JP2663145B2 - Oil layer preparation method using water-in-oil swellable emulsion - Google Patents

Oil layer preparation method using water-in-oil swellable emulsion

Info

Publication number
JP2663145B2
JP2663145B2 JP14801188A JP14801188A JP2663145B2 JP 2663145 B2 JP2663145 B2 JP 2663145B2 JP 14801188 A JP14801188 A JP 14801188A JP 14801188 A JP14801188 A JP 14801188A JP 2663145 B2 JP2663145 B2 JP 2663145B2
Authority
JP
Japan
Prior art keywords
water
oil
swellable polymer
oil layer
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 - Fee Related
Application number
JP14801188A
Other languages
Japanese (ja)
Other versions
JPH01318686A (en
Inventor
羊一 細川
透 福島
理恵 深山
彦忠 坪井
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 SAITETSUKU KK
Original Assignee
MITSUI SAITETSUKU KK
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 SAITETSUKU KK filed Critical MITSUI SAITETSUKU KK
Priority to JP14801188A priority Critical patent/JP2663145B2/en
Publication of JPH01318686A publication Critical patent/JPH01318686A/en
Application granted granted Critical
Publication of JP2663145B2 publication Critical patent/JP2663145B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、地層より石油を有効に回収する方法に関す
るものであり、更に詳しく言えば油中水型水膨潤性重合
体エマルジョンを用いて油層の浸透率を調整する方法に
関する。
Description: FIELD OF THE INVENTION The present invention relates to a method for effectively recovering petroleum from a stratum, and more particularly, to an oil reservoir using a water-in-oil type water-swellable polymer emulsion. The present invention relates to a method for adjusting the penetration rate of a material.

[従来の技術] 原油を地下油層より生産するに際して、生産井より原
油とともに多量の水分が生産される。産出された原油は
随伴する水を分離しなければならず、この分離にかかる
経済的費用が問題となる。更に重要なことは、井戸の全
生産量は装置により制限されているため、随伴する水に
よって原油生産量が低くなることである。随伴する水の
量を減少させれば原油生産速度が上がり、なおかつ分離
にかかる費用も抑えられ、原油生産上極めて有効であ
る。
[Prior Art] When a crude oil is produced from an underground oil reservoir, a large amount of water is produced together with the crude oil from a production well. The crude oil produced must separate the associated water and the economic cost of this separation is problematic. More importantly, the entrained water reduces crude oil production, as the total well production is limited by the equipment. Decreasing the amount of accompanying water increases the rate of crude oil production and reduces the cost of separation, which is extremely effective in producing crude oil.

生産井からの水の生産は、主に油層の外側の地層から
の地下水の流出(ウォーターコーニング)と、水攻法あ
るいは他の水溶液を注入する三次攻法によって注入され
た水あるいは水溶液が油層中の高浸透率層(水の通り易
い層)、あるいは油層中に存在するフラクチャーを通っ
て流出されるものである。すなわち油層の多くは水の通
り易さ(浸透率)の異なった層より成っており、水攻法
あるいは他の水溶液を用いた三次攻法は、これらの層に
水あるいは水溶液を圧入して各層内に存在する原油を押
し出そうとするものであるが、高浸透率部分より優先的
に原油が押し出され、この部分の圧入水が生産井から早
く流出されることにより原油の産出の際に多量の水が随
伴されることになる。さらに圧入水によって原油が押し
出された部分はさらに水が通り易くなり、まだ多量に原
油の残っている邸浸透率部分からの原油の生産速度を低
下させる。
The production of water from production wells is mainly based on the outflow of groundwater from the formation outside the reservoir (water coning) and the water or aqueous solution injected by water flooding or tertiary flooding in which another aqueous solution is injected. Through the high-permeability layer (a layer through which water easily passes) or the fracture existing in the oil layer. In other words, most oil layers are composed of layers with different water permeability (permeability). In the water flooding method or the third flooding method using other aqueous solutions, water or an aqueous solution is injected into these layers and each layer is pressed. It is intended to push out the crude oil present in the oil, but the crude oil is pushed out in preference to the high permeability portion, and the injection water in this portion flows out of the production well earlier, causing A large amount of water will be entrained. Further, the portion where the crude oil is extruded by the injection water becomes more easily permeable, and reduces the production rate of the crude oil from the house permeability portion where a large amount of the crude oil still remains.

これらの水の生成を減少させる方法の1つとして、ア
クリルアミド共重合体および他の水溶性高分子の架橋体
で油層を処理する方法である。代表的な特許として米国
特許第3,749,172号、第3,762,476号、第3,785,437号、
第3,909,423号、第3,949,811号、第3,952,806号、第3,9
78,928号、第4,018,286号、第4,076,628号、第4,110,22
6号がある。
One method of reducing the production of water is to treat the oil layer with a crosslinked product of an acrylamide copolymer and another water-soluble polymer. U.S. Pat.Nos. 3,749,172, 3,762,476, 3,785,437 as representative patents,
No. 3,909,423, No. 3,949,811, No. 3,952,806, No. 3,9
No. 78,928, No. 4,018,286, No. 4,076,628, No. 4,110,22
There is No. 6.

これらの技術は水溶性高分子と架橋剤を用いることを
特徴とする技術である。すなわち水溶性高分子の水溶液
に架橋剤を加えて地層へ注入中、または注入後地下の地
層中で高分子を架橋させ、生成した架橋体で水の通り易
い層中の水路及びフラクチャーを詰めて水を通り難くし
たり、水を全く通らなくしたりする技術である。これら
の技術により、注入水はこれまで水が通り難かった低浸
透率層にも多く流れていき、原油の生産速度を上昇させ
ることとなる。
These techniques are characterized by using a water-soluble polymer and a crosslinking agent. That is, a crosslinking agent is added to the aqueous solution of the water-soluble polymer during the injection into the formation, or after the injection, the polymer is cross-linked in the underground formation, and the generated crosslinked product is used to fill the waterways and fractures in the water-easy layer. It is a technology that makes it difficult to pass water or makes it completely impermeable. By these techniques, the injection water flows to a low permeability layer where water has been difficult to pass so far, thereby increasing the production rate of crude oil.

これら公知の技術は大別すると、クロミウムゲル法と
クエン酸アルミニウム法に分類できる。
These known techniques can be roughly classified into a chromium gel method and an aluminum citrate method.

クロミウムゲル法は主に油層中のフラクチャーを詰め
るのに用い、地上で水溶性高分子と架橋剤を混合して注
入するか、または両者を同時に注入する方法であり、代
表例としては水溶性高分子としてアクリルアミドとアク
リル酸の共重合体、架橋剤としては重クロム酸ナトリウ
ム−亜硫酸ナトリウムを用いるものが挙げられる。
The chromium gel method is mainly used to pack the fractures in the oil layer, and is a method in which a water-soluble polymer and a cross-linking agent are mixed and injected on the ground, or both are injected at the same time. As a molecule, a copolymer using acrylamide and acrylic acid, and as a crosslinking agent, one using sodium dichromate-sodium sulfite may be used.

クエン酸アルミニウム法は主に油層の浸透率を低下さ
せるのに用い、水溶性高分子と架橋剤、すなわちクエン
酸アルミニウムとを交互に注入して地下で架橋させる方
法である。
The aluminum citrate method is mainly used to lower the permeability of an oil layer, and is a method of alternately injecting a water-soluble polymer and a crosslinking agent, that is, aluminum citrate, and crosslinking underground.

[発明が解決しようとする課題] これらの技術の問題点は第一にその架橋方法にある。
すなわち、両方法とも地下で架橋させる方式をとってい
るため、油層の条件によっては架橋が起こらず油層の浸
透率を低下させることができない、またはフラクチャー
を詰めることができないという点にある。更にクロミウ
ムゲル法では架橋が早く起きてしまうと油層の注入口近
傍でゲル化してしまい注入井を使用不能にしてしまうこ
ともある。
[Problems to be Solved by the Invention] The problem of these technologies lies first in the crosslinking method.
That is, since both methods employ a method of crosslinking underground, crosslinking does not occur depending on the conditions of the oil layer, so that the permeability of the oil layer cannot be reduced or the fracture cannot be packed. Furthermore, in the chromium gel method, if crosslinking occurs early, gelation occurs near the injection port of the oil layer, which may render the injection well unusable.

第二の問題点としては処理効果の問題である。油層を
処理する際、注入した水溶性高分子等が高浸透率層のみ
ならず低浸透率層にも入り、この部分の浸透率も低下さ
せてしまい、処理効果を低下させることである。
The second problem is a problem of the processing effect. When the oil layer is treated, the injected water-soluble polymer or the like enters not only the high-permeability layer but also the low-permeability layer, so that the permeability of this portion is reduced, and the treatment effect is reduced.

以上の二点は、公知技術を実施する際の根本的問題点
であり、本質的な改良方法が特に要望されていた。
The above two points are fundamental problems when implementing the known technique, and an essential improvement method has been particularly demanded.

[課題を解決するための手段] 本発明者らは、上記の欠点のない油層の改良方法につ
き種々検討を続けた結果、以下に記す通りの優れた方法
を見いだすことに成功し本発明を完成するに至った。
[Means for Solving the Problems] The present inventors have continued various studies on a method for improving an oil layer without the above-mentioned disadvantages, and as a result, have succeeded in finding an excellent method as described below and completed the present invention. I came to.

すなわち、従来法では水溶性高分子と架橋剤を地層中
に注入し、注入中あるいは注入後架橋させる方式が用い
られているが、これは架橋した高分子重合体を直接地下
の処理が必要な地層まで注入することが実際に困難であ
るからである。
That is, in the conventional method, a method of injecting a water-soluble polymer and a cross-linking agent into the formation and performing cross-linking during or after the injection is used, but this requires direct underground treatment of the cross-linked polymer. This is because it is actually difficult to inject into the stratum.

あらかじめ架橋した高分子重合体を使用すれば、著し
く高い注入圧を必要とし、しかも注入用の井戸を詰めて
使用不能とする恐れが大である。従って架橋重合体を直
接地層中へ注入することは現実的でなく、実際に試みる
ことも困難であった。
The use of a pre-crosslinked high molecular weight polymer requires a remarkably high injection pressure, and furthermore, there is a high possibility that the injection wells will be packed and become unusable. Therefore, it is not practical to inject the crosslinked polymer directly into the formation, and it is difficult to actually try it.

ところが、本発明者らは、水溶性のビニルモノマーを
油中水型のエマルジョンとして架橋剤の共存下に重合し
て得られる油中水型水膨潤性高分子重合体エマルジョン
は、驚くべきことに架橋された重合体でありながら未架
橋の水溶性ポリマーと同様、容易に地層中へ注入可能で
あることを見いだした。
However, the present inventors have surprisingly found that a water-in-oil type water-swellable polymer emulsion obtained by polymerizing a water-soluble vinyl monomer as a water-in-oil type emulsion in the presence of a crosslinking agent is surprising. It has been found that, like a cross-linked polymer, it can be easily injected into the formation as well as an uncross-linked water-soluble polymer.

すなわち、この油中水型水膨潤性重合体は、微細なエ
マルジョン粒子よりなるため水に均一に分散させること
ができ、本質的には水に不溶でありながら外観、性状で
は水可溶性重合体と全く差異がない分散液として存在す
る。従って、この分散液は、水溶性重合体と全く同様に
容易に地層中への圧入が可能であることが見いだされ、
従来技術や公知の知識から全く予期できなかった架橋重
合体である水膨潤性重合体エマルジョンを直接地層中に
注入するという全く新規な手法が見いだされた。
In other words, this water-in-oil type water-swellable polymer can be uniformly dispersed in water because it is composed of fine emulsion particles, and is essentially insoluble in water while having an appearance and properties as a water-soluble polymer. Present as a dispersion with no difference. Therefore, it has been found that this dispersion can be pressed into the formation just as easily as the water-soluble polymer,
A completely new approach has been discovered in which a water-swellable polymer emulsion, which is a crosslinked polymer, which was completely unexpected from the prior art and known knowledge, is directly injected into the formation.

本発明は、水溶性高分子と架橋剤を用いることによる
上述の架橋時の欠点を有するものでなく、すでに架橋さ
れた油中水型水膨潤性重合体エマルジョンを用いること
を特徴とし、従来技術の欠点である架橋時の問題点、お
よび浸透率の改良効果を大幅に向上させたものである。
すなわち本発明の方法は重合時に架橋剤を加えて架橋体
とした油中水型水膨潤性重合体エマルジョンを用いるこ
とを特徴とする技術である。
The present invention does not have the above-mentioned disadvantages at the time of crosslinking by using a water-soluble polymer and a crosslinking agent, and is characterized by using an already crosslinked water-in-oil type water-swellable polymer emulsion. The problems of cross-linking, which are drawbacks, and the effect of improving the permeability are greatly improved.
That is, the method of the present invention is a technique characterized by using a water-in-oil type water-swellable polymer emulsion which is formed into a crosslinked product by adding a crosslinking agent during polymerization.

すなわち、本発明は、 (1)油中水型膨潤性重合体エマルジョンを直接使用す
るか、または該エマルジョンより油および水分を除去し
て得られる水膨潤性重合体を使用することを特徴とする
油層調整方法、 (2)水膨潤性重合体としてアクリルアミド重合体、ア
クリルアミドと他のモノマーとの共重合体、アクリル酸
及びその塩の重合体、およびカチオン基含有単量体の重
合体の少なくとも1種から選ばれる架橋体を使用するこ
とを特徴とする前記(1)の油層調整方法、 (3)水膨潤性重合体エマルジョンを油層に注入する際
に、水膨潤性重合体を含む注入水のpHおよび/または塩
濃度を変えることにより水膨潤性重合体粒子の大きさを
調整して、処理しようとする地層に水膨潤性重合体を注
入することを特徴とする前記(1)および(2)の油層
調整方法、 (4)注入され地下に保持された水膨潤性重合体を、pH
および/または塩濃度を調整した注入水で処理し膨脹あ
るいは縮小させて、浸透率を変えることを特徴とする前
記(1)および(2)の油層調整方法、 に関する。
That is, the present invention is characterized in that (1) directly using a water-in-oil swellable polymer emulsion or using a water-swellable polymer obtained by removing oil and water from the emulsion. (2) At least one of an acrylamide polymer, a copolymer of acrylamide and another monomer, a polymer of acrylic acid and a salt thereof, and a polymer of a cationic group-containing monomer as the water-swellable polymer (1) The method for preparing an oil layer according to (1), wherein a crosslinked product selected from the species is used. (3) When the water-swellable polymer emulsion is injected into the oil layer, the injection water containing the water-swellable polymer is used. (1) and (1) wherein the size of the water-swellable polymer particles is adjusted by changing the pH and / or salt concentration, and the water-swellable polymer is injected into the formation to be treated. Reservoir adjustment method), (4) is injected and held in the underground water-swellable polymers, pH
And / or changing the permeability by treating with an injection water whose salt concentration has been adjusted and expanding or reducing the same to change the permeability.

以下、本発明を詳しく説明する。 Hereinafter, the present invention will be described in detail.

油中水型水膨潤性重合体エマルジョンは、ビニル単量
体として水溶性ビニル単量体の1種又は2種以上、もし
くは水溶性ビニル単量体の1種以上と、水溶性ビニル単
量体と共重合可能なビニル単量体の1種以上、架橋剤と
しては、水溶性ビニルモノマーと共重合可能なものを含
む水溶液を界面活性剤を含む有機分散媒中に注入して乳
化させた後、ラジカル重合させて得られるものである。
The water-in-oil type water-swellable polymer emulsion comprises, as a vinyl monomer, one or more water-soluble vinyl monomers, or one or more water-soluble vinyl monomers, and a water-soluble vinyl monomer. After emulsifying an aqueous dispersion containing at least one kind of vinyl monomer copolymerizable with a water-soluble vinyl monomer as a cross-linking agent into an organic dispersion medium containing a surfactant, , Obtained by radical polymerization.

水溶性ビニル単量体としては、任意の水溶性ビニル単
量体、あるいはその塩を使用することができる。具体例
としては、(メタ)アクリルアミド、N,N−ジメチルア
クリルアミド、(メタ)アクリル酸、2−アクリルアミ
ド−2−メチルプロパンスルホン酸、ビニルスルホン
酸、スチレンスルホン酸、イタコン酸、アリールスルホ
ン酸、ジメチルアミノエチルメタクリレートメチルクロ
ライド4級塩、ジエチルジアリルアンモニウムクロライ
ド、ジメチルジアリルアンモニウムクロライド等が挙げ
られる。好ましい水溶性ビニル単量体としては、アクリ
ルアミド、アクリル酸(塩)、ジメチルアミノエチルメ
タクリレートメチルクロライド4級塩の1種又は2種以
上が挙げられる。
As the water-soluble vinyl monomer, any water-soluble vinyl monomer or a salt thereof can be used. Specific examples include (meth) acrylamide, N, N-dimethylacrylamide, (meth) acrylic acid, 2-acrylamido-2-methylpropanesulfonic acid, vinylsulfonic acid, styrenesulfonic acid, itaconic acid, arylsulfonic acid, dimethyl Aminoethyl methacrylate methyl chloride quaternary salt, diethyldiallylammonium chloride, dimethyldiallylammonium chloride and the like can be mentioned. Preferred water-soluble vinyl monomers include one or more of acrylamide, acrylic acid (salt), and dimethylaminoethyl methacrylate methyl chloride quaternary salt.

アクリル酸及び上記の各種酸は塩の形でも重合に使用
できる。塩の具体例としては、ナトリウム、カリウム、
アンモニウム塩等を挙げることができる。
Acrylic acid and the various acids mentioned above can also be used for the polymerization in salt form. Specific examples of salts include sodium, potassium,
Ammonium salts and the like can be mentioned.

架橋剤としては水溶性ビニル単量体と共重合可能なも
のが用いられ、その具体例としては、N,N−メチレンビ
スアクリルアミド、ジアリルフタレート、ジビニルベン
ゼン、(ポリ)エチレングリコールジ(メタ)アクリレ
ート等が挙げられる。好ましい架橋剤としては、N,N−
メチレンビスアクリルアミドが挙げられる。添加量は水
溶性ビニル単量体に対して0.0005〜5重量%、好ましく
は0.001〜1重量%である。
As the cross-linking agent, one that can be copolymerized with a water-soluble vinyl monomer is used. Specific examples thereof include N, N-methylenebisacrylamide, diallyl phthalate, divinylbenzene, and (poly) ethylene glycol di (meth) acrylate. And the like. Preferred crosslinking agents include N, N-
Methylene bisacrylamide is exemplified. The amount of addition is 0.0005 to 5% by weight, preferably 0.001 to 1% by weight, based on the water-soluble vinyl monomer.

油中水型膨潤性エマルジョンを構成する油成分は有機
性分散媒であり、例えば飽和直鎖炭化水素、分岐状飽和
炭化水素、脂環族系炭化水素、芳香族炭化水素等が挙げ
られる。これらの有機性分散媒は、通常沸点が30〜350
℃の範囲のものが使用される。
The oil component constituting the water-in-oil swellable emulsion is an organic dispersion medium, and examples thereof include saturated linear hydrocarbons, branched saturated hydrocarbons, alicyclic hydrocarbons, and aromatic hydrocarbons. These organic dispersion media usually have a boiling point of 30 to 350.
Those in the range of ° C are used.

また、上記油中水型膨潤性エマルジョンには、通常、
界面活性剤が含まれる。乳化させ、油中水型のエマルジ
ョンを形成、これを安定に保持する目的でgriffinのHLB
(以下、単にHLBと記す。)で3〜7、好ましくは4〜
6の界面活性剤を用いる。具体例としては、ソルビタン
モノエステル類が挙げられる。
In addition, the water-in-oil swellable emulsion usually contains
Surfactants are included. It emulsifies to form a water-in-oil emulsion, and Griffin's HLB for the purpose of keeping it stable
(Hereinafter simply referred to as HLB) 3 to 7, preferably 4 to 7
The surfactant of No. 6 is used. Specific examples include sorbitan monoesters.

本発明の方法によれば油層の調整は、油中水型水膨潤
性重合体エマルジョンを水攻法で用いる水に添加して、
注入井または産生井より注入し、水膨潤性重合体により
油層中の高浸透率層およびフラクチャー等の水の通り易
い層を詰めることにより行なわれる。
According to the method of the present invention, the oil layer is adjusted by adding a water-in-oil water-swellable polymer emulsion to water used in a waterflooding method,
Injection is performed from an injection well or a production well, and a water-swellable polymer is used to pack a high permeability layer in an oil layer and a water-permeable layer such as a fracture.

油層中に注入された水膨潤性重合体の多くは、高浸透
率層およびフラクチャー等の水の通り易い層に優先的に
注入され、吸着、トラップ等により、その層内で保持さ
れ、従って、その層の水路は狭くなりその後注入される
水および水溶液を流れ難くする。一方、水の通り難い低
浸透率の層には水膨潤性重合体が侵入し難く、その結果
として、これまで水が流れ難かった低浸透率層に注入水
および水溶液が流れその部分の原油を回収する速度を速
めることになる。
Most of the water-swellable polymer injected into the oil layer is preferentially injected into a water-permeable layer such as a high-permeability layer and a fracture, and is retained in the layer by adsorption, trap, and the like. The channel in that layer is narrowed, making it harder for the water and aqueous solution subsequently injected to flow. On the other hand, the water-swellable polymer hardly penetrates into the low-permeability layer that is difficult to pass through water, and as a result, the injection water and the aqueous solution flow into the low-permeability layer where water has hardly flowed so far, and the crude oil in that part is removed. The speed of collection will be increased.

油層に注入する油中水型水膨潤性エマルジョンは、直
接注入水に添加するか、または該エマルジョンより油お
よび水分を除去して得られた水膨潤性重合体を注入水に
溶解して使用する。使用濃度は水膨潤性重合体として通
常0.001〜1%、好ましくは0.01〜0.1%である。
The water-in-oil type water-swellable emulsion to be injected into the oil layer is used by directly adding to the injection water or dissolving the water-swellable polymer obtained by removing oil and water from the emulsion into the injection water. . The concentration used is usually 0.001 to 1%, preferably 0.01 to 0.1%, as a water-swellable polymer.

1%を越える濃度での使用は、注入圧が高くなり過ぎ
て油層にダメージを与える。また、0.001%に満たない
濃度での使用は、処理に時間がかかり過ぎて不経済にな
る。
Use at concentrations above 1% will damage the oil layer due to too high injection pressure. Also, use at a concentration of less than 0.001% is uneconomical due to the time required for processing.

水膨潤性重合体の水中での水膨潤率は水に溶けている
塩の種類およびその濃度、pH等により異なる。高塩濃
度、低pH、および高pHでは水膨潤率が小さく、水膨潤性
重合体の大きさが小さくなり、また低塩濃度およびpH=
7付近では水膨潤性重合体の大きさが大きくなる。この
性質を利用し水膨潤性重合体を油層中に注入する際、予
めサンプリングして測定した地層の浸透率に合わせて水
溶液の塩濃度、および/またはpHを調整することによ
り、水膨潤性重合体の大きさを調整するとさらに効果的
に水膨潤性重合体を高浸透率層に注入することができ
る。
The water swelling ratio of water-swellable polymer in water varies depending on the type of salt dissolved in water, its concentration, pH and the like. At high salt concentration, low pH and high pH, the water swelling ratio is small, the size of the water swellable polymer is small, and low salt concentration and pH =
In the vicinity of 7, the size of the water-swellable polymer increases. Utilizing this property, when injecting the water-swellable polymer into the oil layer, the salt concentration and / or the pH of the aqueous solution are adjusted according to the permeability of the formation, which has been sampled and measured in advance, to thereby obtain the water-swellable polymer. By adjusting the size of the coalescence, the water-swellable polymer can be more effectively injected into the high-permeability layer.

[効果] 油層の高浸透率層、フラクチャーに注入された水膨潤
性重合体は油層中に保持され、その後注入する注入水に
対する浸透率を低くし、注入水を通り難くし、これによ
り油層全体の浸透率が均一化される。また、注入水のpH
および/または塩濃度を変えることで保持された水膨潤
性重合体の大きさを変え、浸透率を変えることができ、
油層全体の浸透率はさらに均一となる。
[Effect] The water-swellable polymer injected into the high-permeability layer and the fracture of the oil layer is retained in the oil layer, and thereafter, the permeability of the injected water to the injected water is lowered, thereby making it difficult for the water to flow through the injected water. Is made uniform. Also, the injection water pH
And / or changing the salt concentration can change the size of the retained water-swellable polymer and change the permeability,
The permeability of the entire oil layer becomes more uniform.

具体例として、水膨潤性重合体の粒径の比較的小さく
なる塩濃度あるいはpHで、高浸透率層に水膨潤性重合体
を十分に保持させた後、注入水の塩濃度を徐々に低下さ
せるか、あるいはpH値を7に近づけることにより層中に
保持された水膨潤性重合体の粒径を増加させ、浸透率を
より効果的に低下させることが可能である。
As a specific example, at a salt concentration or pH at which the particle size of the water-swellable polymer is relatively small, after sufficiently retaining the water-swellable polymer in the high-permeability layer, the salt concentration of the injection water is gradually reduced. Alternatively, by bringing the pH value closer to 7, it is possible to increase the particle size of the water-swellable polymer retained in the layer and more effectively reduce the permeability.

この方法で処理された油層はクエン酸アルミニウム法
で処理された油層に比べて高浸透率層の処理割合が高
く、より均一な浸透率層となる。
The oil layer treated by this method has a higher treatment rate of the high permeability layer than the oil layer treated by the aluminum citrate method, resulting in a more uniform permeability layer.

[実施例] 以下に、実施例を挙げて本発明をさらに説明するが、
本発明は下記の例によって限定されるものではない。
EXAMPLES Hereinafter, the present invention will be further described with reference to Examples.
The present invention is not limited by the following examples.

実施例1 ビニルモノマーとしてアクリルアミド(AMD)、アク
リル酸ソーダ(AAC−Na)、ジメチルアミノエチルメタ
アクリレートメチルクロライド4級塩(DMQ)の各々単
独の50%水溶液、およびAMDとAAC−Naとの等モル混合物
の50%水溶液をそれぞれ683g、架橋剤としてメチレンビ
スアクリルアミド0.15g、界面活性剤としてソルビタン
モノオレート18gを使用し、パラフィン64重量%、ナフ
テン35重量%、芳香族炭化水素1重量%の割合から成る
有機分散媒240g中で乳化し重合した油中水型水膨潤性重
合体エマルジョンを01wt%NaCl水溶液に溶解して500ppm
の水膨潤性重合体水溶液(4種類)を調製した。これら
溶液をpH=4に調製し直径1インチ、長さ3インチのBe
rea Sand Stoneのコア(Core)に流速2m/dayで注入し
て抵抗ファクターを調べた。さらにその後0.1%NaCl溶
液を注入して浸透率を測定し、浸透率低下係数を調べ
た。その結果を表−1に示す。
Example 1 Aqueous 50% aqueous solutions of acrylamide (AMD), sodium acrylate (AAC-Na), and dimethylaminoethyl methacrylate methyl chloride quaternary salt (DMQ) alone as vinyl monomers, and a mixture of AMD and AAC-Na Using 683 g of a 50% aqueous solution of the molar mixture, 0.15 g of methylene bisacrylamide as a cross-linking agent and 18 g of sorbitan monooleate as a surfactant, a ratio of paraffin 64% by weight, naphthene 35% by weight, and aromatic hydrocarbon 1% by weight. A water-in-oil type water-swellable polymer emulsion emulsified and polymerized in 240 g of an organic dispersion medium consisting of
Of water-swellable polymer aqueous solutions (4 types) were prepared. These solutions were adjusted to pH = 4 and a 1 inch diameter, 3 inch long Be
The resistance factor was investigated by injecting into the core of rea Sand Stone at a flow rate of 2 m / day. Thereafter, a 0.1% NaCl solution was injected to measure the permeability, and the permeability reduction coefficient was examined. Table 1 shows the results.

実施例2 実施例1で得られたアクリル酸ソーダの油中水型水膨
潤性重合体エマルジョンを0.1%NaCl溶液に溶解し、水
膨潤性重合体の濃度500ppmの溶液を調製した。この溶液
のpHを3、5および7に調製してBerea Sand Stoneの
コアに注入してその抵抗ファクターを調べた。結果を表
−2に示す。
Example 2 A water-in-oil type water-swellable polymer emulsion of sodium acrylate obtained in Example 1 was dissolved in a 0.1% NaCl solution to prepare a solution having a concentration of 500 ppm of the water-swellable polymer. The pH of this solution was adjusted to 3, 5 and 7 and injected into the core of Berea Sand Stone to examine its resistance factor. Table 2 shows the results.

実施例3 実施例1で得られたDMQの油中水型水膨潤性重合体エ
マルジョンを0.1%NaCl溶液に溶解し、水膨潤性重合体
の濃度500ppmの溶液を調製した。この溶液を700mdのBer
ea Sand Stoneに注入し、その後、濃度の異なるNaCl
溶液を注入して浸透率低下係数を調べた結果を表−3に
示す。
Example 3 The water-in-oil type water-swellable polymer emulsion of DMQ obtained in Example 1 was dissolved in a 0.1% NaCl solution to prepare a solution having a concentration of 500 ppm of the water-swellable polymer. Transfer this solution to 700 md Ber
ea Sand Stone, then add different concentrations of NaCl
Table 3 shows the results of examining the permeability reduction coefficient by injecting the solution.

実施例4 実施例3で調製した水膨潤性重合体溶液を、並列につ
ないだ浸透率の異なる2本のBereaSand Stone(コア)
に注入した時の両コアへの流入比、及びその後0.1%NaC
l水を注入した時の注入比をクエン酸アルミ法による場
合及びクロム法による場合と比較した結果を表−4及び
表−5に示す。
Example 4 The water-swellable polymer solution prepared in Example 3 was connected in parallel to two BereaSand Stones (cores) having different permeability.
Ratio to both cores when injected into the core, and then 0.1% NaC
Tables 4 and 5 show the results of comparison of the injection ratio when water was injected with the aluminum citrate method and the chromium method.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 坪井 彦忠 千葉県茂原市東郷1900番地 三井サイア ナミッド株式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Hikotada Tsuboi 1900 Togo, Togo, Mobara-shi, Chiba Mitsui Saia Namid Co., Ltd.

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】油中水型膨潤性重合体エマルジョンを直接
使用するか、または該エマルジョンより油および水分を
除去して得られる水膨潤性重合体を使用することを特徴
とする油層調整方法。
An oil layer preparation method comprising directly using a water-in-oil swellable polymer emulsion or using a water-swellable polymer obtained by removing oil and water from the emulsion.
【請求項2】油中水型膨潤性重合体エマルジョンが水溶
性ビニル単量体の1種または2種以上、もしくは水溶性
ビニル単量体の1種以上と、水溶性ビニル単量体と共重
合可能なビニル単量体の1種以上、および水溶性ビニル
モノマーと共重合可能な架橋剤を含む水溶液を、界面活
性剤を含む有機分散媒中に注入し乳化させた後、ラジカ
ル重合させて得られるものであることを特徴とする特許
請求の範囲第1項に記載の油層調整方法。
2. A water-in-oil type swellable polymer emulsion comprising one or more water-soluble vinyl monomers, or one or more water-soluble vinyl monomers, and a water-soluble vinyl monomer. An aqueous solution containing one or more polymerizable vinyl monomers and a crosslinking agent copolymerizable with a water-soluble vinyl monomer is injected into an organic dispersion medium containing a surfactant, emulsified, and then radically polymerized. The oil layer adjusting method according to claim 1, wherein the oil layer is obtained.
【請求項3】水膨潤性重合体としてアクリルアミド重合
体、アクリルアミドと他のモノマーとの共重合体、アク
リル酸およびその塩の重合体、およびカチオン基含有単
量体の重合体の少なくとも1種から選ばれる架橋体を使
用することを特徴とする特許請求の範囲第1項に記載の
油層調整方法。
3. A water swellable polymer comprising at least one of an acrylamide polymer, a copolymer of acrylamide and another monomer, a polymer of acrylic acid and a salt thereof, and a polymer of a cationic group-containing monomer. The method for adjusting an oil layer according to claim 1, wherein a selected crosslinked product is used.
【請求項4】水膨潤性重合体エマルジョンを油層に注入
する際に、水膨潤性重合体を含む注入水のpHおよび/ま
たは塩濃度を変えることにより水膨潤性重合体粒子の大
きさを調整して、処理しようとする地層に水膨潤性重合
体を注入することを特徴とする特許請求の範囲第1項、
第2項または第3項に記載の油層調整方法。
4. The size of the water-swellable polymer particles is adjusted by changing the pH and / or salt concentration of the water containing the water-swellable polymer when the water-swellable polymer emulsion is injected into the oil layer. Claim 1, wherein the water swellable polymer is injected into the formation to be treated.
Item 4. The oil layer adjusting method according to Item 2 or 3.
【請求項5】注入され地下に保持された水膨潤性重合体
を、pHおよび/または塩濃度を調整した注入水で処理し
膨脹あるいは縮小させて、浸透率を変えることを特徴と
する特許請求の範囲第1項、第2項または第3項に記載
の油層調整方法。
5. The method according to claim 1, wherein the water-swellable polymer injected and held underground is expanded or reduced by treating it with injection water whose pH and / or salt concentration has been adjusted to change the permeability. Item 4. The oil layer adjusting method according to any one of Items 1, 2 and 3.
JP14801188A 1988-06-17 1988-06-17 Oil layer preparation method using water-in-oil swellable emulsion Expired - Fee Related JP2663145B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14801188A JP2663145B2 (en) 1988-06-17 1988-06-17 Oil layer preparation method using water-in-oil swellable emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14801188A JP2663145B2 (en) 1988-06-17 1988-06-17 Oil layer preparation method using water-in-oil swellable emulsion

Publications (2)

Publication Number Publication Date
JPH01318686A JPH01318686A (en) 1989-12-25
JP2663145B2 true JP2663145B2 (en) 1997-10-15

Family

ID=15443108

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14801188A Expired - Fee Related JP2663145B2 (en) 1988-06-17 1988-06-17 Oil layer preparation method using water-in-oil swellable emulsion

Country Status (1)

Country Link
JP (1) JP2663145B2 (en)

Also Published As

Publication number Publication date
JPH01318686A (en) 1989-12-25

Similar Documents

Publication Publication Date Title
CN105504158B (en) Intelligent gel particles capable of being crosslinked again under stratum condition and preparation method and application of intelligent gel particles
US7182136B2 (en) Methods of reducing water permeability for acidizing a subterranean formation
US8263533B2 (en) Method of treating underground formations or cavities by microgels
RU2256071C2 (en) Composition and method for withdrawal of hydrocarbon fluids from underground layer
US8680028B2 (en) Method for the treatment of rock formations and novel polyampholytes
JPS6112706A (en) Manufacture of reverse microlatex of water-soluble copolymer
US20070039732A1 (en) Methods and compositions for improving hydrocarbon recovery by water flood intervention
WO2019183390A1 (en) Preformed particle gel for enhanced oil recovery
GB2524232A (en) Process
US3380529A (en) Method of acidizing a fluid-bearing formation
WO2015113577A1 (en) Method to increase the viscosity of hydrogels by crosslinking a copolymer in the presence of dissolved salt
GB2262117A (en) Conformance control in underground reservoirs
CA3061408A1 (en) Microparticles and method for modifying the permeability of a reservoir zone
US5701955A (en) Downhole fluid control processes
AU2014270747B2 (en) Temperature-stable, electrolytic hydrogel and method for stimulating crude oil and natural gas deposits
WO2019025810A1 (en) Crosslinked polymer microparticles for use in conformance control
JP2663145B2 (en) Oil layer preparation method using water-in-oil swellable emulsion
US11149186B2 (en) Method for enhanced oil recovery by injecting an aqueous polymeric composition containing microgels
CN107646065A (en) Suppress water penetration to the method in the extraction well of the hydrocarbon fluid from subsurface reservoir
WO1995026455A1 (en) Downhole fluid control processes
CA1042648A (en) Polymer waterflooding by controlling water hardness
JP2796867B2 (en) Petroleum recovery with cationic and anionic polymers
CN109689835B (en) Method for inhibiting water penetration in extraction wells of hydrocarbon oils from subterranean reservoirs
US20230323190A1 (en) Method for controlling the migration of formation fines
US20210171820A1 (en) Delayed Gelation Polymer System

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R370 Written measure of declining of transfer procedure

Free format text: JAPANESE INTERMEDIATE CODE: R370

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

LAPS Cancellation because of no payment of annual fees