CN112063375A - High-temperature-resistant high-density oil-based well completion fluid and preparation method thereof - Google Patents

High-temperature-resistant high-density oil-based well completion fluid and preparation method thereof Download PDF

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CN112063375A
CN112063375A CN202010950835.9A CN202010950835A CN112063375A CN 112063375 A CN112063375 A CN 112063375A CN 202010950835 A CN202010950835 A CN 202010950835A CN 112063375 A CN112063375 A CN 112063375A
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completion fluid
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emulsifier
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周双君
余进
罗绪武
赵利
吴义成
于德成
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CNPC Xibu Drilling Engineering Co Ltd
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/32Non-aqueous well-drilling compositions, e.g. oil-based
    • C09K8/34Organic liquids
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/03Specific additives for general use in well-drilling compositions

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Abstract

本发明提出一种抗高温高密度油基完井液及其制备方法,属于石油勘探开发技术领域。该高密度油基完井液,由包括如下重量份数原料制备而得,白油80~90份、氯化钙水溶液10~20份、主乳化剂20~30份、辅乳化剂10~20份、有机土5~10份、提切剂5~10份、润湿剂10~15份、降滤失剂25~30份、氧化钙5~10份、加重材料150~200份。本发明所得产品质量稳定性较好,产品粒径D50小于1.5微米,产品抗温可到240℃以上,产品密度可达2.5g/cm3以上,在高温条件下可保证15‑20天具有良好的流变性和悬浮稳定性,不污染地层,可重复使用。The invention provides a high-temperature resistant and high-density oil-based well completion fluid and a preparation method thereof, belonging to the technical field of petroleum exploration and development. The high-density oil-based completion fluid is prepared by including the following raw materials in parts by weight: 80-90 parts of white oil, 10-20 parts of calcium chloride aqueous solution, 20-30 parts of main emulsifier, and 10-20 parts of auxiliary emulsifier parts, 5-10 parts of organic soil, 5-10 parts of cutting agent, 10-15 parts of wetting agent, 25-30 parts of fluid loss reducer, 5-10 parts of calcium oxide, and 150-200 parts of weighting material. The product obtained by the invention has good quality stability, the product particle size D50 is less than 1.5 microns, the product temperature resistance can reach above 240°C, the product density can reach above 2.5g/cm3, and the product can be guaranteed to have good quality for 15-20 days under high temperature conditions. Rheology and suspension stability, do not pollute the formation, and can be reused.

Description

一种抗高温高密度油基完井液及其制备方法A kind of high temperature resistant and high density oil-based well completion fluid and preparation method thereof

技术领域technical field

本发明属于石油勘探开发技术领域,尤其涉及一种抗高温高密度油基完 井液及其制备方法。The invention belongs to the technical field of petroleum exploration and development, and in particular relates to a high-temperature-resistant and high-density oil-based well completion fluid and a preparation method thereof.

背景技术Background technique

目前,石油钻探不断向深部地层发展,井深达到6000米以上井越来越多, 随着钻探深度增加,井底温度越来越高,钻遇高压地层也越来越多。部分井井底 温度达到200℃,地层压力系数达到2.30。完井液面临高温高压挑战,高密度钻 完井液中需要加入大量的固相加重材料以提高密度,导致了钻完井液中固相含量 高,完井作业要求高密度完井液具有良好的高温沉降稳定性,一般油基完井液在 高温作用下粘度降低,高密度固相在重力作用下易沉降。现场应用普遍存在完井 液高温流变性与沉降稳定性难以控制的基本矛盾。At present, oil drilling continues to develop into deep formations, with more and more wells reaching depths of more than 6,000 meters. As the drilling depth increases, the bottom hole temperature is getting higher and higher, and more and more high-pressure formations are drilled. The bottom hole temperature of some wells reached 200°C, and the formation pressure coefficient reached 2.30. Completion fluids face the challenge of high temperature and high pressure. High-density drilling and completion fluids need to add a large amount of solid weighting materials to increase the density, resulting in high solids content in drilling and completion fluids. Completion operations require high-density completion fluids with good properties. Generally, the viscosity of oil-based completion fluid decreases under the action of high temperature, and the high-density solid phase is easy to settle under the action of gravity. In field applications, the basic contradiction between the high temperature rheology and settlement stability of completion fluids is difficult to control.

新疆准噶尔盆地南缘井完井后地层压力系数高,要求钻井液密度更高,抗温 和抗各种污染能力更强(饱和盐、石膏、钻屑综合污染)。常规加重剂(如重晶 石粉)的粒径通常在10μm~70μm之间,在应用过程中经常出现重晶石沉降速 率高、钻井液密度上下不均等现象。为了解决其悬浮问题,通常需加入大量处理 剂。但随着处理剂加量的增大,一方面导致钻井液的成本急剧上升;另一方面导 致钻井液流变性恶化且难以控制,保持较低的流变参数以有效控制循环当量密度 (ECD)和较高的粘切以保证重晶石悬浮性之间的矛盾难以调和,从而严重影响 完井工作安全性。因此,研发一种高密度油基完井液就显得尤为重要。After completion of wells in the southern margin of the Junggar Basin, Xinjiang, the formation pressure coefficient is high, requiring higher drilling fluid density, stronger resistance to temperature and various contamination (comprehensive contamination of saturated salt, gypsum, and drill cuttings). The particle size of conventional weighting agents (such as barite powder) is usually between 10 μm and 70 μm. During the application process, the phenomenon of high barite sedimentation rate and uneven density of drilling fluid often occur. In order to solve its suspension problem, it is usually necessary to add a large amount of treatment agent. However, with the increase of the amount of treatment agent, the cost of drilling fluid rises sharply on the one hand; on the other hand, the rheology of drilling fluid deteriorates and is difficult to control, so keep low rheological parameters to effectively control the circulating equivalent density (ECD) It is difficult to reconcile the contradiction between the high viscosity and high stick cut to ensure the suspension of barite, which seriously affects the safety of completion work. Therefore, it is particularly important to develop a high-density oil-based completion fluid.

发明内容SUMMARY OF THE INVENTION

本发明提出一种抗高温高密度油基完井液及其制备方法,以解决上述技术问 题。The present invention proposes a high temperature resistant and high density oil-based well completion fluid and a preparation method thereof to solve the above technical problems.

本发明提出高密度油基完井液,由包括如下重量份数原料制备而得,白油 80~90份、氯化钙水溶液10~20份、主乳化剂20~30份、辅乳化剂10~20份、 有机土5~10份、提切剂5~10份、润湿剂10~15份、降滤失剂25~30份、氧 化钙5~10份、加重材料150~200份。The present invention proposes a high-density oil-based completion fluid, which is prepared by including the following raw materials in parts by weight: 80-90 parts of white oil, 10-20 parts of calcium chloride aqueous solution, 20-30 parts of main emulsifier, and 10 parts of auxiliary emulsifier ~20 parts, 5-10 parts of organic soil, 5-10 parts of cutting agent, 10-15 parts of wetting agent, 25-30 parts of fluid loss control agent, 5-10 parts of calcium oxide, 150-200 parts of weighting material.

进一步地,所述白油为3#白油。Further, the white oil is 3# white oil.

进一步地,所述氯化钙水溶液的浓度为30wt%。Further, the concentration of the calcium chloride aqueous solution is 30wt%.

进一步地,所述主乳化剂为脂肪酸的衍生物。Further, the main emulsifier is a derivative of fatty acid.

进一步地,所述辅乳化剂为脂肪酸酰的胺衍生物。Further, the co-emulsifier is an amine derivative of fatty acid acyl.

进一步地,所述提切剂为聚酰胺的胺衍生物。Further, the cutting agent is an amine derivative of polyamide.

进一步地,所述润湿剂为酰胺基聚醚。Further, the wetting agent is an amido polyether.

进一步地,所述降滤失剂为腐植酸酰胺。Further, the fluid loss control agent is humic acid amide.

进一步地,所述加重材料为重晶石、碳酸钙或铁矿粉中至少一种。Further, the weighting material is at least one of barite, calcium carbonate or iron ore powder.

本发明还提出一种上述高密度油基完井液的制备方法,包括如下步骤,The present invention also provides a method for preparing the above-mentioned high-density oil-based completion fluid, comprising the following steps:

(1)将白油置于泥浆罐中,加入主乳化剂、辅乳化剂,搅拌,得混合物一;(1) place white oil in a mud tank, add main emulsifier and auxiliary emulsifier, and stir to obtain mixture 1;

(2)向上述混合物一中加入氯化钙水溶液,搅拌,得混合物二;(2) in above-mentioned mixture one, add calcium chloride aqueous solution, stir, obtain mixture two;

(3)向上述混合物二中加入有机土、提切剂、润湿剂、降滤失剂、氧化钙 和加重材料,搅拌,监测破乳电压达到400V既得产品。(3) in above-mentioned mixture two, add organic soil, cutting agent, wetting agent, fluid loss reducer, calcium oxide and weighting material, stir, monitor demulsification voltage and reach 400V obtained product.

本发明具有以下优势:The present invention has the following advantages:

本发明所得产品质量稳定性较好,产品粒径D50小于1.5微米,产品抗温可 到240℃以上,产品密度可达2.5g/cm3以上,在高温条件下可保证15-20天具有 良好的流变性和悬浮稳定性,不污染地层,可重复使用。The product obtained by the invention has good quality stability, the product particle size D50 is less than 1.5 microns, the product temperature resistance can reach more than 240 DEG C, the product density can reach more than 2.5g/cm 3 , and the product can be guaranteed to have good quality for 15-20 days under high temperature conditions. Excellent rheology and suspension stability, do not pollute the formation, and can be reused.

具体实施方式Detailed ways

下面将结合本发明实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。在不冲突的 情况下,本发明中的实施例及实施例中的特征可以相互组合。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Embodiments of the invention and features of the embodiments may be combined with each other without conflict.

实施例1一种高密度油基完井液(按质量分数配比)Example 1 A kind of high-density oil-based completion fluid (proportion by mass fraction)

9%3#白油、1%氯化钙水溶液、2.5%主乳化剂、3%辅乳化、0.5%有机土、 0.5%提切剂、1%润湿剂、3%降滤失剂、0.5%CaO、重晶石;9% 3# white oil, 1% calcium chloride aqueous solution, 2.5% main emulsifier, 3% auxiliary emulsifier, 0.5% organic soil, 0.5% cutting agent, 1% wetting agent, 3% fluid loss reducer, 0.5% %CaO, barite;

制备方法:包括如下步骤,Preparation method: including the following steps,

(1)将白油置于泥浆罐中,加入主乳化剂、辅乳化剂,搅拌,得混合物一;(1) place white oil in a mud tank, add main emulsifier and auxiliary emulsifier, and stir to obtain mixture 1;

(2)向上述混合物一中加入氯化钙水溶液,搅拌,得混合物二;(2) in above-mentioned mixture one, add calcium chloride aqueous solution, stir, obtain mixture two;

(3)向上述混合物二中加入有机土、提切剂、润湿剂、降滤失剂、氧化钙 和加重材料,搅拌,监测破乳电压达到400V既得产品。(3) in above-mentioned mixture two, add organic soil, cutting agent, wetting agent, fluid loss reducer, calcium oxide and weighting material, stir, monitor demulsification voltage and reach 400V obtained product.

实施例2一种高密度油基完井液(按质量分数配比)Embodiment 2 A kind of high-density oil-based completion fluid (proportion by mass fraction)

8.8%3#白油、1.2%水、3%主乳化剂、2%辅乳化、1%有机土、0.5%提切剂、1%润湿剂、3%降滤失剂、0.5%CaO、重晶石8.8% 3# white oil, 1.2% water, 3% main emulsifier, 2% auxiliary emulsifier, 1% organic soil, 0.5% cutting agent, 1% wetting agent, 3% fluid loss reducer, 0.5% CaO, barite

试验例1Test Example 1

新疆油田GT1井,完钻井深5920m,试油完井液作业要求,采用密度 2.43g/cm3完井液压井,完井液抗温能力135℃,沉降稳定性达到15天。将实施 例1所得完井液进行测试,结果见表1。The GT1 well in Xinjiang Oilfield was completed at a depth of 5920m, and the completion fluid required for oil testing. The completion hydraulic well with a density of 2.43g/cm3 was used. The temperature resistance of the completion fluid was 135°C, and the settlement stability reached 15 days. The completion fluid obtained in Example 1 was tested, and the results are shown in Table 1.

表1Table 1

Figure BDA0002676829470000031
Figure BDA0002676829470000031

老化条件为:200℃×16h;流变性测试温度50℃,HTHP滤失量测试温度 180℃。The aging conditions are: 200℃×16h; the rheology test temperature is 50℃, and the HTHP filtration loss test temperature is 180℃.

实验测试密度达到2.50g/cm3,满足135℃温度条件下静置15天不出现加 重材料硬性沉淀,沉降因子小于0.52。The experimental test density reaches 2.50g/cm3, which satisfies the condition of standing at 135°C for 15 days without hard precipitation of the weighted material, and the sedimentation factor is less than 0.52.

现场应用2.43g/cm3油基完井液注入井筒,连续静置10.5天,保持良好的高 温沉降稳定性,保障压井试油作业顺利进行。On-site application of 2.43g/cm3 oil-based completion fluid was injected into the wellbore, and it was allowed to stand for 10.5 days to maintain good high-temperature settlement stability and ensure smooth well killing and oil testing.

试验例2Test Example 2

博孜12井是位于克拉苏构造带克深区带博孜段与阿瓦特段结合部博孜12 号构造高点附近的一口预探井,设计井深6960m,实钻井深7057m。博孜12井 目的层钻进过程中,使用相对密度1.85的钻井液存在持续渗漏,且安全钻进钻 井液密度窗口小,借用博孜3气藏地温梯度(1.8℃/100m)、静压压力梯度 (0.37MPa/100m),预测博孜12井白垩系巴什基奇克组、巴西改组中深6963.5m (海拔-4871.6m),地层温度约143.93℃,地层压力约125.01MPa,压力系数为 1.83。实测地层温度137.7℃。将实施例2所得完井液进行测试。所得结果见表2。Well Bozi 12 is a pre-exploration well located near the structural high point of Bozi No. 12 at the junction of the Bozi Member and the Avat Member in the Keshen Zone of the Kelasu Structural Belt. The designed well depth is 6960m and the actual drilling depth is 7057m. During the drilling of the target layer of Well Bozi 12, the drilling fluid with a relative density of 1.85 has continuous leakage, and the safe drilling fluid density window is small. The pressure gradient (0.37MPa/100m) is predicted to be 6963.5m (-4871.6m above sea level) in the Cretaceous Bashijiqike Formation in Well Bozi 12 (altitude -4871.6m), the formation temperature is about 143.93℃, the formation pressure is about 125.01MPa, and the pressure coefficient is 1.83. The measured formation temperature is 137.7℃. The completion fluid obtained in Example 2 was tested. The results obtained are shown in Table 2.

表2Table 2

Figure BDA0002676829470000032
Figure BDA0002676829470000032

老化条件为:140℃×16h;流变性测试温度50℃,HTHP滤失量测试温度 140℃。The aging conditions are: 140℃×16h; the rheology test temperature is 50℃, and the HTHP filtration loss test temperature is 140℃.

以上仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精 神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护 范围之内。The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the protection scope of the present invention. within.

Claims (9)

1. The high-temperature-resistant high-density oil-based well completion fluid is characterized by being prepared from the following raw materials, by weight, 80-90 parts of white oil, 10-20 parts of a calcium chloride aqueous solution, 20-30 parts of a main emulsifier, 10-20 parts of an auxiliary emulsifier, 5-10 parts of organic soil, 5-10 parts of a shear improver, 10-15 parts of a wetting agent, 25-30 parts of a fluid loss additive, 5-10 parts of calcium oxide and 150-200 parts of a weighting material.
2. The completion fluid of claim 1, wherein the aqueous calcium chloride solution has a concentration of 30 wt%.
3. The completion fluid of claim 1, wherein the primary emulsifier is a derivative of a fatty acid.
4. The completion fluid of claim 1, wherein the coemulsifier is an amine derivative of a fatty acid.
5. The completion fluid of claim 1, wherein the shear promoter is an amine derivative of a polyamide.
6. The completion fluid of claim 1, wherein the wetting agent is an amido polyether.
7. The completion fluid of claim 1, wherein the fluid loss additive is a humic acid amide.
8. The completion fluid of claim 1, wherein the weighting material is at least one of barite, calcium carbonate, or iron ore fines.
9. A method for preparing the high temperature resistant high density oil-based completion fluid according to any one of claims 1 to 8, comprising the steps of,
(1) putting the white oil into a mud pot, adding a main emulsifier and an auxiliary emulsifier, and stirring to obtain a first mixture;
(2) adding a calcium chloride aqueous solution into the mixture I, and stirring to obtain a mixture II;
(3) and adding organic soil, a cutting agent, a wetting agent, a filtrate reducer, calcium oxide and a weighting material into the mixture II, stirring, and monitoring the demulsification voltage to reach 400V to obtain the product.
CN202010950835.9A 2020-09-11 2020-09-11 High-temperature-resistant high-density oil-based well completion fluid and preparation method thereof Pending CN112063375A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116144331A (en) * 2021-11-22 2023-05-23 中国石油天然气集团有限公司 Oil testing completion fluid and preparation method and application thereof
CN114015424A (en) * 2021-12-06 2022-02-08 沙克(天津)石油技术服务有限公司 Test oil slurry suitable for high-temperature high-pressure well

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Application publication date: 20201211