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JPS632987B2 - - Google Patents
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JPS632987B2 - - Google Patents

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Publication number
JPS632987B2
JPS632987B2 JP60076158A JP7615885A JPS632987B2 JP S632987 B2 JPS632987 B2 JP S632987B2 JP 60076158 A JP60076158 A JP 60076158A JP 7615885 A JP7615885 A JP 7615885A JP S632987 B2 JPS632987 B2 JP S632987B2
Authority
JP
Japan
Prior art keywords
polymer
weight
polyacrylamide
solution
present
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
JP60076158A
Other languages
Japanese (ja)
Other versions
JPS61233029A (en
Inventor
Hikaru Konishi
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.)
DKS Co Ltd
Original Assignee
Dai Ichi Kogyo Seiyaku 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 Dai Ichi Kogyo Seiyaku Co Ltd filed Critical Dai Ichi Kogyo Seiyaku Co Ltd
Priority to JP7615885A priority Critical patent/JPS61233029A/en
Publication of JPS61233029A publication Critical patent/JPS61233029A/en
Publication of JPS632987B2 publication Critical patent/JPS632987B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、ポリアクリルアミド系高分子化合物
溶液の安定化法に関する。 水溶性高分子化合物、たとえばポリアクリルア
ミド系高分子化合物は、一般に重合が容易で、比
較的ゆるやかな条件で極めて高い分子量物が得ら
れる。このポリアクリルアミド系高分子化合物の
溶液物性を利用して水処理剤、土壌改質剤、繊維
加工剤、油水分離剤、石油回収用薬剤など多枝に
わたる分野に実用化されている。一方、欠点とし
て分解を起こし易い点がある。例えば、ポリアク
リルアミド水溶液を室温にて放置しておくと、比
較的短期間のうちに水溶液調製時に有していた粘
性を有さなくなることがある。この現象は高温時
や溶液中にFe2+や、Co2+の遷移金属塩が存在す
る場合顕著であり、はなはだしい場合には水の粘
性と変わらなくなつてしまう場合がある。 以上のような問題点の解決をすべき種々の検討
がなされている。たとえば米国特許第3337356号
および同第3493539号では、紫外線吸収剤を用い
て、劣化を防止している。 一方、ポリアクリルアミド系化合物の高分子粘
性挙動を利用した分野として、石油回収用薬剤が
ある。ところが、高温の油層中に長期間存在する
ため、前記ポリマーの劣化が問題となる。この場
合の高分子化合物水溶液の粘性低下は、水中の溶
存酵素やFe2+、Co2+の遷移金属イオンの関与す
るラジカル反応によるものと考えられている。こ
のことからNa2So3やNaHSO3、あるいはチオ尿
素等の添加により劣化の抑制ができることは知ら
れている。(米国特許第3235523号、同第3234163
号参照) これとは別に、酸素の存在下で劣化抑制作用を
呈するものに、ホルムアルデヒドや種々のアルコ
ールがある。(Journal of Petroleum
technology、Aug.1981、P1513〜参照)この他
に、含S・N化合物(例えば2−メルカプトベン
ゾチアゾールや2−メルカプトベンゾチアゾー
ル)などの安定剤の効果も知られている。(特公
昭58−47414号、特公昭44−26645号および特開昭
55−65696号参照) これら従来技術は、その安定化作用という面で
はまだ十分ではなく、たとえ安定化作用があつた
としても、安定剤をポリマーに対して大量に添加
しなければならないことや、Fe2+や、Co2+のよ
うな遷移金属イオンに対して、その効果は十分で
はなかつた。 本発明者は、これら従来技術の問題点を解消す
べく、鋭意研究の結果、本発明に到達したもので
ある。即ち、ポリアクリルアミド系高分子化合物
溶液に、2−メルカプトベンゾチアゾールのアミ
ン塩を配合することを特徴とする水溶性高分子化
合物溶液の安定化方法を提供するものである。 本発明安定剤2−メルカプトベンゾチアゾール
アミン塩のアミンとしては、アルキルアミン、環
状アミンなどがある。アミン塩を使用することに
より、通常使用されているアルカリ塩やアンモニ
ウム塩よりも更に安定化が図れる。特に、70℃以
上の高温において、その効果が著しい。これは、
通常のアルカリ塩では還元性がなく、アンモニウ
ム塩では、高温下において溶液中から散逸してし
まうのに比し、アミン塩では、そのようなことが
ないことによる。 本発明でいうポリアクリルアミド系高分子化合
物とは、アクリルアミド重合体、アクリルアミド
部分を含む共重合体あるいは、これらの混合物を
いう。共重合体を構成する一方の成分である単量
体としては、具体的にはメタアクリルアミド、
(メタ)アクリル酸(塩)、アクリロニトリル、2
−アクリルアミド−2−メチルプロパンスルホン
酸(塩)、ジ−メチルアミノエチルメタクリレー
ト、アクリル酸低級アルキルエステル、ビニルピ
リジンなどの親水性単量体である。また、共重合
反応によつたものに限らず、たとえば、アクリル
アミド重合体中のアミド基の50%以下を例えば加
水分解したり、メチロール化またはマンニツヒ化
するなど高分子反応により他の官能基を導入した
ものも包含する。本発明において、ポリアクリル
アミド系高分子化合物溶液濃度は約0.0001〜20重
量%水溶液、好ましくは0.001〜5重量%である。 次に、本発明における安定化剤の使用はポリア
クリルアミド系高分子化合物100重量部に対して
0.01〜20重量部が好ましく、0.01重量部未満では
安定剤の効果を発揮することができず、また20重
量部を越えると、経済的効果が期待できない。 本発明安定剤には、1・3ジフエニルグアニジ
ン、ジ−o−トリルグアニジン、1−o−トリル
ビグアニドなどのグアニジン化合物、エチレンジ
アミン四酢酸(以下、EDTA)、そのアルカリ
塩、アンモニウム塩などを併用できる。 ポリマー溶液に使用する水は、主として海水や
地層水等の比較的塩分濃度の高い水が利用され、
必要に応じて不溶物濾過や、バクテリアの殺菌
剤、防蝕剤等を添加することができる。 次に、本発明を実施例により具体的に説明す
る。 (以下の実施例で測定するスクリーン・フアク
ターは、ポリマー水溶液の粘性を示す指標の一つ
で、これは実際の油層中を流れる粘性と相関する
ものである。スクリーン・フアクターは、約30ml
の流体容積を持ち、5枚の0.25インチ径の
100meshステンレススチール製金網からなるスク
リーン粘度計を用いて、ポリマー水溶液とその溶
媒との通過時間の比で示される。測定にあたつて
は各ポリマー溶液を各50℃、70℃、80℃の恒温槽
に保存し、経日毎の測定は、ポリマー溶液の測定
温度を25℃とした。なお、溶存酸素の除去は実施
しなかつた。) 尚、本発明において用いた各種ポリマーの分子
量は次式によつて求めた。 [η]=3.73×10-4M0.66 [η]=1N硝酸ナトリウム中の極限粘度(30℃) M=分子量 実施例 1 分子量約1700万のアクリルアミド重合体
500ppm、塩化ナトリウム3%及び塩化カルシウ
ム0.03%からなる水溶液において、2−メルカプ
トベンゾチアゾール(以下Mと略す)単独、2−
メルカプトベンゾチアゾールのシクロヘキシルア
ミン(以下MHと略す)単独を対系15ppm添加溶
解し、80℃経日安定性を測定した結果は次の表1
のとおりであつた。 実施例 2 分子量約1000万の部分加水分解率20mol%のア
クリルアミド重合体500ppm、塩化ナトリウム3
%及び塩化カルシウム0.03%からなる水溶液にお
いて、MH、MH/1−0−トリルビグアニド=
1/1、MH/EDTA=1/1配合比のものを対
系10ppm添加して溶解し、70℃にて保存し、前記
条件下で測定した結果は、第2表のとおりであつ
た。 実施例 3 アクリルアミド80重量部、アクリル酸ナトリウ
ム15重量部、2−アクリルアミド−2−メチルプ
ロパンスルホン酸ナトリウム5重量部からなる分
子量約700万の共重合体500ppm、塩化ナトリウム
3%及び塩化カルシウム0.3%からなる水溶液に
おいて、2−メルカプトベンゾチアゾールのNa
塩、2−メルカプトベンゾチアゾールのトリエタ
ノールアミン塩を対系50ppm添加し、封管中に密
閉した後、90℃にて保存し、前記条件下で測定し
た結果は、第3表のとおりであつた。 比較例 1 アクリルアミド85重量部、アクリル酸ナトリウ
ム15重量部からなる分子量1100万の共重合
1000ppm、塩化ナトリウム3%及び塩化カルシウ
ム0.03%からなる水溶液において、M単独、MH
単独、MH/ジ−O−トリルビグアニド=1/
1、MH/EDTA=1/1のものを対系20ppmず
つ添加し、50℃、70℃、80℃の各温度にて保存
し、前記条件下で測定した結果は第4表のとおり
であつた。
The present invention relates to a method for stabilizing a polyacrylamide-based polymer compound solution. Water-soluble polymer compounds, such as polyacrylamide-based polymer compounds, are generally easy to polymerize, and extremely high molecular weight products can be obtained under relatively mild conditions. Utilizing the solution properties of this polyacrylamide-based polymer compound, it has been put to practical use in a wide variety of fields, including water treatment agents, soil conditioners, fiber processing agents, oil-water separation agents, and oil recovery agents. On the other hand, the drawback is that it tends to decompose. For example, if an aqueous polyacrylamide solution is left at room temperature, it may lose the viscosity it had when it was prepared within a relatively short period of time. This phenomenon is noticeable at high temperatures or when transition metal salts such as Fe 2+ or Co 2+ are present in the solution, and in extreme cases, the viscosity may become as high as that of water. Various studies have been made to solve the above problems. For example, in US Pat. No. 3,337,356 and US Pat. No. 3,493,539, UV absorbers are used to prevent deterioration. On the other hand, oil recovery agents are a field that utilizes the polymer viscosity behavior of polyacrylamide compounds. However, since the polymer remains in the high-temperature oil layer for a long period of time, deterioration of the polymer becomes a problem. The decrease in viscosity of the aqueous solution of the polymer in this case is thought to be due to a radical reaction involving enzymes dissolved in the water and transition metal ions such as Fe 2+ and Co 2+ . From this, it is known that deterioration can be suppressed by adding Na 2 So 3 , NaHSO 3 , thiourea, or the like. (U.S. Patent No. 3235523, U.S. Patent No. 3234163
(See No.) Apart from this, formaldehyde and various alcohols exhibit deterioration inhibiting effects in the presence of oxygen. (Journal of Petroleum
Technology, Aug. 1981, P1513~) In addition, the effects of stabilizers such as S/N-containing compounds (for example, 2-mercaptobenzothiazole and 2-mercaptobenzothiazole) are also known. (Special Publication No. 58-47414, Special Publication No. 44-26645 and
(Refer to No. 55-65696) These conventional techniques are not yet sufficient in terms of their stabilizing effect; even if they had a stabilizing effect, a large amount of stabilizer had to be added to the polymer; The effect was not sufficient for transition metal ions such as Fe 2+ and Co 2+ . The present inventor has arrived at the present invention as a result of intensive research in order to solve the problems of these conventional techniques. That is, the present invention provides a method for stabilizing a water-soluble polymer compound solution, which is characterized by blending an amine salt of 2-mercaptobenzothiazole into a polyacrylamide-based polymer compound solution. Examples of the amine of the 2-mercaptobenzothiazoleamine salt of the stabilizer of the present invention include alkyl amines and cyclic amines. By using an amine salt, more stabilization can be achieved than the commonly used alkali salts and ammonium salts. The effect is particularly remarkable at high temperatures of 70°C or higher. this is,
This is because ordinary alkali salts do not have reducing properties, and ammonium salts dissipate from the solution at high temperatures, whereas amine salts do not. The polyacrylamide-based polymer compound as used in the present invention refers to an acrylamide polymer, a copolymer containing an acrylamide moiety, or a mixture thereof. Specifically, the monomer that is one of the components constituting the copolymer includes methacrylamide,
(meth)acrylic acid (salt), acrylonitrile, 2
- Hydrophilic monomers such as acrylamide-2-methylpropanesulfonic acid (salt), di-methylaminoethyl methacrylate, acrylic acid lower alkyl ester, and vinylpyridine. In addition, other functional groups can be introduced not only through copolymerization reactions but also through polymer reactions such as hydrolyzing 50% or less of the amide groups in the acrylamide polymer, methylolation, or mannitzization. It also includes those who have. In the present invention, the concentration of the polyacrylamide polymer compound solution is about 0.0001 to 20% by weight aqueous solution, preferably 0.001 to 5% by weight. Next, the use of the stabilizer in the present invention is based on 100 parts by weight of the polyacrylamide polymer compound.
The amount is preferably from 0.01 to 20 parts by weight; if it is less than 0.01 parts by weight, the effect of the stabilizer cannot be exhibited, and if it exceeds 20 parts by weight, no economic effect can be expected. The stabilizer of the present invention can be used in combination with guanidine compounds such as 1,3-diphenylguanidine, di-o-tolylguanidine, and 1-o-tolyl biguanide, ethylenediaminetetraacetic acid (hereinafter referred to as EDTA), its alkali salts, ammonium salts, etc. can. The water used for the polymer solution is mainly water with relatively high salt concentration, such as seawater or geological formation water.
If necessary, insoluble matter filtration, bacterial sterilizers, anticorrosive agents, etc. can be added. Next, the present invention will be specifically explained using examples. (The screen factor measured in the following examples is one of the indicators indicating the viscosity of the polymer aqueous solution, and it correlates with the viscosity flowing in the actual oil layer.The screen factor is approximately 30 ml.
of fluid volume and five 0.25 inch diameter
Using a screen viscometer consisting of a 100 mesh stainless steel wire gauze, it is expressed as the ratio of the transit time between the polymer aqueous solution and its solvent. For measurements, each polymer solution was stored in thermostats at 50°C, 70°C, and 80°C, and the measurement temperature of the polymer solution was set at 25°C for daily measurements. Note that dissolved oxygen was not removed. ) The molecular weights of the various polymers used in the present invention were determined using the following formula. [η] = 3.73×10 -4 M 0.66 [η] = Intrinsic viscosity in 1N sodium nitrate (30°C) M = Molecular weight Example 1 Acrylamide polymer with a molecular weight of approximately 17 million
In an aqueous solution consisting of 500 ppm, 3% sodium chloride, and 0.03% calcium chloride, 2-mercaptobenzothiazole (hereinafter abbreviated as M) alone, 2-
Cyclohexylamine (hereinafter abbreviated as MH) of mercaptobenzothiazole alone was added and dissolved at 15 ppm relative to the system, and the stability over time at 80°C was measured. The results are shown in Table 1 below.
It was as follows. Example 2 500 ppm of acrylamide polymer with a molecular weight of about 10 million and a partial hydrolysis rate of 20 mol%, 3 sodium chloride
% and calcium chloride 0.03%, MH, MH/1-0-tolylbiguanide =
1/1, MH/EDTA = 1/1 blending ratio was added at 10 ppm based on the system, dissolved, stored at 70°C, and measured under the above conditions. The results are shown in Table 2. Example 3 500 ppm copolymer with a molecular weight of approximately 7 million, consisting of 80 parts by weight of acrylamide, 15 parts by weight of sodium acrylate, and 5 parts by weight of sodium 2-acrylamide-2-methylpropanesulfonate, 3% of sodium chloride, and 0.3% of calcium chloride. In an aqueous solution consisting of 2-mercaptobenzothiazole, Na
The triethanolamine salt of 2-mercaptobenzothiazole was added at 50 ppm, sealed in a sealed tube, stored at 90°C, and the results measured under the above conditions are as shown in Table 3. Ta. Comparative Example 1 Copolymerization with a molecular weight of 11 million consisting of 85 parts by weight of acrylamide and 15 parts by weight of sodium acrylate.
In an aqueous solution consisting of 1000 ppm, 3% sodium chloride and 0.03% calcium chloride, M alone, MH
Alone, MH/di-O-tolylbiguanide = 1/
1. Add 20 ppm of MH/EDTA = 1/1 to the sample, store at 50°C, 70°C, and 80°C, and measure under the above conditions. The results are shown in Table 4. Ta.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 ポリアクリルアミド系高分子化合物溶液に、
2−メルカプトベンゾチアゾールのアミン塩を配
合することを特徴とするポリアクリルアミド系高
分子化合物溶液の安定化方法。
1 Into the polyacrylamide polymer compound solution,
A method for stabilizing a polyacrylamide-based polymer compound solution, which comprises blending an amine salt of 2-mercaptobenzothiazole.
JP7615885A 1985-04-09 1985-04-09 Stabilization of water-soluble polymeric compound solution Granted JPS61233029A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7615885A JPS61233029A (en) 1985-04-09 1985-04-09 Stabilization of water-soluble polymeric compound solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7615885A JPS61233029A (en) 1985-04-09 1985-04-09 Stabilization of water-soluble polymeric compound solution

Publications (2)

Publication Number Publication Date
JPS61233029A JPS61233029A (en) 1986-10-17
JPS632987B2 true JPS632987B2 (en) 1988-01-21

Family

ID=13597241

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7615885A Granted JPS61233029A (en) 1985-04-09 1985-04-09 Stabilization of water-soluble polymeric compound solution

Country Status (1)

Country Link
JP (1) JPS61233029A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2506613B2 (en) * 1986-02-07 1996-06-12 三井サイテック 株式会社 Stabilization method of acrylamide polymer aqueous solution
JP4677110B2 (en) * 2001-03-13 2011-04-27 ダイヤニトリックス株式会社 Method for producing acrylamide polymer composition

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4927659A (en) * 1972-07-18 1974-03-12

Also Published As

Publication number Publication date
JPS61233029A (en) 1986-10-17

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