち
本発明は、消臭剤を含有する乳濁液状の高分子凝集剤組
成物である0
本発明の高分子凝集剤組成物は液状物として取扱い得る
ので、移送、希釈、汚泥への添加等の作業を完全な密閉
下で自動化することが可能であシ、汚泥の消臭と脱水と
を同時に行うと共しし、良好な作業環境を保ちながら効
率のよい作業を行うことができる。In order to solve these problems, the inventor of the present invention has developed the present invention as a result of intensive research into a polymer flocculant that can efficiently deodorize and dehydrate sludge in a good working environment. That is, the present invention is an emulsion-like polymer flocculant composition containing a deodorizing agent. Since the polymer flocculant composition of the present invention can be handled as a liquid, it can be transported, diluted, added to sludge, etc. It is possible to automate this work in a completely sealed environment, deodorize sludge and dewater it at the same time, and work efficiently while maintaining a good working environment.
本発明の高分子凝集剤組成物は高分子凝集剤1重量部、
水005〜2重量部、疎水性液体05〜10重量部およ
び消臭剤0.01〜2重量部の比率からなり、それらの
合計85〜999重量%と乳化剤0.1〜15重量%と
から成る。消臭剤は乳化重合法等により得られる高分子
凝集剤乳濁液に添加するか、または乳化重合法により高
分子凝集剤乳濁液を製造する際に添加する。乳化重合法
は公知の方法でよく、例えば重合触媒、紫外線、放射線
などを使用する方法である。The polymer flocculant composition of the present invention includes 1 part by weight of a polymer flocculant,
Consisting of a ratio of 0.05 to 2 parts by weight of water, 0.5 to 10 parts by weight of a hydrophobic liquid, and 0.01 to 2 parts by weight of a deodorant, a total of 85 to 999 weight % of these and 0.1 to 15 weight % of an emulsifier. Become. The deodorizer is added to a polymer flocculant emulsion obtained by an emulsion polymerization method or the like, or added when producing a polymer flocculant emulsion by an emulsion polymerization method. The emulsion polymerization method may be a known method, such as a method using a polymerization catalyst, ultraviolet rays, radiation, etc.
また、本発明の高分子凝集剤組成物は移送その他これを
使用する作業においてR1171件のある液状物として
取扱い得る形態であれはよく、この条件を満足するもの
としては油中水型乳濁液が好ましい。乳濁液中の高分子
凝集剤の濃度は5〜65重量%であシs si&量−
以下では輸送等における経済的理由から好ましくなく、
65賞量チ以上の場合はその乳濁液の製造が技術的に困
難である。Furthermore, the polymer flocculant composition of the present invention may be in a form that can be handled as a liquid as specified in R1171 during transportation or other operations using it, and a water-in-oil emulsion that satisfies this condition is sufficient. is preferred. The concentration of polymer flocculant in the emulsion is 5 to 65% by weight.
The following are not preferred for economic reasons such as transportation.
If the amount is 65 or more, it is technically difficult to produce the emulsion.
本発明に使用する高分子凝集剤は汚泥の脱水に効果を有
するものであればよく、一般にはカチオン性のものが用
いられる。カチオン性高分子凝集剤としてはジメチルア
ミノエチルメタクリレート、N−ジメチルアミノプロピ
ルメタクリルアミド等の酸付加塩またid4級化塩の単
独重合体、これらの塩と他のビニル系単量体、例えはア
クリルアミドとの共重合体、ポリアクリルアミドのマン
ニッヒ変性物、ポリエチレンイミン、ポリビニルイミダ
シリンの酸付加塩等が用いられる。また、汚泥の脱水剤
としてはカチオン性高分子凝集剤とアニオン性冒分子凝
集剤とを併用することもできるので、本発明に使用する
高分子凝集剤はアニオン性のものでもよく、例゛えばア
クリル酸塩の単独重合体、アクリル酸塩、アクリルアミ
ド−2−メチルプロパンスルホン酸塩等とアクリルアミ
ドとの共重合体等が用いられる。The polymer flocculant used in the present invention may be any agent as long as it is effective in dewatering sludge, and generally a cationic agent is used. Examples of cationic polymer flocculants include acid addition salts such as dimethylaminoethyl methacrylate and N-dimethylaminopropyl methacrylamide, and homopolymers of ID quaternized salts, these salts and other vinyl monomers, such as acrylamide. Copolymers of polyacrylamide, Mannich-modified products of polyacrylamide, polyethyleneimine, acid addition salts of polyvinylimidacillin, etc. are used. Furthermore, as a dewatering agent for sludge, a cationic polymer flocculant and an anionic polymer flocculant can be used together, so the polymer flocculant used in the present invention may be anionic, for example, A homopolymer of acrylate, a copolymer of acrylate, acrylamide-2-methylpropanesulfonate, etc., and acrylamide, etc. are used.
本発明に使用する消臭剤はメン)−ル、メントン、シネ
オール、ゲラニオール等のテルペン類、ハツカ油、ラベ
ンダー油、シソ油、ユーカリ油、パイン油、スギ油等の
精油、木タール、木酢液等を用いることができる。消臭
剤の添加量は汚泥に対する消臭効果によって決められ、
前記の使用量の範囲内であれば特に限定はなく、組成物
中の疎水性液体が溶媒ともなるので、固形、液状のいず
れも任意の量で添加することができる。The deodorant used in the present invention includes terpenes such as mengol, menthone, cineole, and geraniol, essential oils such as peppermint oil, lavender oil, perilla oil, eucalyptus oil, pine oil, and cedar oil, wood tar, and wood vinegar. etc. can be used. The amount of deodorizing agent added is determined by its deodorizing effect on sludge.
There is no particular limitation as long as the amount used is within the above range, and since the hydrophobic liquid in the composition also serves as a solvent, it can be added in any amount in either solid or liquid form.
本発明に使用する疎水性液体は水に不溶性または僅かに
可溶性の有機溶媒で、乳化重合法による油中水型乳濁液
の製造に通常使用される疎水性液体であれはよく、例え
ばヘプタン、オクタン等の脂肪族炭化水素、シクロペン
クン、シクロヘキサン等の脂環式炭化水素、トルエン、
キシレン等の芳香族炭化水素が好ましい。The hydrophobic liquid used in the present invention is an organic solvent that is insoluble or slightly soluble in water, and may be any hydrophobic liquid commonly used in the production of water-in-oil emulsions by emulsion polymerization, such as heptane, Aliphatic hydrocarbons such as octane, alicyclic hydrocarbons such as cyclopenkune and cyclohexane, toluene,
Aromatic hydrocarbons such as xylene are preferred.
また、本発明に使用する乳化剤は乳化重合法による油中
水型乳濁液の製造に通常使用される乳化剤であればよく
、ポリオキシエチレンラウリルエーテル、ポリエチレン
グリコールラウレート、ポリエチレングリコールモノス
テアレー札、ンルビタンモノラウレート、ポリオキシエ
チレンンルピタンモノラウレ−ト、ポリオキシエチレン
オクチルフェノールエーテル、セチルステアリルソジウ
ムフタレートなどが用いられる。Furthermore, the emulsifier used in the present invention may be any emulsifier commonly used in the production of water-in-oil emulsions by emulsion polymerization, such as polyoxyethylene lauryl ether, polyethylene glycol laurate, polyethylene glycol monostearate, etc. , polyoxyethylene rubitan monolaurate, polyoxyethylene rubitan monolaurate, polyoxyethylene octylphenol ether, cetyl stearyl sodium phthalate, and the like.
本発明の高分子凝集剤組成物は通常の高分子凝集剤と同
様に、その濃度が0.1〜0.5%となるように水で希
釈して使用する。この希釈液を汚泥に加えて混合し、汚
泥中の固形分を凝集させたのちベルト型プレスフィルタ
ー等により濾過すると、脱水ケーキと戸液とに分離され
る。The polymer flocculant composition of the present invention is used by diluting it with water to a concentration of 0.1 to 0.5%, like a normal polymer flocculant. This diluted liquid is added to the sludge and mixed to coagulate the solid content in the sludge, which is then filtered through a belt-type press filter or the like to separate it into a dehydrated cake and a liquid.
これらの過程で高分子凝集剤と共に溶解された消臭剤は
脱水ケーキ中に均一に移行し、脱水ケーキは消臭される
。これらの作業、特に希釈作業においては、本発明の高
分子凝集剤組成物は配管等によシ密閉下で取扱うことが
できるので、作業環境を汚染することはない。In these processes, the deodorizer dissolved together with the polymer flocculant is uniformly transferred into the dehydrated cake, and the dehydrated cake is deodorized. In these operations, especially dilution operations, the polymer flocculant composition of the present invention can be handled in a sealed manner, such as in piping, so that it does not contaminate the working environment.
以下に実施例によシ本発明を説明するが、本発明はこれ
らの実施例により限定されるものではない。The present invention will be explained below with reference to Examples, but the present invention is not limited to these Examples.
実施例1
メタクリロイルオキシエチル−トリメチルアンモニウム
クロリド200g、アクリルアミド100.9,2.2
’−アゾビス(2−アミジノプロパン)塩酸塩0.21
7を蒸留水200dに溶解して冷却し、重合開始剤を含
む単量体の冷溶液を調製した。Example 1 Methacryloyloxyethyl-trimethylammonium chloride 200g, acrylamide 100.9,2.2
'-azobis(2-amidinopropane) hydrochloride 0.21
7 was dissolved in 200 d of distilled water and cooled to prepare a cold monomer solution containing a polymerization initiator.
この冷浴液を、ポリエチレングリコールモノステアレー
)70.9およびユーカリ油90gを含むシクロヘキサ
ン400.9中に窒素通気上攪拌しながら40°Cにて
徐々に加えた。This cold bath liquid was gradually added to 400.9 g of cyclohexane containing 70.9 g of polyethylene glycol monostearate (polyethylene glycol monostearate) and 90 g of eucalyptus oil at 40° C. while stirring under nitrogen aeration.
この混合物を40℃にて2時間攪拌し次のち、2.2′
−アゾビス(2−アミジノプロパン)塩阪塩の10%水
溶液を5M加え、60℃に昇温してさらに2時間攪拌し
たのち冷却した。This mixture was stirred at 40°C for 2 hours and then heated to 2.2'
5 M of a 10% aqueous solution of -Azobis(2-amidinopropane) Shiosaka salt was added, the temperature was raised to 60°C, and the mixture was further stirred for 2 hours, and then cooled.
生成した共重合体とユーカリ油を含む乳濁液はその粘度
をB型回転粘度計を用いて25℃にて測定すると31c
pであシ、良好な流動性を有する安定な乳濁欣であった
。The viscosity of the emulsion containing the produced copolymer and eucalyptus oil was 31c when measured at 25°C using a B-type rotational viscometer.
It was a stable emulsion with good fluidity.
実施例2
ユーカリ油を添加せずに実施例1に記載と同様の方法で
反応させて得た共重合体を含有する乳濁液に、ユーカリ
油9rJflを攪拌しながら加えて均質な乳淑:液とし
た。この乳濁gは実施例1に記載と同様の方法で測定し
たときの粘度が31、5 cpであシ、良好な流動性を
有する安定な乳濁液であった。Example 2 To an emulsion containing a copolymer obtained by reacting in the same manner as described in Example 1 without adding eucalyptus oil, 9 rJfl of eucalyptus oil was added with stirring to obtain a homogeneous milk extract: It was made into a liquid. This emulsion g had a viscosity of 31.5 cp when measured in the same manner as described in Example 1, and was a stable emulsion with good fluidity.
比較例
高分子凝集剤として使用されるメタクリロイルオキシエ
チルトリメチルアンモニウムクロリドとアクリルアミド
との共重合体の粉末100Iにユーカリ油3gを加えて
混合した。別に同じ共重合体の粉末100gにユーカリ
油101/を加えて混合した。Comparative Example 3 g of eucalyptus oil was added to 100I powder of a copolymer of methacryloyloxyethyltrimethylammonium chloride and acrylamide used as a polymer flocculant and mixed. Separately, 101 g of eucalyptus oil was added to 100 g of powder of the same copolymer and mixed.
50°の角度を有するホッパー(長さ12crrL。Hopper with an angle of 50° (length 12crrL).
流下口・径15箭)にこれらの粉末をそれぞれ入れ、ホ
ッパー下部の流下口よりこれらの粉末を流下させたとこ
ろ、ユーカリ油を混合する前の粉末は自然に流下したが
、ユーカリ油3gを加えた粉末はホッパーを振動させな
いと流下せず、ユーカリ油10gを加えた粉末は振動さ
せても流下しなかった。When these powders were put into a flow port (diameter: 15 mm) and allowed to flow down from the flow port at the bottom of the hopper, the powder before mixing with eucalyptus oil naturally flowed down, but when 3 g of eucalyptus oil was added, The powder to which 10 g of eucalyptus oil was added did not flow down even when the hopper was vibrated.
従って、粉末の高分子凝集に3%以上の量の液状の消臭
剤を加えたものは、粉末としての流動性が低下し、取扱
いが困難になることがわかった。Therefore, it has been found that when 3% or more of a liquid deodorant is added to the polymer agglomerates of powder, the fluidity of the powder decreases, making it difficult to handle.
試験例
イ)実施例1で得た高分子凝集剤とユーカリ油とを含有
する乳濁液、口)実施例2で得た高分子凝集剤とユーカ
リ油とを含有する乳濁液、ハ)ユーカリ油の代りに同量
のノ・ツカ油を用いて実施例1に記載と同様の方法で得
た乳濁液、二)ユーカリ油の代りに同量のノ・ツカ油を
用いて実施例2に記載と同様の方法で得た乳濁液、ホ)
ユーカリ油の代りに同量のスギ油を用いて実施例2に記
載と同様の方法で得た乳濁液、およびへ)ユーカリ油9
0gの代シにユーカリ油9Iを用いて実施例2に記載と
同様の方法で得た乳濁液をそれぞれ用いて、下水処理場
の汚泥を固液分離したときの結果を表1に示す。Test Examples A) Emulsion containing the polymer flocculant obtained in Example 1 and eucalyptus oil, mouth) Emulsion containing the polymer flocculant obtained in Example 2 and eucalyptus oil, C) Emulsion obtained in the same manner as described in Example 1 using the same amount of No-Tsuka oil in place of eucalyptus oil; 2) Example using the same amount of No-Tsuka oil in place of eucalyptus oil. Emulsion obtained by the same method as described in 2), e)
Emulsion obtained in the same manner as described in Example 2 using the same amount of cedar oil in place of eucalyptus oil, and f) Eucalyptus oil 9
Table 1 shows the results of solid-liquid separation of sludge from a sewage treatment plant using emulsions obtained in the same manner as described in Example 2 using 0 g of eucalyptus oil 9I.
比較のため、ト)比較例の粉末高分子凝集剤1001に
ユーカリ油3?を加えたもの、およびチ)実施例2にお
いてユーカリ油を添加する前に得た高分子凝集剤乳濁液
をそれぞれ用いたときの結果も表1に示す。For comparison, g) Eucalyptus oil 3? Table 1 also shows the results when using the polymer flocculant emulsion obtained before adding eucalyptus oil in Example 2, and h) the polymer flocculant emulsion obtained before adding eucalyptus oil in Example 2.
臭気の測定は官能試駆にょシ測定者io人の平均値で示
した。臭気の快・不快度および臭気の強度の測定は次の
基準によった。The odor measurement was expressed as the average value of io number of sensory testers. The degree of pleasantness/displeasure of the odor and the intensity of the odor were measured according to the following criteria.
臭気の快・不快度 臭気の強度
+1:やや快 0:無臭
0:快でも不快でもない 1:弱くにおう−1:やや不
快 2:はっきシにおう−2:不快
3:強くにおう−3:非常に不快Pleasure/discomfort level of odor Odor intensity +1: Slightly pleasant 0: No odor 0: Neither pleasant nor unpleasant 1: Slight odor -1: Slightly unpleasant 2: Clear odor -2: Unpleasant
3: Strong odor - 3: Very unpleasant
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58047618A JPS59173110A (en) | 1983-03-22 | 1983-03-22 | Composition of polymer flocculating agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58047618A JPS59173110A (en) | 1983-03-22 | 1983-03-22 | Composition of polymer flocculating agent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59173110A true JPS59173110A (en) | 1984-10-01 |
Family
ID=12780201
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58047618A Pending JPS59173110A (en) | 1983-03-22 | 1983-03-22 | Composition of polymer flocculating agent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59173110A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0220931U (en) * | 1988-07-29 | 1990-02-13 | ||
US5145925A (en) * | 1990-04-04 | 1992-09-08 | Daikin Industries Ltd. | Chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer |
-
1983
- 1983-03-22 JP JP58047618A patent/JPS59173110A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0220931U (en) * | 1988-07-29 | 1990-02-13 | ||
US5145925A (en) * | 1990-04-04 | 1992-09-08 | Daikin Industries Ltd. | Chlorotrifluoroethylene/perfluoro(alkyl vinyl ether) copolymer |
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