CN202645476U - Mud purification desander - Google Patents
Mud purification desander Download PDFInfo
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- CN202645476U CN202645476U CN 201120567864 CN201120567864U CN202645476U CN 202645476 U CN202645476 U CN 202645476U CN 201120567864 CN201120567864 CN 201120567864 CN 201120567864 U CN201120567864 U CN 201120567864U CN 202645476 U CN202645476 U CN 202645476U
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- 238000000746 purification Methods 0.000 title claims description 11
- 239000004576 sand Substances 0.000 claims abstract description 9
- 239000004744 fabric Substances 0.000 claims description 8
- 238000005553 drilling Methods 0.000 abstract description 10
- 239000002002 slurry Substances 0.000 abstract description 9
- 238000004537 pulping Methods 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- 238000005299 abrasion Methods 0.000 abstract 1
- 239000007790 solid phase Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 239000002245 particle Substances 0.000 description 7
- 238000000926 separation method Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000000440 bentonite Substances 0.000 description 2
- 229910000278 bentonite Inorganic materials 0.000 description 2
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种泥浆净化除砂器。 The utility model relates to a mud purifying desander. the
背景技术 Background technique
泥浆中的固相按其作用可分为两类:一类是有用固相,如膨润土、化学处理剂、重晶石粉等;另一类是无用固相,如钻屑、劣质膨润土、砂粒等。所谓钻井液固相控制,就是要消除有害固相,保存有用固相,以满足钻井工艺对钻井液性能的要求。目前,有四种常用的降低泥浆中固相含量的方法:第一种是用清水稀释钻井液,此方法只是单方面降低了泥浆中的固相含量,并没用将泥浆中的无用固相完全排除泥浆体系;第二种是用清水和性能合格的新泥浆来替换井内泥浆,此方法既增加了废浆排放量,加重了环境污染,又浪费了泥浆材料,增加了泥浆成本;第三种是利用固体的重力,让固体在沉砂池中自己沉落分离,此方法会破坏泥浆性能;第四种是用机械净化法,此方法较以上三种方法除砂效果明显,但是由于钻井工艺的不同,故存在成本高、操作不方便、普及度低的缺陷。 The solid phase in the mud can be divided into two types according to its function: one is useful solid phase, such as bentonite, chemical treatment agent, barite powder, etc.; the other is useless solid phase, such as drill cuttings, inferior bentonite, sand, etc. . The so-called solid phase control of drilling fluid is to eliminate harmful solid phase and preserve useful solid phase to meet the requirements of drilling technology for drilling fluid performance. At present, there are four commonly used methods to reduce the solid phase content in the mud: the first is to dilute the drilling fluid with clean water, this method only unilaterally reduces the solid phase content in the mud, and does not use the useless solid phase in the mud Completely eliminate the mud system; the second is to replace the mud in the well with clean water and new mud with qualified performance. This method not only increases the discharge of waste mud, aggravates environmental pollution, but also wastes mud materials and increases mud costs; third. The first is to use the gravity of the solid to let the solid settle and separate in the grit chamber. This method will destroy the performance of the mud; the fourth is to use the mechanical purification method. This method is more effective in removing sand than the above three methods, but due to drilling Due to the difference in technology, there are defects such as high cost, inconvenient operation, and low popularity. the
发明内容 Contents of the invention
本实用新型的目的在于提出一种旋流分离、筛网分离相结合的泥浆净化除砂器。 The purpose of the utility model is to propose a mud purification and desander combining cyclone separation and screen mesh separation. the
本实用新型的目的是这样实现的:泥浆净化除砂器包含三个过滤装置,一、二级过滤装置由两个串联的旋流除砂器组成,其固定在机架上部,三级过滤装置为振动筛,其设置在一、二级过滤装置下方,机架下部。一级旋流除砂器的溢流管与二级旋流除砂器的进浆管连通,两旋流除砂器的排砂口正对振动筛的筛网中部。 The purpose of this utility model is achieved in this way: the mud purification desander includes three filter devices, the first and second filter devices are composed of two series-connected swirl desanders, which are fixed on the upper part of the frame, and the third filter device It is a vibrating screen, which is set under the primary and secondary filter devices and the lower part of the frame. The overflow pipe of the primary cyclone desander is connected with the slurry inlet pipe of the secondary cyclone desander, and the sand discharge ports of the two cyclone desanders are facing the middle of the screen of the vibrating screen. the
由于实施上述技术方案,泥浆经本实用新型经净化后,使泥浆中的含砂量降低了70%,泥浆的优良性能得到了保证,平均台月效率提高了21.3%,提高了钻井效率,降低了泥浆泵易损件(缸套、活塞、凡尔体)的消耗;减小了钻杆、钻具的磨损,并降低了制浆材料、制浆用水的消耗,降低泥浆成本42.6%,同时减少了废浆排放量,减轻了环境污染。 Due to the implementation of the above-mentioned technical scheme, after the mud is purified by the utility model, the sand content in the mud is reduced by 70%, the excellent performance of the mud is guaranteed, the average platform efficiency is increased by 21.3%, the drilling efficiency is improved, and the drilling efficiency is reduced. Reduced the consumption of mud pump wearing parts (cylinder liner, piston, valve body); reduced the wear of drill pipes and drilling tools, reduced the consumption of pulping materials and water for pulping, and reduced the cost of mud by 42.6%. The discharge of waste pulp is reduced, and the environmental pollution is reduced. the
附图说明:本实用新型的具体结构由以下的附图和实施例给出: Description of drawings: the concrete structure of the present utility model is provided by following accompanying drawing and embodiment:
图1是泥浆净化除砂器结构示意图。 Figure 1 is a schematic diagram of the structure of the mud purification desander.
图例:1、旋流除砂器,2、机架,3、振动轴,4、粗目筛网,5、细目筛网,6、导流槽,7、弹簧,8、振动筛,9、电动机。 Legend: 1. Cyclone desander, 2. Frame, 3. Vibrating shaft, 4. Coarse mesh screen, 5. Fine mesh screen, 6. Diversion groove, 7. Spring, 8. Vibrating screen, 9. Motor . the
具体实施方式: Detailed ways:
本实用新型不受下述实施例的限制,可根据本实用新型的技术方案与实际情况来确定具体的实施方式。 The utility model is not limited by the following examples, and the specific implementation manner can be determined according to the technical scheme of the utility model and actual conditions.
实施例:如图1所示,泥浆净化除砂器包含三个过滤装置,一、二级过滤装置由两个串联的旋流除砂器1组成,其固定在机架2上部,三级过滤装置为振动筛8,其设置在一、二级过滤装置下方,机架2下部。一级旋流除砂器的溢流管与二级旋流除砂器的进浆管连通,两旋流除砂器1的排砂口正对振动筛8的筛网中部。 Embodiment: As shown in Figure 1, the mud purification desander includes three filter devices, the primary and secondary filter devices are composed of two series-connected cyclone desanders 1, which are fixed on the top of the frame 2, and the three-stage filter The device is a vibrating screen 8, which is arranged below the primary and secondary filter devices and the bottom of the frame 2. The overflow pipe of the primary cyclone desander communicates with the slurry inlet pipe of the secondary cyclone desander, and the sand outlets of the two cyclone desanders 1 face the middle of the screen of the vibrating screen 8 . the
旋流除砂器为已经技术,其由壳体,设置在壳体上端的溢流管,与壳体圆周呈切线方向连通的进浆管,以及设置在壳体内的转动装置组成。壳体内分为上部的圆腔和下部的锥形腔,锥形腔下端开口,即为排砂口。任何一种旋流除砂器都有一定的固体分离粒径和净度。例如,某一种旋流除砂器的分离粒径60微米,净度95%,即表示这种旋流除砂器可把大于60微米的固体分离出95%。本实用新型中,可根据具体的使用要求选择不同的旋流除砂器。 The cyclone desander is an existing technology, which consists of a shell, an overflow pipe arranged at the upper end of the shell, a slurry inlet pipe connected to the circumference of the shell in a tangential direction, and a rotating device arranged in the shell. The shell is divided into an upper circular cavity and a lower conical cavity, and the lower end of the conical cavity is open, which is the sand discharge port. Any kind of cyclone desander has a certain solid separation particle size and clarity. For example, a certain cyclone desander has a separation particle size of 60 microns and a purity of 95%, which means that this cyclone desander can separate 95% of solids larger than 60 microns. In the utility model, different cyclone desanders can be selected according to specific usage requirements. the
振动筛8由筛架,以及设置在筛架内的筛网,和设置在筛网下的导流槽6组成,在筛架内上部横穿有振动轴3,振动轴3一侧设置有装设有偏心块的皮带轮,该皮带轮由固定在机架2上的电动机9带动。振动筛8坐于机架2上的底座处,振动筛8底部四角与底座四角间连接有弹簧7。振动筛8内部平铺至少两层筛网,由上至下筛网目数递增。当为两层筛网时,上层为粗目筛网4,下层为细目筛网5。
The vibrating screen 8 is composed of a screen frame, a screen cloth arranged in the screen cloth, and a
泥浆净化时,两个串联的旋流除砂器1将泥浆分离成低密度的溢流和高密度的底流,其中溢流由二级旋流除砂器的溢流管返回泥浆循环系统,底流落在振动筛8上。随后,振动筛8的上层粗目筛网4将高密度的底流再分离成两部分,一部分是浆液和小于网孔的颗粒透过粗目筛网4落向细目筛网5;另一部分是大于网孔的颗粒从粗目筛网4上被排出。最后,振动筛8的下层细目筛网5将含有颗粒的浆液再次进行分离,浆液和小于网孔的颗粒透过细目筛网5经导流槽6返回泥浆循环系统;另一部分是大于网孔的颗粒从细目筛网5上被排出。
During mud purification, two series cyclone desanders 1 separate the mud into low-density overflow and high-density underflow, where the overflow is returned to the mud circulation system by the overflow pipe of the secondary cyclone desander, and the bottom flow It falls on the vibrating screen 8. Subsequently, the upper coarse-mesh screen 4 of the vibrating screen 8 separates the high-density underflow into two parts, one part is the slurry and the particles smaller than the mesh pass through the coarse-mesh screen 4 and fall to the fine-mesh screen 5; the other part is larger than the mesh. The particles are discharged from the coarse screen 4. Finally, the fine-mesh screen 5 of the lower layer of the vibrating screen 8 separates the slurry containing particles again, and the slurry and particles smaller than the mesh pass through the fine-mesh screen 5 and return to the mud circulation system through the
以上技术特征构成了本实用新型的最佳实施例,其具有较强的适应性和最佳实施效果,可根据实际需要增减非必要技术特征,来满足不同情况的需要。 The above technical features constitute the best embodiment of the utility model, which has strong adaptability and best implementation effect, and non-essential technical features can be increased or decreased according to actual needs to meet the needs of different situations.
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CN 201120567864 CN202645476U (en) | 2011-12-30 | 2011-12-30 | Mud purification desander |
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CN 201120567864 CN202645476U (en) | 2011-12-30 | 2011-12-30 | Mud purification desander |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105457393A (en) * | 2015-12-31 | 2016-04-06 | 天津厚普德科技有限公司 | Sewage treatment equipment with gravel filtering mechanism |
CN105642013A (en) * | 2015-12-31 | 2016-06-08 | 天津厚普德科技有限公司 | Double-effect sewage treatment and grit removal system |
CN109339724A (en) * | 2018-12-26 | 2019-02-15 | 中国石油大学(华东) | A drilling fluid desilting and sand removal device |
CN109432851A (en) * | 2018-12-27 | 2019-03-08 | 中交公局第二工程有限公司 | A kind of packaged type filtering slurry circulator |
-
2011
- 2011-12-30 CN CN 201120567864 patent/CN202645476U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105457393A (en) * | 2015-12-31 | 2016-04-06 | 天津厚普德科技有限公司 | Sewage treatment equipment with gravel filtering mechanism |
CN105642013A (en) * | 2015-12-31 | 2016-06-08 | 天津厚普德科技有限公司 | Double-effect sewage treatment and grit removal system |
CN109339724A (en) * | 2018-12-26 | 2019-02-15 | 中国石油大学(华东) | A drilling fluid desilting and sand removal device |
CN109432851A (en) * | 2018-12-27 | 2019-03-08 | 中交公局第二工程有限公司 | A kind of packaged type filtering slurry circulator |
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Granted publication date: 20130102 Termination date: 20141230 |
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