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CN106883832A - A kind of controllable diverting agent of environment-friendly type and preparation method thereof - Google Patents

A kind of controllable diverting agent of environment-friendly type and preparation method thereof Download PDF

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CN106883832A
CN106883832A CN201710213054.XA CN201710213054A CN106883832A CN 106883832 A CN106883832 A CN 106883832A CN 201710213054 A CN201710213054 A CN 201710213054A CN 106883832 A CN106883832 A CN 106883832A
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ammonium persulfate
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吴仲岿
王文轩
林晨
张海丽
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Wuhan University of Technology WUT
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    • C08J2329/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
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    • C08J2405/00Characterised by the use of polysaccharides or of their derivatives not provided for in groups C08J2401/00 or C08J2403/00
    • C08J2405/04Alginic acid; Derivatives thereof
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2489/00Characterised by the use of proteins; Derivatives thereof

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Abstract

本发明提供了一种环保型可控暂堵剂及其制备方法,该暂堵剂由有机环保的合成原液和无机的功能试剂混合而成,其中合成原液是由聚乙烯醇、可溶性淀粉、明胶、海藻酸钠、过硫酸铵与水混合搅拌得到,辅助试剂由无水氯化钙、无水硫酸钠、乙二胺四乙酸二钠、四硼酸钠、过硫酸铵组成。本发明暂堵剂的制备方法是:采用溶液聚合法制备合成原液,然后加入助凝胶试剂,在骨架材料上实现一次凝胶材料的完美结合,再次加入二次凝胶试剂(主凝胶剂),制备得到目标产品。本发明研制的产品封堵效果好、封堵时间可控、返排性能好、无污染、生产工序少、成本低,适用于工业化生产。The invention provides an environment-friendly controllable temporary plugging agent and a preparation method thereof. The temporary plugging agent is formed by mixing an organic and environmentally friendly synthetic stock solution and an inorganic functional reagent, wherein the synthetic stock solution is composed of polyvinyl alcohol, soluble starch, gelatin , sodium alginate, ammonium persulfate and water are mixed and stirred, and the auxiliary reagent is composed of anhydrous calcium chloride, anhydrous sodium sulfate, disodium edetate, sodium tetraborate and ammonium persulfate. The preparation method of the temporary plugging agent of the present invention is: adopt the solution polymerization method to prepare synthetic stock solution, then add gelation aid agent, realize the perfect combination of primary gel material on skeleton material, add secondary gel agent (primary gel agent again) ), to prepare the target product. The product developed by the invention has good plugging effect, controllable plugging time, good flowback performance, no pollution, few production procedures and low cost, and is suitable for industrialized production.

Description

一种环保型可控暂堵剂及其制备方法A kind of environment-friendly controllable temporary plugging agent and preparation method thereof

技术领域technical field

本发明属于页岩气开采技术领域,具体涉及一种环保型可控暂堵剂及其制备方法。The invention belongs to the technical field of shale gas exploitation, and in particular relates to an environment-friendly controllable temporary plugging agent and a preparation method thereof.

背景技术Background technique

页岩气是一种特殊的非常规天然气,赋存于泥岩或页岩中,具有自生自储、无气水界面、大面积连续成藏、低孔、低渗等特征,一般无自然产能或低产,需要大型水力压裂和水平井技术才能进行经济开采,单井生产周期长。美国作为世界上页岩气资源勘探开发最早的国家,已在北美地区形成成熟的评价方法和勘探开发技术,实现了页岩气的工业开发,从理论和技术上证实了页岩气资源有效开发的可能性。因此加快页岩气资源勘探开发,已成为世界主要页岩气资源大国和地区的共同而热切的愿望。Shale gas is a special kind of unconventional natural gas, which occurs in mudstone or shale. It has the characteristics of self-generation and self-storage, no gas-water interface, large-area continuous accumulation, low porosity, and low permeability. Generally, it has no natural productivity or Low production requires large-scale hydraulic fracturing and horizontal well technology for economical production, and the production cycle of a single well is long. As the earliest country in the world for the exploration and development of shale gas resources, the United States has formed mature evaluation methods and exploration and development technologies in North America, realized the industrial development of shale gas, and proved the effective development of shale gas resources theoretically and technically possibility. Therefore, accelerating the exploration and development of shale gas resources has become the common and eager desire of the world's major shale gas resource countries and regions.

页岩气开发技术发展大致可分五个基本阶段(以美国为例):The development of shale gas development technology can be roughly divided into five basic stages (taking the United States as an example):

1 钻直井,进行泡沫压裂(大液量、大排量6.4方/分,要加砂;传统压裂液);1 Drill vertical wells and perform foam fracturing (large fluid volume, large displacement of 6.4 cubic meters per minute, with sand added; traditional fracturing fluid);

2 钻直井,大型水力压裂技术(大液量、大排量6.4方/分,要加砂29%;传统压裂液);2 Drilling vertical wells, large-scale hydraulic fracturing technology (large fluid volume, large displacement 6.4 cubic meters per minute, 29% sand required; traditional fracturing fluid);

3 钻直井,清水压裂或清水加砂压裂(加沙2.66~4.8%),可比凝胶压裂节约成本50%~60%,从1998年至今一直是垂直井的压裂方式;3 Drilling vertical wells, clean water fracturing or clean water and sand fracturing (Gaza 2.66-4.8%), can save 50%-60% of the cost compared with gel fracturing, and it has been the vertical well fracturing method since 1998;

4 1997年,最初由凝胶压裂的井在能量衰竭后,用清水进行二次压裂,可采储量增加了60%,二次压裂技术至2006年仍较为常见;4. In 1997, after the energy failure of the well initially fractured by gel, the recoverable reserves increased by 60% after secondary fracturing with clean water. The secondary fracturing technology was still relatively common until 2006;

5 钻水平井,水平段长304.8~1066.8m,分段清水和砂进行压裂,此技术开始于2003年,2006年“同步压裂”技术产生。5 Drill horizontal wells with a horizontal section length of 304.8-1066.8m, and perform fracturing with clean water and sand in stages. This technology began in 2003, and the "synchronous fracturing" technology was produced in 2006.

但总的说来,现在并不具备对我国页岩气进行工业化开采的技术条件,主要体现在以下方面:But generally speaking, the technical conditions for industrialized exploitation of shale gas in my country are not available now, which is mainly reflected in the following aspects:

⑴我国页岩地质条件与国外成功开发的页岩储层的地质条件有较大差异,国外有效技术难以直接应用;(1) The shale geological conditions in my country are quite different from those of shale reservoirs successfully developed in foreign countries, and it is difficult to directly apply foreign effective technologies;

⑵我们对国外成熟技术还未完全掌握;⑵We have not fully grasped the mature foreign technology;

⑶我国自然环境条件对国外现技术不适应;(3) my country's natural environmental conditions are not suitable for foreign existing technologies;

⑷国外有效技术本身还存在很多需要改进和发展的问题。(4) There are still many problems that need to be improved and developed in foreign effective technologies.

针对以上问题,国内外提出了转向压裂工艺。转向压裂分为缝内转向压裂和缝间转向压裂两种。其核心目的就是提高净压力,迫使裂缝转向,增大储层改造体积。In view of the above problems, the steering fracturing process has been proposed at home and abroad. There are two types of diversion fracturing: intra-fracture diversion fracturing and inter-fracture diversion fracturing. Its core purpose is to increase the net pressure, force fractures to divert, and increase the volume of reservoir stimulation.

缝内转向:根据流体向阻力最小方向流动的原则,暂堵剂颗粒首先进入高渗层,对地层中的大孔道、原生裂缝、水力裂缝壁面以及炮眼处产生“滤饼桥堵”效应,使得压力升高,迫使裂缝转向,增大储层改造体积。In-fracture diversion: According to the principle that the fluid flows in the direction of the least resistance, the temporary plugging agent particles first enter the high-permeability layer, and produce a "filter cake bridge plugging" effect on the large pores, primary fractures, hydraulic fracture walls and blastholes in the formation, making The pressure rises, forcing the fractures to divert and increasing the stimulated volume of the reservoir.

缝间转向:通过注入混合暂堵型材料(纤维+大粒径暂堵剂-可降解)的压裂液和支撑剂,在先压开裂缝口处形成暂时封堵,井底压力升高迫使液体转向,最终所有射孔簇按破裂压力由低到高都依次改造。Inter-fracture diversion: By injecting fracturing fluid and proppant mixed with temporary plugging materials (fiber + large particle size temporary plugging agent - degradable), a temporary plug is formed at the opening of the first fracture, and the bottom hole pressure increases to force The liquid turns, and finally all the perforation clusters are reformed sequentially according to the fracture pressure from low to high.

但是目前国内一般的暂堵剂都存在很多问题:1、封堵时间单一,不能有效的随着地貌环境与施工需要的变化而变化;2、暂堵剂封堵效果不理想;3、暂堵剂完成封堵后,在返排溶液中残留固体悬浮物,使得返排液粘度变大,不易返排,部分暂堵剂排出后还会对地质环境造成危害;4、暂堵剂不易加工,强度不足,耐压性能差等相关施工工艺无法达标。因此,开发一种新型环保可控的暂堵剂显得尤为重要。However, at present, there are many problems with the general temporary plugging agents in China: 1. The plugging time is single, and cannot effectively change with the changes in the landform environment and construction needs; 2. The plugging effect of the temporary plugging agent is not ideal; 3. The temporary plugging After the plugging agent is completed, solid suspended matter remains in the flowback solution, which makes the flowback liquid more viscous and difficult to flow back. Some temporary plugging agents will also cause harm to the geological environment after being discharged; 4. The temporary plugging agent is not easy to process. Insufficient strength, poor pressure resistance and other related construction techniques cannot meet the standards. Therefore, it is particularly important to develop a new type of environmentally friendly and controllable temporary plugging agent.

发明内容Contents of the invention

本发明的目的在于提供一种承压能力高、密度小、易加工的环保型暂堵剂,相比于现有同类产品,其具有封堵效果优异、返排效果好、封堵时间可控的优点,且成本低廉,适合工业化生产。为实现上述目的,本发明所采用的技术方案如下:The purpose of the present invention is to provide an environmentally friendly temporary plugging agent with high pressure bearing capacity, low density and easy processing. Compared with existing similar products, it has excellent plugging effect, good flowback effect, and controllable plugging time Advantages, and low cost, suitable for industrial production. In order to achieve the above object, the technical scheme adopted in the present invention is as follows:

一种环保型可控暂堵剂,由合成原液和凝胶剂复配而成,所述合成原液由聚乙烯醇(PVA)、可溶性淀粉、明胶、海藻酸钠、过硫酸铵与水混合而成,所述凝胶剂包括助凝胶剂和主凝胶剂,其中助凝胶剂由无水氯化钙、无水硫酸钠、乙二胺四乙酸二钠(EDTA-2Na)复配而成,主凝胶剂由四硼酸钠、过硫酸铵复配而成。An environment-friendly controllable temporary plugging agent, which is compounded by a synthetic stock solution and a gel agent, and the synthetic stock solution is prepared by mixing polyvinyl alcohol (PVA), soluble starch, gelatin, sodium alginate, ammonium persulfate and water The gelling agent includes a gelling agent and a main gelling agent, wherein the gelling agent is compounded by anhydrous calcium chloride, anhydrous sodium sulfate, and disodium ethylenediaminetetraacetic acid (EDTA-2Na). The main gelling agent is compounded by sodium tetraborate and ammonium persulfate.

上述方案中,所述合成原液中聚乙烯醇的质量分数为3-9%,可溶性淀粉的质量分数为2-6%,明胶的质量分数为1-6%,水的质量分数为70%,余量为海藻酸钠和过硫酸铵混合物。合成原液的配制遵循少量多次均一的原则。In the above scheme, the mass fraction of polyvinyl alcohol in the synthetic stock solution is 3-9%, the mass fraction of soluble starch is 2-6%, the mass fraction of gelatin is 1-6%, and the mass fraction of water is 70%, The balance is a mixture of sodium alginate and ammonium persulfate. The preparation of the synthetic stock solution follows the principle of uniformity in small quantities and multiple times.

上述方案中,所述助凝胶剂中无水氯化钙、无水硫酸钠、乙二胺四乙酸二钠的质量比为1-2:1-2:1-4。In the above scheme, the mass ratio of anhydrous calcium chloride, anhydrous sodium sulfate, and disodium edetate in the gelling aid is 1-2:1-2:1-4.

上述方案中,所述主凝胶剂中四硼酸钠、过硫酸铵的质量比为1-4:2。In the above scheme, the mass ratio of sodium tetraborate and ammonium persulfate in the main gelling agent is 1-4:2.

上述方案中,所述暂堵剂由合成原液、助凝胶剂、主凝胶剂按照100:3-8:3-6的质量比混合而成。整个凝胶化过程涉及到二次相互穿透凝胶化以及缓蚀解凝胶化。In the above scheme, the temporary plugging agent is formed by mixing the synthetic stock solution, the co-gelling agent, and the main gelling agent in a mass ratio of 100:3-8:3-6. The whole gelation process involves secondary interpenetrating gelation and corrosion-inhibiting degelation.

上述环保型可控暂堵剂的制备方法,包括以下步骤:(a)按配比准确称量聚乙烯醇、可溶性淀粉、明胶、海藻酸钠、过硫酸铵与水,混合溶解得到合成原液;(b)按配比将无水氯化钙、无水硫酸钠、乙二胺四乙酸二钠混合复配成助凝胶剂,将四硼酸钠、过硫酸铵复配成主凝胶剂备用;(c)将助凝胶剂加入到均一的合成原液中,反应一段时间后将主凝胶剂加入到混合溶液中,静置冷却后热压烘干即得环保型可控暂堵剂。The preparation method of the above-mentioned environment-friendly controllable temporary plugging agent comprises the following steps: (a) accurately weighing polyvinyl alcohol, soluble starch, gelatin, sodium alginate, ammonium persulfate and water according to the proportion, mixing and dissolving to obtain a synthetic stock solution; b) According to the ratio, anhydrous calcium chloride, anhydrous sodium sulfate, and disodium edetate are mixed and compounded to form a gelling aid, and sodium tetraborate and ammonium persulfate are compounded to form a main gelling agent for later use; ( c) Add the co-gelling agent into the homogeneous synthesis stock solution, add the main gelling agent into the mixed solution after a period of reaction, let it stand for cooling, and then heat-press and dry to obtain an environment-friendly and controllable temporary plugging agent.

本发明中使用的合成原液是由聚乙烯醇、可溶性淀粉、明胶、海藻酸钠、过硫酸铵等构成的均一复合组分溶液。从稳定性、黏性和价格等方面综合考虑,选用的凝胶化试剂包括无水氯化钙、无水硫酸钠、乙二胺四乙酸二钠以及过硫酸铵、四硼酸钠等。The synthetic stock solution used in the present invention is a uniform composite component solution composed of polyvinyl alcohol, soluble starch, gelatin, sodium alginate, ammonium persulfate and the like. In consideration of stability, viscosity and price, the selected gelling reagents include anhydrous calcium chloride, anhydrous sodium sulfate, disodium edetate, ammonium persulfate, sodium tetraborate, etc.

本发明采用两次凝胶成型相互穿透,包裹缓蚀剂、降粘剂等添加剂制备而成。由于明胶的溶解效果比较恰当且本身是两性物质,暂堵剂骨架支撑体首选明胶;可溶性淀粉粘度比较大,具有较好的稳定性与粘结性且能与明胶共混,作为粘结剂;EDTA-2Na做络合剂,与无水氯化钙和明胶反应,使得明胶与氯化物接触变性,在低温下缓慢溶于水,为后续生产提供了良好的条件;无水氯化钙与无水硫酸钠作为一次凝胶剂(助凝胶剂)用来稳定EDTA-2Na,使其不至于和明胶过快反应,保证溶解速度;硼砂(主凝胶剂)与PVA发生二次凝胶,PVA在原液制备中与明胶良好的共混缔合,在后期生产中将原液缓慢均匀的倒入硼砂的水溶液时,与硼砂迅速凝胶化,生成主产物暂堵剂。The invention adopts two gel formings to penetrate each other, and is prepared by wrapping additives such as corrosion inhibitors and viscosity reducers. Since the dissolution effect of gelatin is relatively appropriate and it is an amphoteric substance, gelatin is the first choice for the skeleton support of the temporary plugging agent; soluble starch has a relatively high viscosity, has good stability and cohesiveness, and can be blended with gelatin as a binder; EDTA-2Na is used as a complexing agent, reacts with anhydrous calcium chloride and gelatin, makes gelatin denatured in contact with chloride, slowly dissolves in water at low temperature, and provides good conditions for subsequent production; anhydrous calcium chloride and anhydrous Sodium sulfate water is used as a primary gelling agent (gelling aid) to stabilize EDTA-2Na so that it does not react too quickly with gelatin to ensure the dissolution rate; borax (primary gelling agent) and PVA undergo secondary gelation, PVA is well blended and associated with gelatin in the preparation of the stock solution, and when the stock solution is slowly and evenly poured into the aqueous solution of borax in the later stage of production, it will quickly gel with borax to form the main product temporary plugging agent.

与现有技术相比,本发明具有以下有益效果:(1)制备暂堵剂所用的原料海藻酸钠、可溶性淀粉、明胶等均具有较好的生物相容性,原料来源环保,暂堵剂可完全溶于水中并随返排液及时排出,不会遗留在地层中,对环境不会造成伤害;(2)封堵效果良好,返排效果优秀,溶解后溶液粘度低至5.3204mPa·s,不足50mPa·s;(3)封堵时间可控,不同配比的凝胶剂配制而成的暂堵剂溶解时间不同;(4)制备工艺简单,原料成本低,适合工业化生产。Compared with the prior art, the present invention has the following beneficial effects: (1) The raw materials sodium alginate, soluble starch, gelatin, etc. used in the preparation of the temporary plugging agent all have good biocompatibility, and the sources of raw materials are environmentally friendly, and the temporary blocking agent It can be completely dissolved in water and discharged in time with the flowback liquid, will not be left in the formation, and will not cause harm to the environment; (2) The plugging effect is good, the flowback effect is excellent, and the viscosity of the solution after dissolution is as low as 5.3204mPa·s , less than 50mPa·s; (3) The plugging time is controllable, and the dissolution time of the temporary plugging agent prepared by different ratios of gels is different; (4) The preparation process is simple, the cost of raw materials is low, and it is suitable for industrial production.

附图说明Description of drawings

图1为本发明实施例1制备得到的暂堵剂对普通细砂的封堵性能曲线;Fig. 1 is the plugging performance curve of the temporary plugging agent prepared in Example 1 of the present invention to ordinary fine sand;

图2为本发明实施例1制备得到的暂堵剂对中砂的封堵性能曲线;Fig. 2 is the plugging performance curve of the temporary plugging agent prepared in Example 1 of the present invention for medium sand;

图3为本发明实施例1制备得到的暂堵剂对混砂A的封堵性能曲线;Fig. 3 is the plugging performance curve of the temporary plugging agent prepared in Example 1 of the present invention to sand mixing A;

图4为本发明实施例1制备得到的暂堵剂对粗砂的封堵性能曲线;Fig. 4 is the plugging performance curve of the temporary plugging agent prepared in Example 1 of the present invention to coarse sand;

图5为本发明实施例1制备得到的暂堵剂对混砂B的封堵性能曲线;Fig. 5 is the plugging performance curve of the temporary plugging agent prepared in Example 1 of the present invention to the mixed sand B;

图6为本发明实施例1制备得到的暂堵剂对混砂C的封堵性能曲线;Fig. 6 is the plugging performance curve of the temporary plugging agent prepared in Example 1 of the present invention to the mixed sand C;

图7为本发明实施例1制备得到的暂堵剂对混砂D的封堵性能曲线。Fig. 7 is the plugging performance curve of the temporary plugging agent prepared in Example 1 of the present invention for sand mixing D.

具体实施方式detailed description

为使本领域普通技术人员充分理解本发明的技术方案和有益效果,以下结合具体实施例进行进一步说明。In order to enable those skilled in the art to fully understand the technical solutions and beneficial effects of the present invention, further description will be given below in conjunction with specific examples.

实施例1Example 1

一种环保型可控暂堵剂,由合成原液与助、主凝胶剂复配而成。以质量份数计,合成原液由聚乙烯醇9份,可溶性淀粉3份,明胶6份,水70份,海藻酸钠和过硫酸铵共计12份组成;助凝胶剂由无水氯化钙1份、无水硫酸钠1份、EDTA-2Na 3份组成,主凝胶剂由四硼酸钠3份、过硫酸铵2份组成。制备时,首先按配比将聚乙烯醇、可溶性淀粉、明胶、海藻酸钠、过硫酸铵和水混合溶解得到均一的合成原液,接着将助凝胶剂加入到合成原液中反应10min左右,再加入主凝胶剂,待所需样品成型后停止反应,取出烘干待用。An environment-friendly controllable temporary plugging agent, which is compounded from synthetic stock solution and auxiliary and main gelling agents. In terms of parts by mass, the synthetic stock solution consists of 9 parts of polyvinyl alcohol, 3 parts of soluble starch, 6 parts of gelatin, 70 parts of water, 12 parts of sodium alginate and ammonium persulfate in total; the gelling aid is composed of anhydrous calcium chloride 1 part, 1 part of anhydrous sodium sulfate, 3 parts of EDTA-2Na, the main gelling agent is composed of 3 parts of sodium tetraborate and 2 parts of ammonium persulfate. When preparing, first mix and dissolve polyvinyl alcohol, soluble starch, gelatin, sodium alginate, ammonium persulfate and water according to the ratio to obtain a uniform synthetic stock solution, then add the gelling aid to the synthetic stock solution and react for about 10 minutes, then add The main gelling agent, stop the reaction after the desired sample is formed, take it out and dry it for later use.

实施例2Example 2

一种环保型可控暂堵剂,由合成原液与助、主凝胶剂复配而成。以质量份数计,合成原液由聚乙烯醇9份,可溶性淀粉3份,明胶6份,水70份,海藻酸钠和过硫酸铵共计12份组成;助凝胶剂由无水氯化钙2份、无水硫酸钠2份、EDTA-2Na 3份组成,主凝胶剂由四硼酸钠3份、过硫酸铵2份组成。制备时,首先按配比将聚乙烯醇、可溶性淀粉、明胶、海藻酸钠、过硫酸铵和水混合溶解得到均一的合成原液,接着将助凝胶剂加入到合成原液中反应10min左右,再加入主凝胶剂,待所需样品成型后停止反应,取出烘干待用。An environment-friendly controllable temporary plugging agent, which is compounded from synthetic stock solution and auxiliary and main gelling agents. In terms of parts by mass, the synthetic stock solution consists of 9 parts of polyvinyl alcohol, 3 parts of soluble starch, 6 parts of gelatin, 70 parts of water, 12 parts of sodium alginate and ammonium persulfate in total; the gelling aid is composed of anhydrous calcium chloride 2 parts, 2 parts of anhydrous sodium sulfate, 3 parts of EDTA-2Na, the main gelling agent is composed of 3 parts of sodium tetraborate and 2 parts of ammonium persulfate. When preparing, first mix and dissolve polyvinyl alcohol, soluble starch, gelatin, sodium alginate, ammonium persulfate and water according to the ratio to obtain a uniform synthetic stock solution, then add the gelling aid to the synthetic stock solution and react for about 10 minutes, then add The main gelling agent, stop the reaction after the desired sample is formed, take it out and dry it for later use.

实施例3Example 3

一种环保型可控暂堵剂,由合成原液与助、主凝胶剂复配而成。以质量份数计,合成原液由聚乙烯醇9份,可溶性淀粉3份,明胶6份,水70份,海藻酸钠和过硫酸铵共计12份组成;助凝胶剂由无水氯化钙2份、无水硫酸钠2份、EDTA-2Na 4份组成,主凝胶剂由四硼酸钠4份、过硫酸铵2份组成。制备时,首先按配比将聚乙烯醇、可溶性淀粉、明胶、海藻酸钠、过硫酸铵和水混合溶解得到均一的合成原液,接着将助凝胶剂加入到合成原液中反应10min左右,再加入主凝胶剂,待所需样品成型后停止反应,取出烘干待用。An environment-friendly controllable temporary plugging agent, which is compounded from synthetic stock solution and auxiliary and main gelling agents. In terms of parts by mass, the synthetic stock solution consists of 9 parts of polyvinyl alcohol, 3 parts of soluble starch, 6 parts of gelatin, 70 parts of water, 12 parts of sodium alginate and ammonium persulfate in total; the gelling aid is composed of anhydrous calcium chloride 2 parts, 2 parts of anhydrous sodium sulfate, 4 parts of EDTA-2Na, the main gelling agent is composed of 4 parts of sodium tetraborate and 2 parts of ammonium persulfate. When preparing, first mix and dissolve polyvinyl alcohol, soluble starch, gelatin, sodium alginate, ammonium persulfate and water according to the ratio to obtain a uniform synthetic stock solution, then add the gelling aid to the synthetic stock solution and react for about 10 minutes, then add The main gelling agent, stop the reaction after the desired sample is formed, take it out and dry it for later use.

为充分了解本发明实施例1制备得到的暂堵剂的相关性能,分别对其进行了相应的测试。In order to fully understand the relevant properties of the temporary plugging agent prepared in Example 1 of the present invention, corresponding tests were carried out respectively.

(1)粘度测试(1) Viscosity test

测试条件:仪器为NDJ-1型旋转式粘度计,1号转子,剪切速率为60转/分,系数为1。测试方法为:在实验室内取1.0g样品置于具塞广口瓶中,加入300ml水,在85℃恒温干燥烘箱中观察溶解情况。实验发现4小时后样品溶解,测得表观粘度为5.3204mPa·s,比室温下的自来水粘度1.0050mPa·s稍微大一点,说明本暂堵剂的返排性能十分优秀。Test conditions: the instrument is a NDJ-1 rotary viscometer, the No. 1 rotor, the shear rate is 60 rpm, and the coefficient is 1. The test method is as follows: take 1.0g sample in the laboratory, put it in a jar with a stopper, add 300ml of water, and observe the dissolution in a constant temperature drying oven at 85°C. The experiment found that the sample dissolved after 4 hours, and the measured apparent viscosity was 5.3204mPa·s, which was slightly higher than the viscosity of tap water at room temperature of 1.0050mPa·s, indicating that the flowback performance of this temporary plugging agent is very good.

(2)暂堵剂的岩心驱替实验(2) Core displacement experiment of temporary plugging agent

2.1 将0-2mm石英砂(细砂)填充到直径20cm、长度60cm的填砂管中,将上述制得的页岩气开采用环保型可控暂堵剂注入到岩心管中,将岩心驱替装置温度设定为85℃、8MPa,每30min观察记录滤失量,进一步考察暂堵剂的封堵能力,结果分别入图1和表1所示。2.1 Fill 0-2mm quartz sand (fine sand) into a sand-packing tube with a diameter of 20 cm and a length of 60 cm, inject the shale gas prepared above into the core tube with an environment-friendly controllable temporary plugging agent, and drive the core into the core tube. The temperature of the replacement device was set at 85°C and 8 MPa, and the fluid loss was observed and recorded every 30 minutes to further investigate the plugging capacity of the temporary plugging agent. The results are shown in Figure 1 and Table 1 respectively.

表1 页岩气开采用环保型可控暂堵剂对普通细砂的封堵性能Table 1. The plugging performance of ordinary fine sand by environment-friendly controllable temporary plugging agent in shale gas development

时间(h)time (h) 0.50.5 1.01.0 1.51.5 2.02.0 2.52.5 3.03.0 3.53.5 4.04.0 4.54.5 滤失量(ml)Filtration loss (ml) 33 00 00 00 00 00 00 00 100100

由表1和图1可见,实施例1制备的页岩气开采用环保型可控暂堵剂对粒径很小(0-1mm)的细砂封堵效果为100%,且在规定溶解时间后解堵,返排效果好。It can be seen from Table 1 and Figure 1 that the environmental-friendly controllable temporary plugging agent for shale gas development prepared in Example 1 has a 100% plugging effect on fine sand with a small particle size (0-1 mm), and the plugging effect is 100% within the specified dissolution time. After the blockage is removed, the flowback effect is good.

2.2 将平均粒径为2-5mm砂砾(中砂)填充到直径20cm、长度60cm的填砂管中,将上述制得的页岩气开采用环保型可控暂堵剂注入到岩心管中,将岩心驱替装置温度设定为85℃、8MPa,每30min观察记录滤失量,进一步考察暂堵剂的封堵能力,结果如表2和图2所示。2.2 Fill the gravel (medium sand) with an average particle size of 2-5 mm into a sand-packing tube with a diameter of 20 cm and a length of 60 cm, and inject the shale gas prepared above into the core tube with an environment-friendly controllable temporary plugging agent. Set the temperature of the core displacement device at 85°C and 8 MPa, observe and record the fluid loss every 30 minutes, and further investigate the plugging capacity of the temporary plugging agent. The results are shown in Table 2 and Figure 2.

表2 页岩气开采用环保型可控暂堵剂对中砂的封堵性能Table 2. Plugging performance of environment-friendly controllable temporary plugging agent for medium sand in shale gas development

时间(h)time (h) 0.50.5 1.01.0 1.51.5 2.02.0 2.52.5 3.03.0 3.53.5 4.04.0 4.54.5 滤失量(ml)Filtration loss (ml) 100100 0.20.2 0.20.2 00 00 00 00 00 100100

由表2和图2可见,页岩气开采用环保型可控暂堵剂对粒径一般(1-3mm)中砂的封堵在前30min内样品溶胀前封堵不太理想,溶胀完成后封堵率为100%,且在规定溶解时间后解堵,返排效果好。It can be seen from Table 2 and Figure 2 that the use of environmentally friendly and controllable temporary plugging agents in shale gas development is not ideal for plugging medium-sized (1-3mm) medium sand in the first 30 minutes before the sample swells. The plugging rate is 100%, and the plugging is removed after the specified dissolution time, and the flowback effect is good.

2.3 将细砂与细砂混合(混砂A)填充到直径20cm、长度60cm的填砂管中,将上述制得的页岩气开采用环保型可控暂堵剂注入到岩心管中,将岩心驱替装置温度设定为85℃、8MPa,每30min观察记录滤失量,进一步考察暂堵剂的封堵能力,结果如表3何、图3所示。2.3 Fill fine sand with fine sand (mixed sand A) into a sand-packing tube with a diameter of 20 cm and a length of 60 cm, and inject the shale gas developed above into the core tube with an environmentally friendly and controllable temporary plugging agent. The temperature of the core displacement device was set at 85°C and 8 MPa, and the fluid loss was observed and recorded every 30 minutes to further investigate the plugging capacity of the temporary plugging agent. The results are shown in Table 3 and Figure 3.

表3 页岩气开采用环保型可控暂堵剂对混砂A的封堵性能Table 3 The plugging performance of environmental-friendly controllable temporary plugging agent for sand mixing A in shale gas development

时间(h)time (h) 0.50.5 1.01.0 1.51.5 2.02.0 2.52.5 3.03.0 3.53.5 4.04.0 4.54.5 滤失量(ml)Filtration loss (ml) 100100 3.53.5 77 44 33 33 33 88 100100

由表3和图3可见,页岩气开采用环保型可控暂堵剂对混砂A的封堵在前30min内样品溶胀前封堵不太理想,溶胀完成后封堵率为90%以上,且相当稳定,且在规定溶解时间后解堵,返排效果好。It can be seen from Table 3 and Figure 3 that the plugging of mixed sand A with an environmentally friendly and controllable temporary plugging agent in shale gas development is not ideal before the sample is swollen in the first 30 minutes, and the plugging rate is over 90% after the swelling is completed , and quite stable, and after the specified dissolution time, the blockage is removed, and the flowback effect is good.

2.4 将5-10mm的砂砾(粗砂)填充到直径20cm、长度60cm的填砂管中,将上述制得的页岩气开采用环保型可控暂堵剂注入到岩心管中,将岩心驱替装置温度设定为85℃、8MPa,每30min观察记录滤失量,进一步考察暂堵剂的封堵能力,结果如表4和图4所示。2.4 Fill the 5-10mm gravel (coarse sand) into the sand-packing tube with a diameter of 20 cm and a length of 60 cm, inject the shale gas developed above into the core tube with an environment-friendly controllable temporary plugging agent, and drive the core into the core tube. The temperature of the replacement device was set at 85°C and 8 MPa, and the fluid loss was observed and recorded every 30 minutes to further investigate the plugging capacity of the temporary plugging agent. The results are shown in Table 4 and Figure 4.

表4 页岩气开采用环保型可控暂堵剂对粗砂的封堵性能Table 4. Plugging performance of environmental-friendly controllable temporary plugging agent for coarse sand in shale gas development

时间(h)time (h) 0.50.5 1.01.0 1.51.5 2.02.0 2.52.5 3.03.0 3.53.5 4.04.0 4.54.5 滤失量(ml)Filtration loss (ml) 100100 88 55 33 22 1515 2727 100100 100100

由表4和图4可见,页岩气开采用环保型可控暂堵剂对粒径较大的粗砂(5-10mm)的封堵在前30min内样品溶胀前封堵不太理想,溶胀完成后封堵率为90%以上,由于粗砂粒径较大,沙砾间缝隙较大,暂堵剂与水的接触面积较大,暂堵剂溶解较快,后期溶解速度加快。且在规定溶解时间后解堵,返排效果好。It can be seen from Table 4 and Figure 4 that the plugging of large particle size coarse sand (5-10 mm) by environmental-friendly controllable temporary plugging agent in shale gas development is not ideal before the sample swells in the first 30 minutes, and the swelling After completion, the plugging rate is more than 90%. Due to the large particle size of the coarse sand and the large gaps between the gravels, the contact area between the temporary plugging agent and water is large, the temporary plugging agent dissolves quickly, and the later dissolution speed is accelerated. And after the specified dissolution time, the blockage is removed, and the flowback effect is good.

2.5 将细砂与粗砂(混砂B)填充到直径20cm、长度60cm的填砂管中,将上述制得的页岩气开采用环保型可控暂堵剂注入到岩心管中,将岩心驱替装置温度设定为85℃、8MPa,每30min观察记录滤失量,进一步考察暂堵剂的封堵能力,结果见表5和图5。2.5 Fill fine sand and coarse sand (mixed sand B) into a sand-packing tube with a diameter of 20 cm and a length of 60 cm, and inject the shale gas prepared above into the core tube with an environmentally-friendly controllable temporary plugging agent. The temperature of the displacement device was set at 85°C and 8 MPa, and the fluid loss was observed and recorded every 30 minutes to further investigate the plugging capacity of the temporary plugging agent. The results are shown in Table 5 and Figure 5.

表5 页岩气开采用环保型可控暂堵剂对混砂B的封堵性能Table 5. Plugging performance of environment-friendly controllable temporary plugging agent for sand mixing B in shale gas development

时间(h)time (h) 0.50.5 1.01.0 1.51.5 2.02.0 2.52.5 3.03.0 3.53.5 4.04.0 4.54.5 滤失量(ml)Filtration loss (ml) 100100 66 22 22 22 22 99 99 100100

由表5、图5可见,页岩气开采用环保型可控暂堵剂对混砂B的封堵在前30min内样品溶胀前封堵不太理想,溶胀完成后封堵率为90%以上,并且比较稳定,在规定溶解时间后解堵,返排效果好。It can be seen from Table 5 and Figure 5 that the plugging of mixed sand B with an environmentally friendly and controllable temporary plugging agent for shale gas development is not ideal before the sample swells in the first 30 minutes, and the plugging rate is over 90% after the swelling is completed , and relatively stable, after the specified dissolution time, the blockage is removed, and the flowback effect is good.

2.6 将中砂与粗砂(混砂C)填充到直径20cm、长度60cm的填砂管中,将上述制得的页岩气开采用环保型可控暂堵剂注入到岩心管中,将岩心驱替装置温度设定为85℃、8MPa,每30min观察记录滤失量,进一步考察暂堵剂的封堵能力,结果见表6和图6。2.6 Fill medium sand and coarse sand (mixed sand C) into a sand-packing tube with a diameter of 20 cm and a length of 60 cm, inject the shale gas prepared above into the core tube with an environment-friendly controllable temporary plugging agent, and core The temperature of the displacement device was set at 85°C and 8 MPa, and the fluid loss was observed and recorded every 30 minutes to further investigate the plugging capacity of the temporary plugging agent. The results are shown in Table 6 and Figure 6.

表6 页岩气开采用环保型可控暂堵剂对混砂C的封堵性能Table 6. Plugging performance of environment-friendly controllable temporary plugging agent for sand mixing C in shale gas development

时间(h)time (h) 0.50.5 1.01.0 1.51.5 2.02.0 2.52.5 3.03.0 3.53.5 4.04.0 4.54.5 滤失量(ml)Filtration loss (ml) 100100 1818 66 55 66 66 100100 100100 100100

由表6、图6可见,页岩气开采用环保型可控暂堵剂对混砂C的封堵在前30min内样品溶胀前封堵不太理想,溶胀完成后封堵率为82%以上,经过一段时间的挤压后,封堵率达到94%左右,并且比较稳定;在规定溶解时间后解堵,返排效果好。It can be seen from Table 6 and Figure 6 that the plugging of mixed sand C with environmentally friendly and controllable temporary plugging agent in shale gas development is not ideal before the sample swells in the first 30 minutes, and the plugging rate after swelling is over 82% , After a period of extrusion, the plugging rate reaches about 94%, and it is relatively stable; after the specified dissolution time, the blockage is removed, and the flowback effect is good.

2.7 将细砂、中砂与粗砂(混砂D)填充到直径20cm、长度60cm的填砂管中,将上述制得的页岩气开采用环保型可控暂堵剂注入到岩心管中,将岩心驱替装置温度设定为85℃、8MPa,每30min观察记录滤失量,进一步考察暂堵剂的封堵能力,结果见表7、图7。2.7 Fill fine sand, medium sand and coarse sand (mixed sand D) into the sand packing pipe with a diameter of 20cm and a length of 60cm, and inject the environmental-friendly controllable temporary plugging agent for shale gas development prepared above into the core pipe , set the temperature of the core displacement device at 85°C and 8 MPa, observe and record the fluid loss every 30 minutes, and further investigate the plugging capacity of the temporary plugging agent. The results are shown in Table 7 and Figure 7.

表7 页岩气开采用环保型可控暂堵剂对混砂D的封堵性能Table 7. Plugging performance of environmental-friendly controllable temporary plugging agent for sand mixing D in shale gas development

时间(h)time (h) 0.50.5 1.01.0 1.51.5 2.02.0 2.52.5 3.03.0 3.53.5 4.04.0 4.54.5 滤失量(ml)Filtration loss (ml) 100100 1515 66 66 55 55 100100 100100 100100

由表6、图6可见,页岩气开采用环保型可控暂堵剂对混砂D的封堵在前30min内样品溶胀前封堵不太理想,溶胀完成后封堵率为85%以上,经过一段时间的挤压后,封堵率达到94%左右,并且比较稳定;在规定溶解时间后解堵,返排效果好。It can be seen from Table 6 and Figure 6 that the plugging of mixed sand D with environmental-friendly controllable temporary plugging agent in shale gas development is not ideal in the first 30 minutes before the sample is swollen, and the plugging rate is over 85% after the swelling is completed , After a period of extrusion, the plugging rate reaches about 94%, and it is relatively stable; after the specified dissolution time, the blockage is removed, and the flowback effect is good.

上面结合附图对本发明的实施例进行了描述,但是本发明并不局限于上述的具体实施方式,上述的具体实施方式仅仅是示意性的,而不是限制性的,本领域的普通技术人员在本发明的启示下,在不脱离本发明宗旨和权利要求所保护的范围情况下,还可做出很多形式的改变,这些均属于本发明的保护之内。Embodiments of the present invention have been described above in conjunction with the accompanying drawings, but the present invention is not limited to the above-mentioned specific implementations, and the above-mentioned specific implementations are only illustrative, rather than restrictive, and those of ordinary skill in the art will Under the enlightenment of the present invention, without departing from the gist of the present invention and the protection scope of the claims, many changes can be made, and these all belong to the protection of the present invention.

Claims (6)

1. a kind of controllable diverting agent of environment-friendly type, is formed by synthesizing stoste and gel compounding, it is characterised in that:The synthesis stoste Mixed by polyvinyl alcohol, soluble starch, gelatin, sodium alginate, ammonium persulfate and water, the gel includes helping gel Agent and main gel, wherein help gel to be formed by anhydrous calcium chloride, anhydrous sodium sulfate, disodium ethylene diamine tetraacetate compounding, it is main Gel is formed by sodium tetraborate, ammonium persulfate compounding.
2. the controllable diverting agent of a kind of environment-friendly type according to claim 1, it is characterised in that:Polyethylene in the synthesis stoste The mass fraction of alcohol is 3-9%, and the mass fraction of soluble starch is 2-6%, and the mass fraction of gelatin is 1-6%, the matter of water Amount fraction is 70%, balance of sodium alginate and ammonium persulfate mixture.
3. the controllable diverting agent of a kind of environment-friendly type according to claim 1, it is characterised in that:It is described to help anhydrous chlorine in gel It is 1-2 to change calcium, anhydrous sodium sulfate, the mass ratio of disodium ethylene diamine tetraacetate:1-2:1-4.
4. the controllable diverting agent of a kind of environment-friendly type according to claim 1, it is characterised in that:Tetraboric acid in the main gel Sodium, the mass ratio of ammonium persulfate are 1-4:2.
5. the controllable diverting agent of a kind of environment-friendly type according to claim any one of 1-4, it is characterised in that:The diverting agent by Synthesize stoste, help gel, main gel according to 100:3-8:The mass ratio of 3-6 is mixed.
6. the preparation method of the controllable diverting agent of a kind of environment-friendly type, it is characterised in that comprise the following steps:A () is claimed by proportion speed Weight northylen alcohol, soluble starch, gelatin, sodium alginate, ammonium persulfate and water, mixed dissolution obtain synthesizing stoste;B () is by matching somebody with somebody Gel is helped than mixing to be re-dubbed anhydrous calcium chloride, anhydrous sodium sulfate, disodium ethylene diamine tetraacetate, by sodium tetraborate, over cure It is standby that sour ammonium is re-dubbed main gel;C () will help gel to be added in homogeneous synthesis stoste, will be main after reaction a period of time Gel is added in mixed solution, stands the hot pressing controllable diverting agent of drying environment-friendly type after cooling.
CN201710213054.XA 2017-04-01 2017-04-01 A kind of controllable diverting agent of environment-friendly type and preparation method thereof Pending CN106883832A (en)

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Application publication date: 20170623