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CN201284636Y - Circulating foam simulation experiment apparatus - Google Patents

Circulating foam simulation experiment apparatus Download PDF

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Publication number
CN201284636Y
CN201284636Y CNU200820141304XU CN200820141304U CN201284636Y CN 201284636 Y CN201284636 Y CN 201284636Y CN U200820141304X U CNU200820141304X U CN U200820141304XU CN 200820141304 U CN200820141304 U CN 200820141304U CN 201284636 Y CN201284636 Y CN 201284636Y
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foam
defoaming
defoamer
stop valve
chemical
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万里平
孟英峰
李永杰
陈浩
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Southwest Petroleum University
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Abstract

本实用新型涉及在石油天然气钻井中模拟循环泡沫钻井用的一种可循环泡沫模拟实验装置。它由基液添加系统、供气系统、泡沫加热系统、机械消泡装置系统和化学消泡剂添加系统连接构成。其通过基液添加系统、供气系统、泡沫加热系统、机械消泡装置系统和化学消泡剂添加系统相连形成闭合的整体实验系统,实施泡沫循环利用。有益效果是:1.通过监测取样器出口的泡沫质量、半衰期、温度、压力、密度等参数,可实现泡沫性能的快速调节,达到模拟井下高温高压环境的目的;2.模拟实验装置充分利用化学与机械联合消泡的增效作用,克服单一消泡法消泡效率不足的缺点,有利于实现泡沫的循环利用。

The utility model relates to a circulatory foam simulation experiment device used for simulating circulation foam drilling in oil and gas drilling. It is composed of base liquid adding system, air supply system, foam heating system, mechanical defoaming device system and chemical defoaming agent adding system. It forms a closed overall experimental system by connecting the base liquid adding system, air supply system, foam heating system, mechanical defoaming device system and chemical defoaming agent adding system, and implements foam recycling. The beneficial effects are: 1. By monitoring the foam quality, half-life, temperature, pressure, density and other parameters at the outlet of the sampler, the foam performance can be quickly adjusted to achieve the purpose of simulating the high temperature and high pressure environment in the well; 2. The simulation experiment device makes full use of chemical The synergistic effect of combined defoaming with machinery overcomes the shortcomings of insufficient defoaming efficiency of the single defoaming method, and is conducive to realizing the recycling of foam.

Description

一种可循环泡沫模拟实验装置 A recyclable foam simulation experiment device

技术领域 technical field

本实用新型涉及在石油天然气钻井中模拟循环泡沫钻井用的一种可循环泡沫模拟实验装置。The utility model relates to a circulatory foam simulation experiment device used for simulating circulation foam drilling in oil and gas drilling.

背景技术 Background technique

泡沫流体技术始于20世纪50年代,国内在80年代开始泡沫流体钻井技术的研究和应用,并相继在新疆、胜利、辽河、大庆、长庆、四川等油田取得现场实践。泡沫流体由于具有与普通流体不同的独特结构,与常规泥浆钻井相比,泡沫钻井具有以下显著优点:1、提高钻速,延长钻头的使用寿命;2、钻井液漏失量低,可减少地层损害;3、携岩能力强,能有效地清除井底岩屑;4、油气显示明显;5、粘度高、静液柱压力低、可大大减少地层漏失。因此,泡沫钻井技术在低压、低渗油气藏和易漏地层应用较多,是实现欠平衡钻井保护低压油气藏的最有效的方法之一,随着新老油田的开发,以泡沫作循环介质的钻井作业会不断增加。Foam fluid technology began in the 1950s, and domestic research and application of foam fluid drilling technology began in the 1980s, and field practice was successively obtained in Xinjiang, Shengli, Liaohe, Daqing, Changqing, Sichuan and other oilfields. Foam fluid has a unique structure different from ordinary fluids. Compared with conventional mud drilling, foam drilling has the following significant advantages: 1. Improve the drilling speed and prolong the service life of the drill bit; 2. Low drilling fluid loss can reduce formation damage ; 3. Strong rock-carrying ability, which can effectively remove cuttings at the bottom of the well; 4. Obvious oil and gas display; 5. High viscosity and low hydrostatic column pressure can greatly reduce formation loss. Therefore, foam drilling technology is widely used in low-pressure, low-permeability oil and gas reservoirs and leaky formations. It is one of the most effective methods to realize underbalanced drilling and protect low-pressure oil and gas reservoirs. With the development of new and old oil fields, foam is used as a circulating medium drilling operations will continue to increase.

目前的泡沫钻井工艺存在泡沫一次性使用量大,返出的泡沫易污染环境等问题,不仅增加泡沫钻井成本,而且不利于泡沫钻井技术的推广应用。泡沫流体循环利用已成为国内外共同关注的技术难题,制约此技术的“瓶颈”问题在于难以找到一种高效、快速消除从井口返出的大量泡沫的有效方法。目前常用的消泡法包括物理消泡法;机械消泡法;化学消泡法和自然消泡法等四种,它们在消除泡沫的同时都存在不足。物理消泡不能处理大量泡沫,只适用于某些应急措施;机械消泡不仅需要附加设备,而且消泡率不高;化学消泡法施工简单、消泡率高,但消泡剂耗量大,成本偏高;自然消泡占地面积大、消泡时间长。The current foam drilling technology has problems such as large amount of foam used at one time, and the returned foam is easy to pollute the environment, which not only increases the cost of foam drilling, but also is not conducive to the popularization and application of foam drilling technology. Foam fluid recycling has become a technical problem of common concern at home and abroad. The "bottleneck" problem restricting this technology is that it is difficult to find an effective method to quickly and efficiently eliminate a large amount of foam returning from the wellhead. Currently commonly used defoaming methods include physical defoaming method; mechanical defoaming method; chemical defoaming method and natural defoaming method, and they all have deficiencies in eliminating foam. Physical defoaming cannot handle a large amount of foam and is only suitable for some emergency measures; mechanical defoaming not only requires additional equipment, but also has a low defoaming rate; chemical defoaming method is simple in construction and high in defoaming rate, but consumes a lot of defoaming agent , the cost is high; natural defoaming covers a large area and takes a long time to defoam.

专利CN200510078221.1介绍了钻井泡沫循环利用方法,将返至井口的泡沫直接导入密闭循环系统,在密闭条件下清除其中的岩屑,然后利用泡沫增压系统对其进行增压,使其压力达到需要的值,最后再使其进入入井管汇、实现循环利用。此外还有采用机械法消泡的专利介绍。由于目前缺乏在室内模拟循环泡沫钻井用的实验装置,所以研究在室内模拟循环泡沫钻井用的实验装置对泡沫钻井工艺技术发展,找出最佳的消泡方法具有重要意义。Patent CN200510078221.1 introduces a drilling foam recycling method. The foam returned to the wellhead is directly introduced into the closed circulation system, and the cuttings are removed under the closed condition, and then pressurized by the foam pressurization system to make its pressure reach The required value, and finally make it enter the well manifold to realize recycling. In addition, there is a patent introduction on the use of mechanical defoaming. Since there is no experimental device for indoor simulation of circulating foam drilling, it is of great significance to study the experimental device for indoor simulation of circulating foam drilling for the development of foam drilling technology and to find out the best defoaming method.

实用新型内容 Utility model content

本实用新型目的在于提供一种模拟循环泡沫钻井用的实验装置,为研究泡沫钻井工艺提供实验数据及理论基础。The purpose of the utility model is to provide an experimental device for simulating circulating foam drilling, and to provide experimental data and theoretical basis for studying foam drilling technology.

本实用新型所采用的技术方案是:一种可循环泡沫模拟实验装置由基液添加系统、供气系统、泡沫加热系统、机械消泡装置系统和化学消泡剂添加系统连接构成,其通过基液添加系统、供气系统、泡沫加热系统、机械消泡装置系统和化学消泡剂添加系统相连形成闭合的整体实验系统。The technical solution adopted by the utility model is: a recyclable foam simulation experiment device is composed of a base liquid adding system, an air supply system, a foam heating system, a mechanical defoaming device system and a chemical defoaming agent adding system. Liquid addition system, gas supply system, foam heating system, mechanical defoamer system and chemical defoamer addition system are connected to form a closed overall experimental system.

所述基液添加系统由泡沫基液罐、截止阀、计量泵、孔板流量计依序安装组成;所述供气系统由空压机、放空阀、贮气罐、截止阀、转子流量计、截止阀依序连接安装组成;通过基液添加系统与供气系统形成气液混合流,进入泡沫发生器;泡沫发生器出口端安装有压力表和截止阀;通过调节进入泡沫发生器的气液比和压力,可实现模拟泡沫钻井的压力环境的目的。The base liquid adding system is composed of a foam base liquid tank, a stop valve, a metering pump, and an orifice flowmeter; the air supply system is composed of an air compressor, a vent valve, an air tank, a stop valve, and a rotameter. The gas-liquid mixed flow is formed through the base liquid adding system and the gas supply system, and enters the foam generator; a pressure gauge and a stop valve are installed at the outlet of the foam generator; by adjusting the gas entering the foam generator Fluid ratio and pressure can realize the purpose of simulating the pressure environment of foam drilling.

所述泡沫加热系统由电缆伴热管、热电偶温度计、截止阀、泡沫取样器连接组成:泡沫取样器的出口端安装有压力表和截止阀;通过调节电缆伴热管温度可以达到模拟井下高温环境的目的,泡沫取样器可用来实时监测泡沫质量、半衰期、温度、压力、密度等参数。The foam heating system is composed of a cable heating tube, a thermocouple thermometer, a shut-off valve and a foam sampler; a pressure gauge and a shut-off valve are installed at the outlet of the foam sampler; the temperature of the underground high-temperature environment can be simulated by adjusting the temperature of the cable heating tube. Objective: The foam sampler can be used to monitor foam quality, half-life, temperature, pressure, density and other parameters in real time.

所述机械消泡装置系统是在机械消泡装置的顶部安装有喷淋管,从消泡剂储罐中泵送出的消泡剂,通过喷淋管均匀喷洒到泡沫上,达到化学消泡的目的;机械消泡装置的两端对称安装有破泡喷嘴,泡沫流体通过破泡喷嘴喷出,利用其冲击力、剪切力及产生负压来实现机械消泡,通过改变破泡喷嘴的喷嘴数量和孔径,可以调节机械消泡装置的消泡效率。The mechanical defoaming device system is equipped with a spray pipe on the top of the mechanical defoaming device, and the defoamer pumped from the defoamer storage tank is evenly sprayed on the foam through the spray pipe to achieve chemical defoaming. The purpose; both ends of the mechanical defoaming device are symmetrically installed with foam-breaking nozzles, the foam fluid is sprayed out through the foam-breaking nozzles, and the impact force, shear force and negative pressure are used to achieve mechanical defoaming. By changing the foam-breaking nozzle The number of nozzles and the hole diameter can adjust the defoaming efficiency of the mechanical defoaming device.

所述化学消泡剂添加系统是从泡沫基液罐分流出部分基液,经截止阀、离心泵进入消泡剂储罐,化学消泡剂和泡沫基液在消泡剂储罐中经过搅拌充分混均后,由离心泵、截止阀和压力表进入喷淋管,由此构成化学消泡剂添加系统;通过从泡沫基液罐中引入部分基液将消泡剂稀释,然后从喷淋管进入机械消泡装置,在机械消泡装置中实现化学与机械联合消泡。The chemical defoamer adding system divides part of the base liquid from the foam base liquid tank, enters the defoamer storage tank through a stop valve and a centrifugal pump, and the chemical defoamer and foam base liquid are stirred in the defoamer storage tank After fully mixing, the centrifugal pump, shut-off valve and pressure gauge enter the spray pipe, thus forming a chemical defoamer addition system; the defoamer is diluted by introducing part of the base liquid from the foam base liquid tank, and then sprayed The pipe enters the mechanical defoaming device, where chemical and mechanical combined defoaming is realized.

破泡后的液体从机械消泡装置底部,经离心泵、截止阀,回流到泡沫基液罐,实现泡沫的循环利用。The broken liquid flows back from the bottom of the mechanical defoaming device through the centrifugal pump and stop valve to the foam base liquid tank to realize the recycling of the foam.

本实用新型的有益效果是:1、通过监测取样器出口泡沫质量、半衰期、温度、压力、密度等参数,可实现泡沫性能的快速调节,达到模拟井下高温高压环境的目的;2、模拟实验装置充分利用化学与机械联合消泡的增效作用,克服单一消泡法消泡效率不足的缺点,有利于实现泡沫的循环利用。The beneficial effects of the utility model are: 1. By monitoring the foam quality, half-life, temperature, pressure, density and other parameters at the outlet of the sampler, the rapid adjustment of the foam performance can be realized to achieve the purpose of simulating the high temperature and high pressure environment in the well; 2. The simulation experiment device Make full use of the synergistic effect of combined chemical and mechanical defoaming, overcome the shortcomings of insufficient defoaming efficiency of the single defoaming method, and help realize the recycling of foam.

附图说明 Description of drawings

附图1为本实用新型可循环泡沫模拟实验装置的工艺流程示意图。Accompanying drawing 1 is the process flow diagram of the utility model recyclable foam simulation experiment device.

图中1.泡沫基液罐,2.截止阀,3.计量泵,4.孔板流量计,5.空压机,6.放空阀,7.贮气罐,8.截止阀,9.转子流量计,10.截止阀,11.泡沫发生器,12.出口端的压力表,13.截止阀,14.电缆伴热管,15.热电偶温度计,16.截止阀,17.泡沫取样器,18.出口端的压力表,19.截止阀,20.机械消泡装置,21.破泡喷嘴,22.喷淋管,23.压力表,24.截止阀,25.计量泵,26.消泡剂储罐,27.离心泵,28.截止阀,29.离心泵,30.截止阀。In the figure 1. Foam base liquid tank, 2. Stop valve, 3. Metering pump, 4. Orifice flowmeter, 5. Air compressor, 6. Vent valve, 7. Air storage tank, 8. Stop valve, 9. Rotameter, 10. Stop valve, 11. Foam generator, 12. Pressure gauge at outlet, 13. Stop valve, 14. Cable heating tube, 15. Thermocouple thermometer, 16. Stop valve, 17. Foam sampler, 18. Pressure gauge at the outlet, 19. Stop valve, 20. Mechanical defoaming device, 21. Bubble breaking nozzle, 22. Spray pipe, 23. Pressure gauge, 24. Stop valve, 25. Metering pump, 26. Defoaming Agent storage tank, 27. centrifugal pump, 28. shut-off valve, 29. centrifugal pump, 30. shut-off valve.

具体实施方式 Detailed ways

下面结合附图和实施例对本实用新型作进一步说明。本实用新型一种可循环泡沫模拟实验装置由基液添加系统、供气系统、泡沫加热系统、机械消泡装置系统和化学消泡剂添加系统连接构成,其通过基液添加系统、供气系统、泡沫加热系统、机械消泡装置系统和化学消泡剂添加系统相连形成闭合的整体实验系统。Below in conjunction with accompanying drawing and embodiment the utility model is further described. A recyclable foam simulation experiment device of the utility model is composed of a base liquid addition system, an air supply system, a foam heating system, a mechanical defoaming device system and a chemical defoamer addition system. , foam heating system, mechanical defoaming device system and chemical defoamer adding system are connected to form a closed overall experimental system.

所述基液添加系统由泡沫基液罐1、截止阀2、计量泵3、孔板流量计4依序安装组成;所述供气系统由空压机5、放空阀6、贮气罐7、截止阀8、转子流量计9、截止阀10依序连接安装组成;通过基液添加系统与供气系统形成气液混合流,进入泡沫发生器11;泡沫发生器11出口端安装有压力表12和截止阀13;通过调节进入泡沫发生器11的气液比和压力,可实现模拟泡沫钻井的压力环境的目的。The base liquid addition system is composed of a foam base liquid tank 1, a shut-off valve 2, a metering pump 3, and an orifice flowmeter 4; , stop valve 8, rotameter 9 and stop valve 10 are connected and installed in sequence; a gas-liquid mixed flow is formed through the base liquid addition system and the gas supply system, and enters the foam generator 11; a pressure gauge is installed at the outlet of the foam generator 11 12 and cut-off valve 13; by adjusting the gas-liquid ratio and pressure entering the foam generator 11, the purpose of simulating the pressure environment of foam drilling can be achieved.

所述泡沫加热系统由电缆伴热管14、热电偶温度计15、截止阀16、泡沫取样器17连接组成:泡沫取样器17的出口端安装有压力表18和截止阀19;通过调节电缆伴热管14的温度可以达到模拟井下高温环境的目的,泡沫取样器17可用来实时监测泡沫质量、半衰期、温度、压力、密度等参数。The foam heating system is composed of a cable heating pipe 14, a thermocouple thermometer 15, a shut-off valve 16, and a foam sampler 17: a pressure gauge 18 and a shut-off valve 19 are installed at the outlet of the foam sampler 17; The temperature can achieve the purpose of simulating the downhole high temperature environment, and the foam sampler 17 can be used to monitor parameters such as foam quality, half-life, temperature, pressure, and density in real time.

所述机械消泡装置系统是在机械消泡装置20的顶部安装有喷淋管22,从消泡剂储罐26中泵送出的消泡剂,通过喷淋管22均匀喷洒到泡沫上,达到化学消泡的目的;机械消泡装置20的两端对称安装有破泡喷嘴21,泡沫流体通过破泡喷嘴21喷出,利用其冲击力、剪切力及产生负压来实现机械消泡,通过改变破泡喷嘴21的喷嘴数量和孔径,可以调节机械消泡装置20的消泡效率。The mechanical defoaming device system is that a spray pipe 22 is installed on the top of the mechanical defoaming device 20, and the defoamer pumped out from the defoamer storage tank 26 is evenly sprayed onto the foam by the spray pipe 22, To achieve the purpose of chemical defoaming; the two ends of the mechanical defoaming device 20 are symmetrically installed with foam-breaking nozzles 21, and the foam fluid is sprayed out through the foam-breaking nozzles 21, and the mechanical defoaming is realized by using its impact force, shear force and negative pressure , the defoaming efficiency of the mechanical defoaming device 20 can be adjusted by changing the nozzle number and aperture of the foam breaking nozzle 21 .

所述化学消泡剂添加系统是从泡沫基液罐1分流出部分基液,经截止阀28、离心泵27进入消泡剂储罐26,化学消泡剂和泡沫基液在消泡剂储罐26中经过搅拌充分混均后,由离心泵25、截止阀24和压力表23进入喷淋管22,由此构成化学消泡剂添加系统;通过从泡沫基液罐1中引入部分基液将消泡剂稀释,然后从喷淋管22进入机械消泡装置20,在机械消泡装置20中实现化学与机械联合消泡。破泡后的液体从机械消泡装置20底部,经离心泵29、截止阀30,回流到泡沫基液罐1,实现泡沫的循环利用。The chemical defoamer addition system is to flow out part of the base liquid from the foam base liquid tank 1, and enter the defoamer storage tank 26 through the stop valve 28 and the centrifugal pump 27, and the chemical defoamer and the foam base liquid are stored in the defoamer storage After stirring and fully mixing in the tank 26, the centrifugal pump 25, the shut-off valve 24 and the pressure gauge 23 enter the spray pipe 22, thereby forming a chemical defoamer addition system; by introducing part of the base liquid from the foam base liquid tank 1 The defoaming agent is diluted, and then enters the mechanical defoaming device 20 from the spray pipe 22, and the combined chemical and mechanical defoaming is realized in the mechanical defoaming device 20. The broken liquid flows back from the bottom of the mechanical defoaming device 20 through the centrifugal pump 29 and the shut-off valve 30 to the foam base liquid tank 1 to realize recycling of the foam.

工作原理:working principle:

在泡沫基液罐1中预先配制一定浓度的稳定泡沫,泡沫基液由截止阀2、离心泵3、孔板流量计4进入孔隙式泡沫发生器11,空气经由空压机5、贮气罐7、截止阀8、转子流量计9、截止阀10进入孔隙式泡沫发生器11。调节气体流量为1.5m3/min,液体流量为17.81/min,此时气液比为84.3。从孔隙式泡沫发生器11出口端的压力表12和截止阀13流出的泡沫进入泡沫加热系统。经电缆伴热管14加热后,热电偶温度计15测得泡沫温度为81℃,室内测得泡沫取样器17中泡沫质量为86.2%,泡沫半衰期为45min,泡沫取样器17的出口端压力表18的读数为1.3MPa。A certain concentration of stable foam is pre-prepared in the foam base liquid tank 1. The foam base liquid enters the porous foam generator 11 through the stop valve 2, the centrifugal pump 3, and the orifice flowmeter 4, and the air passes through the air compressor 5 and the air storage tank. 7. Stop valve 8, rotameter 9, and stop valve 10 enter the porous foam generator 11. Adjust the gas flow rate to 1.5m 3 /min, the liquid flow rate to 17.81/min, and the gas-liquid ratio at this time is 84.3. The foam flowing out from the pressure gauge 12 and the shut-off valve 13 at the outlet end of the porous foam generator 11 enters the foam heating system. After being heated by the cable heating pipe 14, the foam temperature measured by the thermocouple thermometer 15 is 81° C., and the foam quality in the foam sampler 17 measured indoors is 86.2%, and the foam half-life is 45 minutes. The reading is 1.3MPa.

从泡沫取样器17出口端的压力表18和截止阀19流出的高温、高压泡沫进入机械消泡装置系统。机械消泡装置20的两端分别对称安装有10个直径为2mm的喷嘴。The high-temperature, high-pressure foam flowing out from the pressure gauge 18 at the outlet end of the foam sampler 17 and the shut-off valve 19 enters the mechanical defoaming device system. Ten nozzles with a diameter of 2 mm are respectively symmetrically installed on both ends of the mechanical defoaming device 20 .

从泡沫基液罐1分流出部分基液,经截止阀28、离心泵27进入消泡剂储罐26,在消泡剂储罐26中添加有化学消泡剂,化学消泡剂和泡沫基液在消泡剂储罐26中经过搅拌充分混合后,由计量泵25、截止阀24和压力表23进入喷淋管22,通过喷淋管22将化学消泡剂均匀喷洒到泡沫上,实现化学消泡的目的。Part of the base liquid flows out from the foam base liquid tank 1, and enters the defoamer storage tank 26 through the stop valve 28 and the centrifugal pump 27. In the defoamer storage tank 26, a chemical defoamer, chemical defoamer and foam base are added. After the liquid is stirred and fully mixed in the defoamer storage tank 26, it enters the spray pipe 22 through the metering pump 25, the stop valve 24 and the pressure gauge 23, and sprays the chemical defoamer evenly on the foam through the spray pipe 22 to realize The purpose of chemical defoaming.

测试结果显示:单一机械消泡率为60.5%,单一化学消泡率为85.0%,在机械消泡装置20中实现化学与机械联合消泡,消泡率可达97.0%,余下的泡沫在机械消泡装置20中实现自然消泡。破泡后的液体从机械消泡装置20底部,经离心泵29、截止阀30,回流到泡沫基液罐1,实现泡沫的循环利用。The test results show that the single mechanical defoaming rate is 60.5%, the single chemical defoaming rate is 85.0%, and the combined chemical and mechanical defoaming is realized in the mechanical defoaming device 20, and the defoaming rate can reach 97.0%. Natural defoaming is realized in the defoaming device 20. The broken liquid flows back from the bottom of the mechanical defoaming device 20 through the centrifugal pump 29 and the shut-off valve 30 to the foam base liquid tank 1 to realize recycling of the foam.

Claims (4)

1. a foam analogue experiment installation capable of circulation is made of base fluid add-on system, air supply system, foam heating system, mechanical defoaming device system and chemical defoamer add-on system, it is characterized in that: linking to each other by base fluid add-on system, air supply system, foam heating system, mechanical defoaming device system and chemical defoamer add-on system forms closed integral experiment system; Described mechanical defoaming device system is equipped with shower (22) at the top of mechanical defoaming device (20), and the defoamer that pumps out from defoamer storage tank (26) evenly is sprayed onto on the foam by shower (22), realizes the effect of chemical froth breaking; Described chemical defoamer add-on system is to distribute the part base fluid from foam base fluid jar (1), enter defoamer storage tank (26) through stop valve (28), centrifugal pump (27), chemical defoamer and foam base fluid process in defoamer storage tank (26) enters shower (22) by centrifugal pump (25), stop valve (24) and pressure meter (23) after stirring and fully being mixed.By from foam base fluid jar (1), introducing the part base fluid defoamer is diluted, enter mechanical defoaming device (20) from shower (22) then, in mechanical defoaming device (20), realize chemistry and mechanically combining froth breaking.
2. a kind of foam analogue experiment installation capable of circulation according to claim 1 is characterized in that: described base fluid add-on system is installed in regular turn by foam base fluid jar (1), stop valve (2), measuring pump (3), orifice flowmeter (4) and is formed; Described air supply system is made up of air compressor machine (5), atmospheric valve (6), gas tank (7), stop valve (8), spinner flowmeter (9), stop valve (10) connection in regular turn; Form gas-liquid mixed stream by base fluid add-on system and air supply system, enter foam maker (11); Foam maker (11) port of export is equipped with pressure meter (12) and stop valve (13); Enter the gas liquid ratio and the pressure of foam maker (11) by adjusting, can realize simulating the purpose of the pressure environment of foam drilling.
3. a kind of foam analogue experiment installation capable of circulation according to claim 1 is characterized in that: described foam heating system is connected to form by cable heat tracing pipe (14), thermocouple thermometer (15), stop valve (16), foam sampler (17); The port of export of foam sampler (17) is equipped with pressure meter (18) and stop valve (19); Can reach the purpose of hot environment under the simulation well by the temperature of regulating cable heat tracing pipe (14), foam sampler (17) can be used to monitor in real time parameters such as foam quality, half-life, temperature, pressure, density.
4. a kind of foam analogue experiment installation capable of circulation according to claim 1, it is characterized in that: the two ends of mechanical defoaming device (20) are symmetrically installed with brokenly bubble nozzle (21), aerated fluid is by broken bubble nozzle (21) ejection, utilize its impact force, shearing force and produce negative pressure and realize mechanical defoaming, by changing brokenly the nozzle quantity and the aperture of bubble nozzle (21), can regulate the defoaming effectiveness of mechanical defoaming device (20).
CNU200820141304XU 2008-11-07 2008-11-07 Circulating foam simulation experiment apparatus Expired - Fee Related CN201284636Y (en)

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* Cited by examiner, † Cited by third party
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CN101871330A (en) * 2010-07-20 2010-10-27 西南石油大学 Foam recycling method for realizing foam drilling by using low-carbon alcohol
CN101975716A (en) * 2010-09-10 2011-02-16 长沙理工大学 Device for testing foaming performance of foam asphalt
CN101701902B (en) * 2009-11-20 2011-06-22 同济大学 Theoretical Calculation Method of Expansion Rate and Half-life of Foamed Asphalt
CN103195372A (en) * 2013-04-24 2013-07-10 中国水电顾问集团中南勘测设计研究院 Spiral drill bit, foam drilling device and foam drilling process
CN104931655A (en) * 2015-06-15 2015-09-23 中铁十一局集团第五工程有限公司 Foam generating testing equipment allowing foam quality to be adjusted
CN111359266A (en) * 2020-04-09 2020-07-03 北京国电龙源环保工程有限公司 System for defoaming slurry outside desulfurization absorption tower and measuring density and construction method
CN115902171A (en) * 2022-12-11 2023-04-04 西南石油大学 Drilling Foam Fluid Carrying Rock Simulation Device with Temperature Control Function for Laboratory
CN116622347A (en) * 2023-05-26 2023-08-22 中煤科工集团重庆研究院有限公司 A micro-bubble drilling fluid for coal mines and its recycling method and system

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101701902B (en) * 2009-11-20 2011-06-22 同济大学 Theoretical Calculation Method of Expansion Rate and Half-life of Foamed Asphalt
CN101871330A (en) * 2010-07-20 2010-10-27 西南石油大学 Foam recycling method for realizing foam drilling by using low-carbon alcohol
CN101975716A (en) * 2010-09-10 2011-02-16 长沙理工大学 Device for testing foaming performance of foam asphalt
CN101975716B (en) * 2010-09-10 2012-01-11 长沙理工大学 Device for testing foaming performance of foam asphalt
CN103195372A (en) * 2013-04-24 2013-07-10 中国水电顾问集团中南勘测设计研究院 Spiral drill bit, foam drilling device and foam drilling process
CN103195372B (en) * 2013-04-24 2016-08-17 中国电建集团中南勘测设计研究院有限公司 A kind of screw type bit and a kind of foam drilling device and foam drilling technique
CN104931655A (en) * 2015-06-15 2015-09-23 中铁十一局集团第五工程有限公司 Foam generating testing equipment allowing foam quality to be adjusted
CN104931655B (en) * 2015-06-15 2016-08-17 中铁十一局集团第五工程有限公司 The foam of adjustable foam quality produces testing equipment
CN111359266A (en) * 2020-04-09 2020-07-03 北京国电龙源环保工程有限公司 System for defoaming slurry outside desulfurization absorption tower and measuring density and construction method
CN111359266B (en) * 2020-04-09 2022-04-22 国能龙源环保有限公司 System for defoaming slurry outside desulfurization absorption tower and measuring density and construction method
CN115902171A (en) * 2022-12-11 2023-04-04 西南石油大学 Drilling Foam Fluid Carrying Rock Simulation Device with Temperature Control Function for Laboratory
CN116622347A (en) * 2023-05-26 2023-08-22 中煤科工集团重庆研究院有限公司 A micro-bubble drilling fluid for coal mines and its recycling method and system

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