CN117414727A - Preparation method and device for clean fracturing fluid - Google Patents
Preparation method and device for clean fracturing fluid Download PDFInfo
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- CN117414727A CN117414727A CN202311310492.XA CN202311310492A CN117414727A CN 117414727 A CN117414727 A CN 117414727A CN 202311310492 A CN202311310492 A CN 202311310492A CN 117414727 A CN117414727 A CN 117414727A
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- 239000012530 fluid Substances 0.000 title claims abstract description 152
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 116
- 238000002156 mixing Methods 0.000 claims abstract description 66
- 238000003756 stirring Methods 0.000 claims abstract description 57
- 238000012216 screening Methods 0.000 claims abstract description 55
- 238000006243 chemical reaction Methods 0.000 claims abstract description 47
- 238000010438 heat treatment Methods 0.000 claims abstract description 41
- 239000012535 impurity Substances 0.000 claims abstract description 37
- 238000001179 sorption measurement Methods 0.000 claims abstract description 16
- 238000001914 filtration Methods 0.000 claims abstract description 12
- 238000003825 pressing Methods 0.000 claims abstract 28
- 238000007599 discharging Methods 0.000 claims abstract 3
- 239000002994 raw material Substances 0.000 claims description 22
- 239000002699 waste material Substances 0.000 claims description 18
- 230000002457 bidirectional effect Effects 0.000 claims description 16
- 238000004064 recycling Methods 0.000 claims description 14
- 239000012528 membrane Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 238000002347 injection Methods 0.000 claims description 9
- 239000007924 injection Substances 0.000 claims description 9
- 238000001125 extrusion Methods 0.000 claims description 7
- 238000007790 scraping Methods 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 4
- 238000011084 recovery Methods 0.000 claims description 4
- 230000009471 action Effects 0.000 claims description 3
- 239000000523 sample Substances 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 230000003247 decreasing effect Effects 0.000 claims 1
- 239000011148 porous material Substances 0.000 claims 1
- 238000007873 sieving Methods 0.000 claims 1
- 230000035699 permeability Effects 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 description 13
- 239000007788 liquid Substances 0.000 description 9
- 229920002907 Guar gum Polymers 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 5
- 239000000665 guar gum Substances 0.000 description 5
- 229960002154 guar gum Drugs 0.000 description 5
- 235000010417 guar gum Nutrition 0.000 description 5
- 239000000376 reactant Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- ZRALSGWEFCBTJO-UHFFFAOYSA-N Guanidine Chemical compound NC(N)=N ZRALSGWEFCBTJO-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 229920001938 Vegetable gum Polymers 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 239000003899 bactericide agent Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- ZYGHJZDHTFUPRJ-UHFFFAOYSA-N coumarin Chemical compound C1=CC=C2OC(=O)C=CC2=C1 ZYGHJZDHTFUPRJ-UHFFFAOYSA-N 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 230000001934 delay Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 239000003129 oil well Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000002562 thickening agent Substances 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 102000008186 Collagen Human genes 0.000 description 1
- 108010035532 Collagen Proteins 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- CHJJGSNFBQVOTG-UHFFFAOYSA-N N-methyl-guanidine Natural products CNC(N)=N CHJJGSNFBQVOTG-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229920001436 collagen Polymers 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 229960000956 coumarin Drugs 0.000 description 1
- 235000001671 coumarin Nutrition 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- SWSQBOPZIKWTGO-UHFFFAOYSA-N dimethylaminoamidine Natural products CN(C)C(N)=N SWSQBOPZIKWTGO-UHFFFAOYSA-N 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/02—Combinations of filters of different kinds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/80—After-treatment of the mixture
- B01F23/808—Filtering the mixture
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
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Abstract
Description
技术领域Technical field
本发明涉及一种清洁压裂液的制备方法和装置,属于压裂液制备装置技术领域。The invention relates to a preparation method and device for clean fracturing fluid, belonging to the technical field of fracturing fluid preparation devices.
背景技术Background technique
压裂液在压裂施工中起到传递压力和携带支撑剂的作用,目前国内外广泛使用的压裂液是以天然植物胶为稠化剂的水基压裂液,水基压裂液由聚合物稠化剂(植物胶、胍胶、香豆胶等)、交联剂、破胶剂、pH值调节剂、杀菌剂、粘土稳定剂和助排剂等组成,多为交联凝胶体系,加入添加剂帮助保护地层,比较经济,适于连续或批量混合,适用于油井、气井、注水井,也适用于砂岩或灰岩地层;其中以胍胶衍生物为代表的植物胶压裂液体系占整个压裂液的90%,一直在提高油气井采收率方面发挥着重要作用;但胍胶原粉的水不溶残渣含量偏大(约19%-25%),其冻胶破胶后含残渣较高,可达到7%-10%,因此现有的压裂液在制备过程中,仅对反应原料中的杂质进行过滤,其制备的水基压裂液中的残渣含量仍然较高,会导致储层渗透率和裂缝的导流能力下降。Fracturing fluid plays the role of transmitting pressure and carrying proppant during fracturing construction. Currently, the fracturing fluid widely used at home and abroad is water-based fracturing fluid with natural vegetable gum as the thickener. Water-based fracturing fluid is made of It is composed of polymer thickener (vegetable gum, guar gum, coumarin gum, etc.), cross-linking agent, gel breaker, pH adjuster, bactericide, clay stabilizer and drainage aid, mostly cross-linked gel. The system, adding additives to help protect the formation, is relatively economical, suitable for continuous or batch mixing, suitable for oil wells, gas wells, water injection wells, and also suitable for sandstone or limestone formations; among them, plant gum fracturing liquids represented by guar gum derivatives It accounts for 90% of the entire fracturing fluid and has been playing an important role in improving oil and gas well recovery; however, the water-insoluble residue content of guanidine collagen powder is relatively large (about 19%-25%), and after the gel breaks The residue content is relatively high, which can reach 7%-10%. Therefore, during the preparation process of existing fracturing fluids, only the impurities in the reaction raw materials are filtered, and the residue content in the water-based fracturing fluid prepared is still relatively high. , which will lead to a decrease in reservoir permeability and fracture conductivity.
发明内容Contents of the invention
有鉴于此,本发明的目的在于提供一种清洁压裂液的制备方法和装置,以解决现有技术中所提到的技术问题。In view of this, the object of the present invention is to provide a preparation method and device for clean fracturing fluid to solve the technical problems mentioned in the prior art.
一种清洁压裂液的制备装置,包括:A preparation device for clean fracturing fluid, including:
反应釜,所述反应釜的内部由上往下依次设置有混合腔室、筛分腔室和压滤腔室,所述混合腔室与所述筛分腔室之间设置有一级出料口,所述筛分腔室与所述压滤腔室之间设置有二级出料口,所述一级出料口内安装有第一电子阀;Reaction kettle, the interior of the reaction kettle is provided with a mixing chamber, a screening chamber and a filter pressure chamber in order from top to bottom, and a first-level discharge port is provided between the mixing chamber and the screening chamber. , a secondary discharge port is provided between the screening chamber and the filter press chamber, and a first electronic valve is installed in the primary discharge port;
所述混合腔室内设置有加热搅拌组件,所述加热搅拌组件用于对加入所述混合腔室内的反应原料进行加热、搅拌,使得所述混合腔室内的反应原料充分混合后,得到水基压裂液,并进行破胶反应;The mixing chamber is provided with a heating and stirring component. The heating and stirring component is used to heat and stir the reaction raw materials added to the mixing chamber, so that the reaction raw materials in the mixing chamber are fully mixed to obtain a water-based pressure. Crack the liquid and perform gel breaking reaction;
所述筛分腔室内设置有筛分组件,所述筛分组件用于对所述水基压裂液中的部分不溶物杂质进行过滤,并将过滤后的不溶物排出到所述反应釜外;A screening assembly is provided in the screening chamber. The screening assembly is used to filter some insoluble impurities in the water-based fracturing fluid and discharge the filtered insoluble matter out of the reaction kettle. ;
所述压滤腔室内设置有压滤组件,所述压滤组件的底部预留有缓冲槽,所述压滤组件用于对所述水基压裂液中的剩余不溶物杂质进行吸附过滤,得到清洁压裂液,并将所述清洁压裂液压入所述缓冲槽内,进行储存;A filter press component is provided in the filter press chamber, and a buffer tank is reserved at the bottom of the filter press component. The filter press component is used to adsorb and filter the remaining insoluble impurities in the water-based fracturing fluid. Obtain clean fracturing fluid, and pour the clean fracturing fluid into the buffer tank for storage;
驱动单元,所述驱动单元用于驱动所述搅拌组件、所述筛分组件和所述压滤组件进行同步转动;A driving unit, the driving unit is used to drive the stirring assembly, the screening assembly and the filter press assembly to rotate synchronously;
控制单元,所述控制单元分别与所述第一电子阀和所述驱动单元连接,用于控制所述第一电子阀的启闭,以及控制所述驱动单元的启停。A control unit, the control unit is respectively connected to the first electronic valve and the driving unit, and is used to control the opening and closing of the first electronic valve, and to control the starting and stopping of the driving unit.
可选地,所述加热搅拌组件包括:Optionally, the heating stirring assembly includes:
搅拌杆,所述搅拌杆的一端贯穿所述混合腔室的顶端,并延伸至所述反应釜的外侧与所述驱动单元的输出端连接,所述搅拌杆的另一端与所述混合腔室的底端转动连接;Stirring rod, one end of the stirring rod penetrates the top of the mixing chamber and extends to the outside of the reaction kettle to be connected to the output end of the drive unit, and the other end of the stirring rod is connected to the mixing chamber The bottom end of the rotary connection;
若干搅拌叶片,若干所述搅拌叶片环形均匀安装在所述搅拌杆的外表面上,每一所述搅拌叶片的结构均为弧形滤板;A plurality of stirring blades, a plurality of stirring blades are evenly installed on the outer surface of the stirring rod in an annular shape, and the structure of each stirring blade is an arc-shaped filter plate;
若干加热板,若干所述加热板均匀安装在所述混合腔室的侧壁上,所述搅拌叶片在旋转过程中与所述加热板之间留有间隙;A plurality of heating plates, which are evenly installed on the side walls of the mixing chamber, leaving a gap between the stirring blades and the heating plates during rotation;
温度传感器,所述温度传感器的探头安装在所述混合腔室的底端;A temperature sensor, the probe of which is installed at the bottom end of the mixing chamber;
所述加热板和所述温度传感器分别与所述控制单元连接。The heating plate and the temperature sensor are respectively connected to the control unit.
可选地,所述筛分组件包括:Optionally, the screening components include:
转轴,所述转轴的一端贯穿所述筛分腔室的顶端与所述搅拌杆连接,所述转轴的另一端与所述筛分腔室的底端转动连接;A rotating shaft, one end of the rotating shaft passes through the top of the screening chamber and is connected to the stirring rod, and the other end of the rotating shaft is rotationally connected to the bottom end of the screening chamber;
若干锥形滤筒,若干所述锥形滤筒沿竖直方向并列安装在所述筛分腔室内,且若干所述锥形滤筒的滤孔孔径由上往下依次递减,每一所述锥形滤筒的开口端均朝下设置,所述锥形滤筒的中部套设在所述转轴的外表面上,所述锥形滤筒的底端一侧安装在所述筛分腔室的侧壁上;Several conical filter cartridges are installed side by side in the screening chamber along the vertical direction, and the filter hole diameters of the several conical filter cartridges decrease in sequence from top to bottom, and each of the conical filter cartridges The open ends of the conical filter cylinder are all set downward, the middle part of the conical filter cylinder is sleeved on the outer surface of the rotating shaft, and the bottom end of the conical filter cylinder is installed in the screening chamber. on the side wall;
废料回收箱,所述废料回收箱安装在所述反应釜的外侧壁上;A waste recycling box, which is installed on the outer wall of the reactor;
所述筛分腔室的侧壁上靠近所述锥形滤筒底部的一侧设置有若干排料口,若干所述排料口分别与所述废料回收箱的内部连通,所述排料口的高度大于所述锥形滤筒的壁厚,所述排料口的底端与所述锥形滤筒的底端平齐;A number of discharge openings are provided on the side wall of the screening chamber close to the bottom of the conical filter cartridge. Several of the discharge openings are respectively connected with the inside of the waste recycling box. The discharge openings The height is greater than the wall thickness of the conical filter cartridge, and the bottom end of the discharge port is flush with the bottom end of the conical filter cartridge;
每一所述锥形滤筒的顶端一侧均平行设置有刮板,所述刮板的一端安装在所述转轴的外表面上,所述刮板的另一端与所述锥形滤筒的侧壁滑动连接;所述刮板将所述锥形滤筒表面过滤后的不溶物杂质刮入到所述排料口内,并从所述排料口排放到所述废料回收箱内;A scraper is arranged parallel to the top side of each conical filter cartridge. One end of the scraper is installed on the outer surface of the rotating shaft, and the other end of the scraper is in contact with the conical filter cartridge. The side walls are slidingly connected; the scraper scrapes the filtered insoluble impurities on the surface of the conical filter cylinder into the discharge port, and discharges them from the discharge port into the waste recycling box;
每一所述排料口处均安装有第二电子阀,所述第二电子阀与所述控制单元连接。A second electronic valve is installed at each discharge port, and the second electronic valve is connected to the control unit.
可选地,所述压滤组件包括:Optionally, the filter press assembly includes:
双向往复丝杆,所述双向往复丝杆的一端贯穿所述压滤腔室的顶端与所述转轴连接,所述双向往复丝杆的另一端延伸至所述缓冲槽内,并与所述缓冲槽的内壁底端转动连接;A bidirectional reciprocating screw rod. One end of the bidirectional reciprocating screw rod penetrates the top of the filter press chamber and is connected to the rotating shaft. The other end of the bidirectional reciprocating screw rod extends into the buffer groove and is connected with the buffer groove. The bottom end of the inner wall of the groove is rotationally connected;
压滤板,所述压滤板的顶端设置有若干沉头孔,若干所述沉头孔内分别安装有单向膜;A filter press plate, the top of the filter press plate is provided with a number of countersunk holes, and one-way membranes are respectively installed in several of the countersunk holes;
所述压滤板包括一级压滤板、二级压滤板和三级压滤板,所述一级压滤板、所述二级压滤板和所述三级压滤板由上往下依次设置在所述压滤腔室内;The filter press plate includes a first-stage filter press plate, a second-stage filter press plate and a third-stage filter press plate. The first-stage filter press plate, the second-stage filter press plate and the third-stage filter press plate are arranged from top to bottom. The following are arranged in the filter press chamber in sequence;
所述一级压滤板螺纹安装在所述双向往复丝杆的外表面上,且所述一级压滤板的往复移动范围设置在所述压滤腔室的顶端与所述二级压滤板之间,所述一级压滤板的外表面与所述压滤腔室的侧壁滑动连接,所述一级压滤板靠近所述压滤腔室侧壁处设置有限位孔,所述限位孔内安装有限位杆,所述限位杆的一端与所述压滤腔室的顶端连接,所述限位杆的另一端与所述二级压滤板的顶端连接;The threads of the first-stage filter press plate are installed on the outer surface of the two-way reciprocating screw rod, and the reciprocating movement range of the first-stage filter press plate is set between the top of the filter press chamber and the second-stage filter press. Between the plates, the outer surface of the first-stage filter press plate is slidingly connected to the side wall of the filter press chamber, and the first-stage filter press plate is provided with a limited hole near the side wall of the filter press chamber, so A limit rod is installed in the limit hole, one end of the limit rod is connected to the top of the filter press chamber, and the other end of the limit rod is connected to the top of the secondary filter press plate;
所述二级压滤板和所述三级压滤板分别套设在所述双向往复丝杆的外表面上,所述二级压滤板和所述三级压滤板的外表面分别安装在所述压滤腔室的侧壁上,所述二级压滤板和所述三级压滤板的相对面之间填充有吸附层。The two-stage filter press plate and the three-stage filter press plate are respectively sleeved on the outer surface of the two-way reciprocating screw rod, and the outer surfaces of the two-stage filter press plate and the three-stage filter press plate are installed respectively. On the side wall of the filter press chamber, an adsorption layer is filled between the opposite surfaces of the secondary filter press plate and the third-stage filter press plate.
可选地,所述单向膜为锥形橡胶套,所述锥形橡胶套安装在所述沉头孔内,所述锥形橡胶套的开口端朝向所述压滤板的顶端一侧;Optionally, the one-way membrane is a cone-shaped rubber sleeve, the cone-shaped rubber sleeve is installed in the countersunk hole, and the open end of the cone-shaped rubber sleeve faces the top side of the filter press plate;
当所述锥形橡胶套未受到向下的挤压力时,所述锥形橡胶套的底端处于闭合状态;When the conical rubber sleeve is not subjected to downward extrusion force, the bottom end of the conical rubber sleeve is in a closed state;
当所述锥形橡胶套受到向下的挤压力时,所述锥形橡胶套的底端处于打开状态。When the conical rubber sleeve is subjected to downward extrusion force, the bottom end of the conical rubber sleeve is in an open state.
可选地,所述反应釜的顶端设置有加料口和注水口,所述加料口和所述注水口分别与所述混合腔室连通;Optionally, the top of the reaction kettle is provided with a feeding port and a water injection port, and the feeding port and the water injection port are respectively connected with the mixing chamber;
所述反应釜的底端设置有三级出料口和排污口,所述三级出料口和所述排污口分别与所述缓冲槽的侧壁底端连通,所述三级出料口安装有第三电子阀,所述排污口安装有第四电子阀,所述第三电子阀和所述第四电子阀分别与控制单元连接。The bottom end of the reaction kettle is provided with a three-stage discharge port and a sewage discharge port. The three-stage discharge port and the sewage discharge port are respectively connected with the bottom end of the side wall of the buffer tank. The three-stage discharge port A third electronic valve is installed, and the sewage outlet is installed with a fourth electronic valve. The third electronic valve and the fourth electronic valve are respectively connected to the control unit.
一种清洁压裂液的制备方法,利用上述所述的制备装置制取清洁压裂液,包括以下步骤:A method for preparing clean fracturing fluid, using the above-mentioned preparation device to prepare clean fracturing fluid, including the following steps:
步骤一)向混合腔室内添加反应原料制备水基压裂液,并对所述水基压裂液进行破胶处理;Step 1) Add reaction raw materials into the mixing chamber to prepare water-based fracturing fluid, and perform gel breaking treatment on the water-based fracturing fluid;
步骤二)所述水基压裂液进行破胶处理后,控制单元控制第一电子阀将一级出料口打开,使得经破胶处理后的所述水基压裂液流入到筛分腔室内,并通过筛分组件对经破胶处理后的所述水基压裂液进行筛分过滤处理;Step 2) After the water-based fracturing fluid undergoes gel breaking treatment, the control unit controls the first electronic valve to open the first-level discharge port, so that the water-based fracturing fluid after gel breaking treatment flows into the screening chamber. In the room, the water-based fracturing fluid after gel breaking treatment is screened and filtered through a screening component;
步骤三)经筛分过滤处理后的所述水基压裂液,从第二出料口流入到压滤腔室内,并通过压滤组件进行压滤吸附处理后,得到清洁压裂液。Step 3) The water-based fracturing fluid that has been screened and filtered flows into the filtration chamber from the second outlet, and is filtered and adsorbed through the filtration assembly to obtain clean fracturing fluid.
可选地,在所述步骤一)中,当所述混合腔室内添加反应原料结束后,控制单元控制驱动单元启动,并控制加热板对混合腔室内部进行加热,使得驱动单元控制搅拌杆转动,并带动搅拌叶片对混合腔室内部的反应原料进行搅拌,使得反应原料充分混合后得到水基压裂液,所述水基压裂液达到预设温度值后与破胶剂发生破胶反应,同时通过温度传感器检测混合腔室内水基压裂液的温度,直至温度传感器检测到所述水基压裂液的温度值达到预设温度值,并将检测信息发送给控制单元,使得所述控制单元控制加热板停止加热。Optionally, in step 1), after the addition of reaction raw materials in the mixing chamber is completed, the control unit controls the driving unit to start, and controls the heating plate to heat the inside of the mixing chamber, so that the driving unit controls the rotation of the stirring rod. , and drive the stirring blade to stir the reaction raw materials inside the mixing chamber, so that the reaction raw materials are fully mixed to obtain a water-based fracturing fluid. After the water-based fracturing fluid reaches the preset temperature value, a gel breaking reaction occurs with the gel breaker. , and at the same time, the temperature sensor is used to detect the temperature of the water-based fracturing fluid in the mixing chamber, until the temperature sensor detects that the temperature value of the water-based fracturing fluid reaches the preset temperature value, and sends the detection information to the control unit, so that the The control unit controls the heating plate to stop heating.
可选地,在所述步骤二)中,所述控制单元控制加热板停止加热后,至少延迟30秒再控制第一电子阀打开,使得所述水基压裂液完全破胶处理后,从所述一级出料口流入到所述筛分腔室内,并依次经过多个锥形滤筒对所述水基压裂液中的部分不溶物杂质进行过滤,同时通过对应的刮板将每一所述锥形滤筒表面过滤后的不溶物杂质进行刮除;Optionally, in step 2), after the control unit controls the heating plate to stop heating, it delays for at least 30 seconds before controlling the first electronic valve to open, so that after the water-based fracturing fluid is completely broken, the The first-level discharge port flows into the screening chamber, and sequentially passes through multiple conical filter cylinders to filter some insoluble impurities in the water-based fracturing fluid, and at the same time, each part is filtered through the corresponding scraper. 1. scraping off the filtered insoluble impurities on the surface of the conical filter cylinder;
所述混合腔室内部的水基压裂液完全排出后,控制单元控制第一电子阀关闭,并控制第二电子阀打开,使得所述刮板在离心力作用下,将所述锥形滤筒表面的不溶物杂质从排料口甩出到废料回收箱内,所述第二电子阀直至下一次所述第一电子阀打开前关闭。After the water-based fracturing fluid inside the mixing chamber is completely discharged, the control unit controls the first electronic valve to close and the second electronic valve to open, so that the scraper moves the conical filter cartridge under the action of centrifugal force. The insoluble impurities on the surface are thrown out from the discharge port into the waste recycling box, and the second electronic valve is closed until the first electronic valve is opened next time.
可选地,在所述步骤三)中,所述水基压裂液从第二出料口流入到所述压滤腔室后,双向往复丝杆驱动一级压滤板上下往复挤压所述水基压裂液;Optionally, in step three), after the water-based fracturing fluid flows into the filter press chamber from the second outlet, the bidirectional reciprocating screw drives the first-stage filter press plate to reciprocate up and down to squeeze the filter press chamber. The water-based fracturing fluid;
当所述一级压滤板向上挤压所述水基压裂液时,部分所述水基压裂液顶开所述一级压滤板上的单向膜,并流向所述一级压滤板与所述二级压滤板之间;When the first-stage filter press plate squeezes the water-based fracturing fluid upward, part of the water-based fracturing fluid pushes away the unidirectional membrane on the first-stage filter press plate and flows to the first-stage press plate. Between the filter plate and the secondary filter press plate;
当所述一级压滤板向下挤压所述水基压裂液时,将所述一级压滤板与所述二级压滤板之间的所述水基压裂液,压入到所述二级压滤板与所述三级压滤板之间,并经所述吸附层吸附过滤后,顶开所述三级压滤板上的单向膜,流入缓冲槽内。When the first-stage filter press plate squeezes the water-based fracturing fluid downward, the water-based fracturing fluid between the first-stage filter press plate and the second-stage filter press plate is pressed into Between the second-stage filter press plate and the third-stage filter press plate, and after adsorption and filtration by the adsorption layer, the one-way membrane on the third-stage filter press plate is pushed open and flows into the buffer tank.
本发明能产生的有益效果包括:The beneficial effects produced by this invention include:
本发明所提供的清洁压裂液的制备装置,通过设置混合腔室、筛分腔室和压滤腔室,能够对水基压裂液经破胶处理后,立即进行过滤处理,避免水基压裂液冷却后粘性增大导致杂质不易分离;同时通过筛分组件,能够将水基压裂液中的部分不溶物杂质进行过滤,并将过滤后的不溶物杂质排出到反应釜外,从而减少水基压裂液中的残渣含量;并通过设置压滤组件,能够对水基压裂液中的剩余不溶物杂质进行吸附过滤,进一步减少水基压裂液中的残渣含量,来制备清洁压裂液,提高储层渗透率和裂缝的导流能力。The preparation device for clean fracturing fluid provided by the present invention, by setting up a mixing chamber, a screening chamber and a filter pressure chamber, can filter the water-based fracturing fluid immediately after gel breaking treatment to avoid water-based fracturing fluid. After the fracturing fluid is cooled, the viscosity increases, making it difficult to separate impurities; at the same time, through the screening component, some insoluble impurities in the water-based fracturing fluid can be filtered, and the filtered insoluble impurities can be discharged out of the reactor, thereby Reduce the residue content in the water-based fracturing fluid; and by setting up a filter press component, the remaining insoluble impurities in the water-based fracturing fluid can be adsorbed and filtered to further reduce the residue content in the water-based fracturing fluid to prepare clean Fracturing fluid improves reservoir permeability and fracture conductivity.
附图说明Description of the drawings
图1为本发明一种清洁压裂液的制备装置的结构示意图;Figure 1 is a schematic structural diagram of a preparation device for clean fracturing fluid according to the present invention;
图2为本发明中图1的A-A处剖视图;Figure 2 is a cross-sectional view along line A-A of Figure 1 in the present invention;
图3为本发明中图1的B-B处剖视图;Figure 3 is a sectional view taken along line B-B of Figure 1 in the present invention;
图4为本发明中图2的C处放大图;Figure 4 is an enlarged view of C in Figure 2 according to the present invention;
图5为本发明一种清洁压裂液的制备方法的流程示意图;Figure 5 is a schematic flow chart of a preparation method of clean fracturing fluid according to the present invention;
图中:1、反应釜;2、混合腔室;3、筛分腔室;4、压滤腔室;5、一级出料口;6、二级出料口;7、第一电子阀;8、缓冲槽;9、驱动单元;10、搅拌杆;11、搅拌叶片;12、加热板;13、温度传感器;14、转轴;15、锥形滤筒;16、废料回收箱;17、排料口;18、刮板;19、第二电子阀;20、双向往复丝杆;21、一级压滤板;22、二级压滤板;23、三级压滤板;24、沉头孔;25、单向膜;26、限位杆;27、吸附层;28、加料口;29、注水口;30、三级出料口;31、排污口;32、第三电子阀;33、第四电子阀。In the picture: 1. Reactor; 2. Mixing chamber; 3. Screening chamber; 4. Press filter chamber; 5. Primary discharge port; 6. Secondary discharge port; 7. First electronic valve ; 8. Buffer tank; 9. Drive unit; 10. Stirring rod; 11. Stirring blade; 12. Heating plate; 13. Temperature sensor; 14. Rotating shaft; 15. Conical filter cartridge; 16. Waste recycling box; 17. Discharge port; 18. Scraper; 19. Second electronic valve; 20. Bidirectional reciprocating screw; 21. Primary filter press plate; 22. Secondary filter press plate; 23. Third-stage filter press plate; 24. Sinking Head hole; 25. One-way membrane; 26. Limiting rod; 27. Adsorption layer; 28. Feeding port; 29. Water injection port; 30. Third-level outlet; 31. Sewage outlet; 32. Third electronic valve; 33. The fourth electronic valve.
具体实施方式Detailed ways
下面结合实施例详述本发明,但本发明并不局限于这些实施例。The present invention will be described in detail below with reference to examples, but the present invention is not limited to these examples.
实施例一;Embodiment 1;
如图1-图4所示,本发明提供一种清洁压裂液的制备装置,包括:As shown in Figures 1-4, the present invention provides a preparation device for clean fracturing fluid, including:
反应釜1,反应釜1的内部由上往下依次设置有混合腔室2、筛分腔室3和压滤腔室4,混合腔室2与筛分腔室3之间开设有一级出料口5,筛分腔室3与压滤腔室4之间开设有二级出料口6,一级出料口5内安装有第一电子阀7;Reactor 1. The interior of the reactor 1 is provided with a mixing chamber 2, a screening chamber 3 and a filter pressure chamber 4 in order from top to bottom. There is a first-level discharge between the mixing chamber 2 and the screening chamber 3. Port 5, a secondary discharge port 6 is provided between the screening chamber 3 and the filter pressure chamber 4, and a first electronic valve 7 is installed in the primary discharge port 5;
混合腔室2内安装有加热搅拌组件,加热搅拌组件用于对加入混合腔室2内的反应原料进行加热、搅拌,其中反应原料包含胍胶粉末、交联剂、破胶剂、pH值调节剂、杀菌剂、粘土稳定剂、助排剂和水,使得混合腔室2内的反应原料充分混合后,得到水基压裂液,并将水基压裂液加热到70℃后,破胶剂逐渐溶解并释放酸性物质对水基压裂液进行破胶反应;A heating and stirring component is installed in the mixing chamber 2. The heating and stirring component is used to heat and stir the reaction raw materials added to the mixing chamber 2. The reaction raw materials include guar gum powder, cross-linking agent, gel breaker, and pH value adjustment. agent, bactericide, clay stabilizer, drainage aid and water, so that the reaction raw materials in the mixing chamber 2 are fully mixed to obtain a water-based fracturing fluid, and after heating the water-based fracturing fluid to 70°C, the gel is broken The agent gradually dissolves and releases acidic substances to perform a gel breaking reaction on the water-based fracturing fluid;
筛分腔室3内安装有筛分组件,筛分组件用于对水基压裂液中的部分不溶物杂质进行过滤,并将过滤后的不溶物杂质排出到反应釜1外,用于对水基压裂液中的不溶物杂质进行一级过滤,减少水基压裂液中的残渣含量,进而提高储层渗透率和裂缝的导流能力;A screening assembly is installed in the screening chamber 3. The screening assembly is used to filter some insoluble impurities in the water-based fracturing fluid and discharge the filtered insoluble impurities to the outside of the reaction kettle 1 for processing. Insoluble impurities in the water-based fracturing fluid undergo one-stage filtration to reduce the residue content in the water-based fracturing fluid, thereby improving reservoir permeability and fracture conductivity;
压滤腔室4内安装有压滤组件,压滤组件的底部预留有缓冲槽8,压滤组件用于对水基压裂液中的剩余不溶物杂质进行吸附过滤,进一步减少水基压裂液中的残渣含量,得到清洁压裂液,提高储层渗透率和裂缝的导流能力,并将清洁压裂液压入缓冲槽8内,进行储存;A filter press assembly is installed in the filter press chamber 4. A buffer tank 8 is reserved at the bottom of the filter press assembly. The filter press assembly is used to adsorb and filter the remaining insoluble impurities in the water-based fracturing fluid to further reduce the water-based pressure. The residue content in the fracturing fluid is obtained to obtain clean fracturing fluid, which improves the reservoir permeability and fracture conductivity, and the clean fracturing fluid is poured into the buffer tank 8 for storage;
驱动单元9,驱动单元9用于驱动搅拌组件、筛分组件和压滤组件进行同步转动;Driving unit 9, the driving unit 9 is used to drive the stirring assembly, screening assembly and filter press assembly to rotate synchronously;
控制单元,控制单元分别与第一电子阀7和驱动单元9连接,用于控制第一电子阀7的启闭,以及控制驱动单元9的启停。The control unit is connected to the first electronic valve 7 and the driving unit 9 respectively, and is used to control the opening and closing of the first electronic valve 7 and the starting and stopping of the driving unit 9.
需要说明的是:为了便于判断混合腔室2、筛分腔室3和压滤腔室4内部的工作状态,在反应釜1外并位于每一腔室的中下部分别设置一个观察窗口;同时为了便于自动检测混合腔室2内部的水基压裂液是否完全排出,可以在混合腔室2的底部安装液位开关,并将液位开关连接至控制单元,使得控制单元根据液位开关的液位检测信息控制第一电子阀7的启闭。It should be noted that: in order to facilitate the judgment of the internal working status of the mixing chamber 2, the screening chamber 3 and the filter pressure chamber 4, an observation window is set outside the reaction kettle 1 and located in the middle and lower part of each chamber; at the same time In order to facilitate the automatic detection of whether the water-based fracturing fluid inside the mixing chamber 2 is completely discharged, a liquid level switch can be installed at the bottom of the mixing chamber 2, and the liquid level switch is connected to the control unit, so that the control unit can act according to the position of the liquid level switch. The liquid level detection information controls the opening and closing of the first electronic valve 7 .
作为本发明的另一种实施方式,可以将制备好的水基压裂液和破胶剂直接加入到混合腔室2内进行破胶处理,然后对破胶处理后的水基压裂液中含有的不溶物杂质,依次进行筛分过滤和吸附过滤后,得到清洁压裂液,能够提高清洁压裂液的制备效率,适用于大型油井开采施工。As another embodiment of the present invention, the prepared water-based fracturing fluid and gel breaker can be directly added into the mixing chamber 2 for gel breaking treatment, and then the water-based fracturing fluid after gel breaking treatment can be The insoluble impurities contained in it are sequentially screened, filtered and adsorbed to obtain clean fracturing fluid, which can improve the preparation efficiency of clean fracturing fluid and is suitable for large-scale oil well mining construction.
进一步地,加热搅拌组件包括:Further, the heating stirring assembly includes:
搅拌杆10,搅拌杆10的一端贯穿混合腔室2的顶端,并延伸至反应釜1的外侧与驱动单元9的输出端连接,搅拌杆10的另一端与混合腔室2的底端转动连接,其中驱动单元9采用减速机,减速机通过机架安装在反应釜1的顶端;Stirring rod 10, one end of the stirring rod 10 penetrates the top of the mixing chamber 2, and extends to the outside of the reactor 1 to be connected to the output end of the drive unit 9. The other end of the stirring rod 10 is rotationally connected to the bottom end of the mixing chamber 2. , in which the drive unit 9 adopts a reducer, which is installed on the top of the reactor 1 through a frame;
若干搅拌叶片11,若干搅拌叶片11环形均匀焊接在搅拌杆10的外表面上,每一搅拌叶片11的结构均为弧形滤板,在搅拌过程中,通过弧形滤板上的滤孔,有助于对水中出现结块现象的反应原料进行破碎,从而加快胍胶粉末在水中的溶解,避免胍胶粉末加入水中后出现结块的现象;A number of stirring blades 11 are evenly welded to the outer surface of the stirring rod 10 in an annular shape. The structure of each stirring blade 11 is an arc-shaped filter plate. During the stirring process, through the filter holes on the arc-shaped filter plate, It helps to break up the reaction raw materials that appear to be agglomerated in the water, thereby accelerating the dissolution of the guar gum powder in the water and avoiding the agglomeration of the guar gum powder after it is added to the water;
若干加热板12,若干加热板12均匀焊接在混合腔室2的侧壁上,使得搅拌叶片11在对混合腔室2内部的反应物进行搅拌时,加热板12能够对反应物提供阻力,从而增大搅拌叶片11对反应物的扰动力度,提高混合效率,同时搅拌叶片11在旋转过程中与加热板12之间留有间隙,能够防止搅拌叶片11在旋转过程中与加热板12之间发生碰撞;Several heating plates 12 are evenly welded on the side walls of the mixing chamber 2, so that when the stirring blades 11 stir the reactants inside the mixing chamber 2, the heating plates 12 can provide resistance to the reactants, thereby Increase the disturbance intensity of the stirring blade 11 to the reactants and improve the mixing efficiency. At the same time, there is a gap between the stirring blade 11 and the heating plate 12 during the rotation process, which can prevent the mixing between the stirring blade 11 and the heating plate 12 during the rotation process. collision;
温度传感器13,温度传感器13和加热板12分别与控制单元连接,温度传感器13的探头安装在混合腔室2的底端,用于检测混合腔室2内反应物的温度,并将检测到的温度信息发送给控制单元,使得控制单元根据温度信息控制加热板12对混合腔室2内的反应物进行加热。The temperature sensor 13, the temperature sensor 13 and the heating plate 12 are respectively connected to the control unit. The probe of the temperature sensor 13 is installed at the bottom end of the mixing chamber 2 for detecting the temperature of the reactants in the mixing chamber 2 and detecting the temperature. The temperature information is sent to the control unit, so that the control unit controls the heating plate 12 to heat the reactants in the mixing chamber 2 according to the temperature information.
进一步地,筛分组件包括:Further, the screening components include:
转轴14,转轴14的一端贯穿筛分腔室3的顶端与搅拌杆10的底端焊接,转轴14的另一端与筛分腔室3的底端通过轴承转动连接;Rotating shaft 14, one end of the rotating shaft 14 passes through the top of the screening chamber 3 and is welded to the bottom end of the stirring rod 10, and the other end of the rotating shaft 14 is rotationally connected to the bottom end of the screening chamber 3 through a bearing;
若干锥形滤筒15,若干锥形滤筒15沿竖直方向并列安装在筛分腔室3内,且若干锥形滤筒15的滤孔孔径由上往下依次递减,每一锥形滤筒15的开口端均朝下设置,锥形滤筒15的中部套设在转轴14的外表面上,锥形滤筒15的底端一侧固定安装在筛分腔室3的侧壁上,用于水基压裂液经破胶处理后,对水基压裂液中的不溶物杂质进行多级过滤;Several conical filter cylinders 15 are installed side by side in the screening chamber 3 along the vertical direction, and the filter hole diameters of the several conical filter cylinders 15 decrease in sequence from top to bottom. The open ends of the cylinder 15 are all arranged downward, the middle part of the conical filter cylinder 15 is sleeved on the outer surface of the rotating shaft 14, and the bottom end side of the conical filter cylinder 15 is fixedly installed on the side wall of the screening chamber 3. It is used for multi-stage filtration of insoluble impurities in the water-based fracturing fluid after gel breaking treatment;
废料回收箱16,废料回收箱16焊接在反应釜1的外侧壁上,用于收集过滤后的不溶物杂质,同时为了便于对废料回收箱16内部积攒的杂质进行清理,在废料回收箱16的底部设置锥形下料口,并在锥形下料口的底部安装阀板,用于定期清理废料回收箱16内部的不溶物杂质;The waste recycling box 16 is welded on the outer wall of the reactor 1 and is used to collect filtered insoluble impurities. At the same time, in order to facilitate the cleaning of the impurities accumulated inside the waste recycling box 16, there is a A conical discharge port is provided at the bottom, and a valve plate is installed at the bottom of the conical discharge port for regularly cleaning insoluble impurities inside the waste recycling box 16;
筛分腔室3的侧壁上靠近锥形滤筒15底部的一侧开设有若干排料口17,若干排料口17分别与废料回收箱16的内部连通,排料口17的高度大于锥形滤筒15的壁厚,排料口17的底端与锥形滤筒15的底端平齐,每一锥形滤筒15的顶端一侧均平行设置有刮板18,刮板18的一端固定安装在转轴14的外表面上,刮板18的另一端与锥形滤筒15的侧壁滑动连接,使得转轴14在旋转过程中,带动刮板18将锥形滤筒15表面过滤后的不溶物杂质刮入到排料口17内,并从排料口17甩出到废料回收箱16内,实现不溶物杂质的自动清理;A number of discharge openings 17 are provided on the side wall of the screening chamber 3 close to the bottom of the conical filter cylinder 15. The several discharge openings 17 are respectively connected with the inside of the waste recycling box 16. The height of the discharge openings 17 is larger than that of the conical filter cartridge 15. The wall thickness of the cone-shaped filter cartridge 15 is such that the bottom end of the discharge port 17 is flush with the bottom end of the cone-shaped filter cartridge 15. A scraper 18 is arranged parallel to the top side of each cone-shaped filter cartridge 15. The scraper 18 One end is fixedly installed on the outer surface of the rotating shaft 14, and the other end of the scraper 18 is slidingly connected to the side wall of the conical filter cylinder 15, so that during the rotation of the rotating shaft 14, the scraper 18 is driven to filter the surface of the conical filter cylinder 15. The insoluble impurities are scraped into the discharge port 17 and thrown out from the discharge port 17 into the waste recycling box 16 to realize automatic cleaning of insoluble impurities;
每一排料口17处均安装有第二电子阀19,第二电子阀19与控制单元连接,第二电子阀19在第一电子阀7打开前关闭,防止刮板18在离心力作用下,将水基压裂液从排料口17带入到废料回收箱16内。A second electronic valve 19 is installed at each discharge port 17. The second electronic valve 19 is connected to the control unit. The second electronic valve 19 is closed before the first electronic valve 7 is opened to prevent the scraper 18 from centrifugal force. The water-based fracturing fluid is brought into the waste recovery box 16 from the discharge port 17 .
进一步地,压滤组件包括:Further, the filter press assembly includes:
双向往复丝杆20,双向往复丝杆20的一端贯穿压滤腔室4的顶端与转轴14的底端焊接,双向往复丝杆20的另一端延伸至缓冲槽8内,并与缓冲槽8的内壁底端通过轴承转动连接;Bidirectional reciprocating screw rod 20. One end of the bidirectional reciprocating screw rod 20 penetrates the top of the filter press chamber 4 and is welded to the bottom end of the rotating shaft 14. The other end of the bidirectional reciprocating screw rod 20 extends into the buffer tank 8 and is connected with the buffer tank 8. The bottom end of the inner wall is rotationally connected through a bearing;
压滤板,压滤板的顶端开设有若干沉头孔24,若干沉头孔24内分别安装有单向膜25;其中,压滤板包括一级压滤板21、二级压滤板22和三级压滤板23,一级压滤板21、二级压滤板22和三级压滤板23由上往下依次安装在压滤腔室4内。The filter press plate has a number of countersunk holes 24 at the top, and one-way membranes 25 are respectively installed in the countersunk holes 24; wherein, the filter press plate includes a primary filter press plate 21 and a secondary filter press plate 22. and a three-stage filter press plate 23. The first-stage filter press plate 21, the second-stage filter press plate 22 and the third-stage filter press plate 23 are installed in the filter press chamber 4 in sequence from top to bottom.
具体的,一级压滤板21螺纹安装在双向往复丝杆20的外表面上,且一级压滤板21的往复移动范围设置在压滤腔室4的顶端与二级压滤板22之间,一级压滤板21的外表面与压滤腔室4的侧壁滑动连接,一级压滤板21靠近压滤腔室4侧壁处开设有限位孔,限位孔内滑动安装有限位杆26,限位杆26的一端与压滤腔室4的顶端固定连接,限位杆26的另一端与二级压滤板22的顶端固定连接;二级压滤板22和三级压滤板23分别套设在双向往复丝杆20的外表面上,二级压滤板22和三级压滤板23的外表面分别固定安装在压滤腔室4的侧壁上,二级压滤板22和三级压滤板23的相对面之间填充有吸附层27;该压滤组件在使用过程中,当水基压裂液从二级出料口6流入到压滤腔室4后,双向往复丝杆20驱动一级压滤板21上下往复挤压水基压裂液;其中,当一级压滤板21向上挤压水基压裂液,并将部分水基压裂液挤压到与压滤腔室4的顶端相接触后,水基压裂液顶开一级压滤板21上的单向膜25,并流向所述一级压滤板21与所述二级压滤板22之间;紧接着,当一级压滤板21向下挤压水基压裂液时,将一级压滤板21与二级压滤板22之间的水基压裂液,压入到二级压滤板22与三级压滤板23之间,并经吸附层27对水基压裂液中的不溶物杂质进行吸附过滤后,得到清洁压裂液,且清洁压裂液再一级压滤板21的持续施压下,顶开三级压滤板23上的单向膜25,流入缓冲槽8内。Specifically, the primary filter press plate 21 is threadedly installed on the outer surface of the bidirectional reciprocating screw rod 20, and the reciprocating movement range of the primary filter press plate 21 is set between the top of the filter press chamber 4 and the secondary filter press plate 22. During this period, the outer surface of the first-stage filter press plate 21 is slidingly connected to the side wall of the filter press chamber 4. A limited hole is provided in the first-stage filter press plate 21 close to the side wall of the filter press chamber 4. There is a limited sliding installation in the limit hole. Position rod 26, one end of the limit rod 26 is fixedly connected to the top of the filter press chamber 4, and the other end of the limit rod 26 is fixedly connected to the top of the secondary filter press plate 22; the second-stage filter plate 22 and the third-stage filter The filter plates 23 are respectively sleeved on the outer surface of the bidirectional reciprocating screw rod 20. The outer surfaces of the secondary filter press plate 22 and the third-stage filter press plate 23 are respectively fixedly installed on the side walls of the filter press chamber 4. The opposite surfaces of the filter plate 22 and the third-stage filter press plate 23 are filled with an adsorption layer 27; during use of the filter press assembly, when the water-based fracturing fluid flows from the secondary outlet 6 into the filter press chamber 4 Finally, the bidirectional reciprocating screw rod 20 drives the primary filter plate 21 to reciprocate up and down to squeeze the water-based fracturing fluid; wherein, when the primary filter plate 21 squeezes the water-based fracturing fluid upward, part of the water-based fracturing fluid is After being squeezed into contact with the top of the filter chamber 4, the water-based fracturing fluid pushes away the one-way membrane 25 on the primary filter plate 21 and flows toward the primary filter plate 21 and the secondary filter plate 21. between the filter press plates 22; then, when the primary filter press plate 21 squeezes the water-based fracturing fluid downward, the water-based fracturing fluid between the primary filter press plate 21 and the secondary filter press plate 22 , is pressed between the secondary filter press plate 22 and the third-stage filter press plate 23, and after adsorbing and filtering the insoluble impurities in the water-based fracturing fluid through the adsorption layer 27, a clean fracturing fluid is obtained, and the clean fracturing fluid is Under the continuous pressure of the first-stage filter press plate 21, the cracking liquid pushes open the one-way membrane 25 on the third-stage filter press plate 23 and flows into the buffer tank 8.
需要说明的是:本实施例中,为了消除一级压滤板21在上下往复移动过程中,其上下两侧腔室内形成压力差,出现反吸状况,影响单向膜25的正常使用,将限位杆26设置为空心杆,并在限位杆26的侧壁上开设有若干换气孔,用于将一级压滤板21两侧的腔室连通;同时为了便于后续对限位杆26进行维护,将限位杆26的两端通过螺栓等紧固件进行固定安装。It should be noted that in this embodiment, in order to eliminate the pressure difference formed in the chambers on the upper and lower sides of the first-stage filter press plate 21 during its up and down reciprocating movement, causing back suction and affecting the normal use of the one-way membrane 25, the The limit rod 26 is set as a hollow rod, and a number of ventilation holes are provided on the side walls of the limit rod 26 to connect the chambers on both sides of the first-stage filter plate 21; at the same time, in order to facilitate the subsequent adjustment of the limit rod 26 for maintenance, and fix and install the two ends of the limit rod 26 with bolts and other fasteners.
作为本发明的一种具体实施方式,本实施例中的吸附层27采用由活性炭纤维构成的蜂窝式夹层结构,该夹层至少设置有三层,且相邻两层之间采用钢结构骨架固定,同时在钢结构骨架上喷涂有耐腐蚀涂层。As a specific implementation mode of the present invention, the adsorption layer 27 in this embodiment adopts a honeycomb sandwich structure composed of activated carbon fibers. The sandwich layer is provided with at least three layers, and a steel structure skeleton is used to fix the two adjacent layers. The steel structure skeleton is sprayed with a corrosion-resistant coating.
进一步地,单向膜25为锥形橡胶套,锥形橡胶套安装在沉头孔24内,锥形橡胶套的开口端朝向压滤板的顶端一侧;当锥形橡胶套未受到向下的挤压力时,锥形橡胶套的底端处于闭合状态;当锥形橡胶套受到向下的挤压力时,锥形橡胶套的底端处于打开状态。Further, the one-way membrane 25 is a conical rubber sleeve. The conical rubber sleeve is installed in the countersunk hole 24. The open end of the conical rubber sleeve faces the top side of the filter press plate; when the conical rubber sleeve is not subjected to downward pressure, When the cone-shaped rubber sleeve is subjected to downward extrusion force, the bottom end of the cone-shaped rubber sleeve is in a closed state; when the cone-shaped rubber sleeve is subjected to downward extrusion force, the bottom end of the cone-shaped rubber sleeve is in an open state.
进一步地,反应釜1的顶端开设有加料口28和注水口29,加料口28和注水口29分别与混合腔室2连通,便于通过加料口28添加反应原料,以及通过注水口29添加水;反应釜1的底端开设有三级出料口30和排污口31,三级出料口30和排污口31分别与缓冲槽8的侧壁底端连通,三级出料口30安装有第三电子阀32,排污口31安装有第四电子阀33,第三电子阀32和第四电子阀33分别与控制单元连接,用于控制第三电子阀32和第四电子阀33的启闭。Further, the top of the reaction kettle 1 is provided with a feeding port 28 and a water injection port 29. The feeding port 28 and the water injection port 29 are respectively connected with the mixing chamber 2 to facilitate the addition of reaction raw materials through the feeding port 28 and the addition of water through the water injection port 29; The bottom end of the reaction kettle 1 is provided with a third-level discharge port 30 and a sewage discharge port 31. The third-level discharge port 30 and the sewage discharge port 31 are respectively connected with the bottom end of the side wall of the buffer tank 8. The third-level discharge port 30 is equipped with a third-level discharge port 30 and a sewage discharge port 31. There are three electronic valves 32, and a fourth electronic valve 33 is installed on the sewage outlet 31. The third electronic valve 32 and the fourth electronic valve 33 are respectively connected to the control unit for controlling the opening and closing of the third electronic valve 32 and the fourth electronic valve 33. .
具体的,该制备装置在使用过程中,将压裂液输送管道的进料端安装在三级出料口30上,将排污口31通过排污管道连接至沉淀池;其中,当清洁压裂液制备完成后,控制单元打开第三电子阀32,将清洁压裂液送入压裂液输送管道内,同时为了使得清洁压裂液快速流出缓冲槽8,可以在压裂液输送管道上增设输送泵;当该制备装置使用结束,或其内部的吸附层27,以及过滤口受到堵塞,导致清洁压裂液的制备效率降低需要清洗时,停止继续加料,然后通过控制单元关闭第二电子阀19和第三电子阀32,并打开第一电子阀7和第四电子阀33,再持续向混合腔室2内注水,并启动驱动单元9,使得搅拌叶片11对混合腔室2内未排完的水基压裂液进行稀释,降低粘度;同时,刮板18利用稀释后的水基压裂液对锥形滤筒15表面的杂质进行刮除,进而加快稀释后的水基压裂液从滤孔通过;并且,在一级压滤板21的往复挤压下,不断将稀释后的水基压裂液压入到吸附层27内,对吸附层27表面进行冲洗,然后将冲洗后的废液通过排污口31以及排污管道排放到沉淀池内,直至排污管道的水流排放速度保持畅通,最后将沉淀池内沉淀后的澄清液进行循环利用。Specifically, during use of the preparation device, the feed end of the fracturing fluid transportation pipeline is installed on the third-stage outlet 30, and the sewage outlet 31 is connected to the sedimentation tank through the sewage pipeline; wherein, when cleaning the fracturing fluid After the preparation is completed, the control unit opens the third electronic valve 32 to send the clean fracturing fluid into the fracturing fluid delivery pipeline. At the same time, in order to allow the clean fracturing fluid to flow out of the buffer tank 8 quickly, a delivery valve can be added to the fracturing fluid delivery pipeline. Pump; when the use of the preparation device is finished, or the internal adsorption layer 27 and the filter port are clogged, resulting in a reduction in the preparation efficiency of clean fracturing fluid and the need for cleaning, stop adding materials, and then close the second electronic valve 19 through the control unit and the third electronic valve 32, and open the first electronic valve 7 and the fourth electronic valve 33, then continue to inject water into the mixing chamber 2, and start the driving unit 9, so that the mixing blades 11 have not completely drained the mixing chamber 2 The water-based fracturing fluid is diluted to reduce the viscosity; at the same time, the scraper 18 uses the diluted water-based fracturing fluid to scrape off impurities on the surface of the conical filter cartridge 15, thereby accelerating the dilution of the water-based fracturing fluid from The filter holes pass through; and, under the reciprocating extrusion of the first-stage filter plate 21, the diluted water-based fracturing fluid is continuously injected into the adsorption layer 27, the surface of the adsorption layer 27 is washed, and then the washed waste is The liquid is discharged into the sedimentation tank through the sewage outlet 31 and the sewage pipe until the water discharge speed of the sewage pipe remains unobstructed, and finally the clarified liquid after sedimentation in the sedimentation tank is recycled.
实施例二;Embodiment 2;
如图5所示,本发明还提供一种清洁压裂液的制备方法,利用上述的制备装置制取清洁压裂液,包括以下步骤:As shown in Figure 5, the present invention also provides a method for preparing clean fracturing fluid. The above-mentioned preparation device is used to prepare clean fracturing fluid, which includes the following steps:
步骤一)向混合腔室2内添加反应原料制备水基压裂液,并对水基压裂液进行破胶处理。Step 1) Add reaction raw materials into the mixing chamber 2 to prepare water-based fracturing fluid, and perform gel breaking treatment on the water-based fracturing fluid.
具体的,当混合腔室2内添加反应原料结束后,控制单元控制驱动单元9启动,并控制加热板12对混合腔室2内部进行加热,使得驱动单元9控制搅拌杆10转动,并带动搅拌叶片11对混合腔室2内部的反应原料进行搅拌,使得反应原料充分混合后得到水基压裂液,水基压裂液达到预设温度值后与破胶剂发生破胶反应,同时通过温度传感器13检测混合腔室2内水基压裂液的温度,直至温度传感器13检测到水基压裂液的温度值达到预设温度值,并将检测信息发送给控制单元,使得控制单元控制加热板12停止加热。Specifically, when the addition of reaction raw materials into the mixing chamber 2 is completed, the control unit controls the driving unit 9 to start, and controls the heating plate 12 to heat the inside of the mixing chamber 2, so that the driving unit 9 controls the rotation of the stirring rod 10 and drives the stirring. The blade 11 stirs the reaction raw materials inside the mixing chamber 2, so that the reaction raw materials are fully mixed to obtain a water-based fracturing fluid. After the water-based fracturing fluid reaches the preset temperature value, a gel breaking reaction occurs with the gel breaker, and at the same time, the temperature The sensor 13 detects the temperature of the water-based fracturing fluid in the mixing chamber 2 until the temperature sensor 13 detects that the temperature value of the water-based fracturing fluid reaches a preset temperature value, and sends the detection information to the control unit, so that the control unit controls the heating. Plate 12 stops heating.
步骤二)水基压裂液进行破胶处理后,控制单元控制第一电子阀7将一级出料口5打开,使得经破胶处理后的水基压裂液流入到筛分腔室3内,并通过筛分组件对经破胶处理后的水基压裂液进行筛分过滤处理。Step 2) After the water-based fracturing fluid undergoes gel breaking treatment, the control unit controls the first electronic valve 7 to open the primary discharge port 5 so that the water-based fracturing fluid after gel breaking treatment flows into the screening chamber 3 inside, and the water-based fracturing fluid after gel breaking treatment is screened and filtered through the screening component.
具体的,控制单元控制加热板12停止加热后,至少延迟30秒再控制第一电子阀7打开,使得水基压裂液完全破胶处理后,从一级出料口5流入到筛分腔室3内,并依次经过多个锥形滤筒15对水基压裂液中的部分不溶物杂质进行过滤,同时通过对应的刮板18将每一锥形滤筒15表面过滤后的不溶物杂质进行刮除;Specifically, after the control unit controls the heating plate 12 to stop heating, it delays for at least 30 seconds before controlling the first electronic valve 7 to open, so that after the water-based fracturing fluid is completely gel-breaking, it flows from the primary outlet 5 into the screening chamber. In the chamber 3, some insoluble impurities in the water-based fracturing fluid are filtered through multiple conical filter cylinders 15 in sequence, and at the same time, the filtered insoluble matter on the surface of each conical filter cylinder 15 is filtered through the corresponding scraper 18. Impurities are scraped off;
混合腔室2内部的水基压裂液完全排出后,控制单元控制第一电子阀7关闭,并控制第二电子阀19打开,使得刮板18在离心力作用下,将锥形滤筒15表面的不溶物杂质从排料口17甩出到废料回收箱16内,第二电子阀19直至下一次第一电子阀7打开前关闭。After the water-based fracturing fluid inside the mixing chamber 2 is completely discharged, the control unit controls the first electronic valve 7 to close and the second electronic valve 19 to open, so that the scraper 18 moves the surface of the conical filter cartridge 15 under the action of centrifugal force. The insoluble impurities are thrown out from the discharge port 17 into the waste recovery box 16, and the second electronic valve 19 is closed until the first electronic valve 7 is opened next time.
步骤三)经筛分过滤处理后的水基压裂液,从第二出料口流入到压滤腔室4内,并通过压滤组件进行压滤吸附处理后,得到清洁压裂液。Step 3) The water-based fracturing fluid that has been screened and filtered flows into the filter pressure chamber 4 from the second outlet, and is filtered and adsorbed through the filter press assembly to obtain clean fracturing fluid.
具体的,水基压裂液从第二出料口流入到压滤腔室4后,双向往复丝杆20驱动一级压滤板21上下往复挤压水基压裂液;Specifically, after the water-based fracturing fluid flows into the filter press chamber 4 from the second outlet, the bidirectional reciprocating screw 20 drives the primary filter plate 21 to reciprocate up and down to squeeze the water-based fracturing fluid;
当一级压滤板21向上挤压水基压裂液时,部分水基压裂液顶开一级压滤板21上的单向滤膜,并流向一级压滤板21与二级压滤板22之间;When the primary filter press plate 21 squeezes the water-based fracturing fluid upward, part of the water-based fracturing fluid pushes open the one-way filter membrane on the primary filter press plate 21 and flows to the primary filter press plate 21 and the secondary pressure fracturing fluid. between filter plates 22;
当一级压滤板21向下挤压水基压裂液时,将一级压滤板21与二级压滤板22之间的水基压裂液,压入到二级压滤板22与三级压滤板23之间,并经吸附层27吸附过滤后,顶开三级压滤板23上的单向膜25,流入缓冲槽8内。When the primary filter press plate 21 squeezes the water-based fracturing fluid downward, the water-based fracturing fluid between the primary filter press plate 21 and the secondary filter press plate 22 is pressed into the secondary filter press plate 22 and the three-stage filter press plate 23, and after adsorption and filtration by the adsorption layer 27, the one-way membrane 25 on the three-stage filter press plate 23 is pushed open, and flows into the buffer tank 8.
以上所述,仅是本发明的几个实施例,并非对本发明做任何形式的限制,虽然本发明以较佳实施例揭示如上,然而并非用以限制本发明,任何熟悉本专业的技术人员,在不脱离本发明技术方案的范围内,利用上述揭示的技术内容做出些许的变动或修饰均等同于等效实施案例,均属于技术方案范围内。The above are only a few embodiments of the present invention, and are not intended to limit the present invention in any way. Although the present invention is disclosed above in preferred embodiments, it is not intended to limit the present invention. Any person familiar with the art, Without departing from the scope of the technical solution of the present invention, slight changes or modifications made using the technical content disclosed above are equivalent to equivalent implementation examples and fall within the scope of the technical solution.
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CN118724207A (en) * | 2024-06-25 | 2024-10-01 | 安瑞森(宿迁)电子材料有限公司 | A hydrofluoric acid waste liquid treatment tank |
CN119075487A (en) * | 2024-11-06 | 2024-12-06 | 夏津鸿泰鼎新材料科技有限公司 | A dissolving liquid filtering device for producing lyocell fibers |
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CN118724207A (en) * | 2024-06-25 | 2024-10-01 | 安瑞森(宿迁)电子材料有限公司 | A hydrofluoric acid waste liquid treatment tank |
CN119075487A (en) * | 2024-11-06 | 2024-12-06 | 夏津鸿泰鼎新材料科技有限公司 | A dissolving liquid filtering device for producing lyocell fibers |
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