CN115157443B - A device suitable for preparing water-based foam and mixing it with cement slurry - Google Patents
A device suitable for preparing water-based foam and mixing it with cement slurry Download PDFInfo
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- CN115157443B CN115157443B CN202210696955.XA CN202210696955A CN115157443B CN 115157443 B CN115157443 B CN 115157443B CN 202210696955 A CN202210696955 A CN 202210696955A CN 115157443 B CN115157443 B CN 115157443B
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- 239000006260 foam Substances 0.000 title claims abstract 57
- 239000004568 cement Substances 0.000 title claims abstract 38
- 239000002002 slurry Substances 0.000 title claims abstract 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract 14
- 239000007789 gas Substances 0.000 claims abstract 21
- 238000005187 foaming Methods 0.000 claims abstract 13
- 239000007788 liquid Substances 0.000 claims abstract 13
- 238000003756 stirring Methods 0.000 claims abstract 7
- 239000011261 inert gas Substances 0.000 claims abstract 5
- 239000000945 filler Substances 0.000 claims abstract 4
- 238000000034 method Methods 0.000 claims 7
- 238000002474 experimental method Methods 0.000 claims 6
- 239000010881 fly ash Substances 0.000 claims 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims 3
- 229910000831 Steel Inorganic materials 0.000 claims 3
- 239000010959 steel Substances 0.000 claims 3
- 229910001220 stainless steel Inorganic materials 0.000 claims 2
- 239000010935 stainless steel Substances 0.000 claims 2
- 241001122767 Theaceae Species 0.000 claims 1
- 239000011230 binding agent Substances 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000004891 communication Methods 0.000 claims 1
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 claims 1
- 239000011148 porous material Substances 0.000 claims 1
- 239000001397 quillaja saponaria molina bark Substances 0.000 claims 1
- 229930182490 saponin Natural products 0.000 claims 1
- 150000007949 saponins Chemical class 0.000 claims 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 claims 1
- 239000003381 stabilizer Substances 0.000 claims 1
- 239000002562 thickening agent Substances 0.000 claims 1
- 210000002268 wool Anatomy 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 2
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 1
- 239000001569 carbon dioxide Substances 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/08—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions using driven mechanical means affecting the mixing
- B28C5/10—Mixing in containers not actuated to effect the mixing
- B28C5/12—Mixing in containers not actuated to effect the mixing with stirrers sweeping through the materials, e.g. with incorporated feeding or discharging means or with oscillating stirrers
- B28C5/14—Mixing in containers not actuated to effect the mixing with stirrers sweeping through the materials, e.g. with incorporated feeding or discharging means or with oscillating stirrers the stirrers having motion about a horizontal or substantially horizontal axis
- B28C5/142—Mixing in containers not actuated to effect the mixing with stirrers sweeping through the materials, e.g. with incorporated feeding or discharging means or with oscillating stirrers the stirrers having motion about a horizontal or substantially horizontal axis the stirrer shaft carrying screw-blades
- B28C5/143—Mixing in containers not actuated to effect the mixing with stirrers sweeping through the materials, e.g. with incorporated feeding or discharging means or with oscillating stirrers the stirrers having motion about a horizontal or substantially horizontal axis the stirrer shaft carrying screw-blades for materials flowing continuously through the mixing device
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/08—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions using driven mechanical means affecting the mixing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/08—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions using driven mechanical means affecting the mixing
- B28C5/0806—Details; Accessories
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Structural Engineering (AREA)
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
Description
技术领域technical field
本发明属于发泡设备与搅拌设备领域,具体涉及一种适用于制备水基泡沫并将其与水泥浆混合搅拌的装置。The invention belongs to the field of foaming equipment and stirring equipment, in particular to a device suitable for preparing water-based foam and mixing it with cement slurry.
背景技术Background technique
相同水灰比条件下,泡沫水泥浆具有更低的渗透性以及更高的强度。不同比重的泡沫水泥浆完全能满足抗压强度、渗透性、流动度等不同工作性能的要求。泡沫水泥浆作为一种新型材料已得到了广泛应用。同时水泥生产中由于燃料燃烧以及熟料煅烧,会产生大量的对环境有污染的气体,例如二氧化碳气体,为了减少空气中的碳排放,保护环境,尝试利用这些气体制作水基泡沫,从而制备轻质泡沫水泥浆,再由轻质泡沫水泥浆制备泡沫同步注浆浆液的方法并取得成效。但现有发泡设备制备所得的水基泡沫大都不具有均匀的泡沫结构,较高的发泡倍数以及一定的稳定时间,所制备水基泡沫不能达到工程所需的质量要求,同时现有混合设备在进行混合搅拌时大多为一次添加,两者混合,混合时泡沫很容易破裂,破泡率较高,水基泡沫与水泥浆的接触面积少,混合搅拌所得泡沫水泥浆各项性质都不能满足工程要求,为了得到质量较好的泡沫水泥浆用于实验经常需要人工搅拌,同时,当前技术几乎无法实现发泡与混合搅拌的步调一致,即发泡完成后在加入水泥浆的同时将泡沫通入混合器中以确保材料损耗较少,设备磨损较少。Under the same water-cement ratio, the foam cement slurry has lower permeability and higher strength. Foam cement slurry with different specific gravity can fully meet the requirements of different working performances such as compressive strength, permeability and fluidity. Foam cement slurry has been widely used as a new type of material. At the same time, due to fuel combustion and clinker calcination in cement production, a large amount of environmentally polluting gases will be produced, such as carbon dioxide gas. In order to reduce carbon emissions in the air and protect the environment, we try to use these gases to make water-based foams, so as to prepare lightweight The method of preparing foam synchronous grouting grout from light foam cement slurry and achieving good results. However, most of the water-based foams prepared by the existing foaming equipment do not have a uniform foam structure, a high expansion ratio and a certain stability time, and the prepared water-based foams cannot meet the quality requirements required by the project. At the same time, the existing mixing When the equipment is mixed and stirred, it is mostly added at one time. When the two are mixed, the foam is easy to break when mixed, the foam breaking rate is high, the contact area between the water-based foam and the cement slurry is small, and the properties of the foamed cement slurry obtained by mixing and stirring are not good. To meet the engineering requirements, manual mixing is often required in order to obtain good quality foamed cement slurry for experiments. At the same time, the current technology can hardly achieve the same pace of foaming and mixing, that is, after foaming is completed, the foam is added to the cement slurry at the same time. Feed into the mixer to ensure less material loss and less equipment wear.
因此需要一种能制备细腻,均匀,稳定的水基泡沫的发泡设备以及一种结构简单,混合搅拌过程中泡沫破裂少,泡沫和水泥浆接触面积大的混合设备,同时需保证二者工作步调一致。Therefore, there is a need for a foaming equipment that can prepare fine, uniform, and stable water-based foam and a mixing equipment that has a simple structure, less foam breakage during mixing and mixing, and a large contact area between foam and cement slurry, and at the same time, it is necessary to ensure that both work In step.
发明内容Contents of the invention
本发明所要解决的技术问题是,提供一种适用于制备水基泡沫并将其与水泥浆混合搅拌的装置,该装置通过不同气瓶提供制备泡沫所需的气体;通过烧瓶提供温度恒定的发泡液;通过发泡器制备细腻,稳定,均匀的水基泡沫;通过混合器将所制备水基泡沫与水泥浆混合搅拌,得到破泡率低,泡沫与水泥浆接触面积大,各项性能能够满足工程需要的泡沫水泥浆;通过设计的工作步骤控制发泡与混合的步调一致。此外,该装置的结构设计简洁,成本较低。The technical problem to be solved by the present invention is to provide a device suitable for preparing water-based foam and mixing it with cement slurry. The device provides the gas required for preparing foam through different gas cylinders; Foam liquid; fine, stable and uniform water-based foam is prepared through a foamer; the prepared water-based foam and cement slurry are mixed and stirred through a mixer to obtain a low foam breaking rate, a large contact area between the foam and the cement slurry, and various properties Foam cement slurry that can meet the needs of the project; control the foaming and mixing steps through the designed working steps. In addition, the structure design of the device is simple and the cost is low.
为解决上述技术问题,本发明采用的技术方案为:In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is:
一种适用于制备水基泡沫并将其与水泥浆混合搅拌的装置,包括气瓶、烧瓶、泡沫腔室和搅拌筒,所述气瓶内填充惰性气体,所述气瓶的出气口依次与气体入口管和T型三通管相连通,所述T型三通管的另外两端分别与烧瓶开口处的发泡液入口管和泡沫腔室左下端的开口管道相连通,所述烧瓶内装有发泡液,所述烧瓶上设有恒温加热器,所述泡沫腔室内设有多层孔隙率逐渐增大的多孔介质,相邻层多孔介质之间设有填充物,所述泡沫腔室的底部设有排放管,所述泡沫腔室的中上端设有泡沫出口管,所述气瓶的出气口处设有气瓶阀门,所述烧瓶的出口处设有烧瓶阀门,所述泡沫出口管处设有泡沫出口管阀门,所述泡沫出口管与搅拌筒相连通,所述搅拌筒的上端设有进浆口用于输入水泥浆,所述搅拌筒的下端设有出浆口。A device suitable for preparing water-based foam and mixing it with cement slurry, including a gas cylinder, a flask, a foam chamber and a mixing drum, the gas cylinder is filled with inert gas, and the gas outlet of the gas cylinder is sequentially connected with the The gas inlet pipe is communicated with the T-shaped tee pipe, and the other two ends of the T-shaped tee pipe are respectively connected with the foaming liquid inlet pipe at the opening of the flask and the open pipe at the lower left end of the foam chamber. Foaming liquid, the flask is provided with a constant temperature heater, the foam chamber is provided with multi-layer porous media with gradually increasing porosity, fillers are arranged between adjacent layers of porous media, and the foam chamber The bottom is provided with a discharge pipe, the middle and upper end of the foam chamber is provided with a foam outlet pipe, the air outlet of the gas cylinder is provided with a cylinder valve, the outlet of the flask is provided with a flask valve, and the foam outlet pipe A foam outlet pipe valve is provided at the center, and the foam outlet pipe is connected with the mixing drum. The upper end of the mixing drum is provided with a slurry inlet for inputting cement slurry, and the lower end of the mixing drum is provided with a slurry outlet.
进一步的,所述搅拌筒横向放置,所述搅拌筒内设有横向放置的中空螺旋杆,所述搅拌筒和所述中空螺旋杆均与轴承的旋转轴相连,所述轴承通过电机供电,所述泡沫出口管伸入到所述搅拌筒内,所述泡沫出口管与所述中空螺旋杆相通,所述中空螺旋杆上均匀设置出泡圆孔。Further, the mixing drum is placed horizontally, and a horizontally placed hollow screw rod is arranged inside the mixing drum. Both the mixing drum and the hollow screw rod are connected to the rotating shaft of the bearing, and the bearing is powered by a motor. The foam outlet pipe extends into the mixing drum, and the foam outlet pipe communicates with the hollow screw rod, and the hollow screw rod is evenly provided with round holes for foaming.
优选的,所述轴承包括反向转动的内旋转轴和外旋转轴,所述内旋转轴与所述中空螺旋杆相连,所述外旋转轴与所述搅拌筒相连,所述中空螺旋杆的外壁设有若干内轴叶片,所述搅拌筒的内壁上设有若干外轴叶片。Preferably, the bearing includes an inner rotating shaft and an outer rotating shaft that rotate in opposite directions, the inner rotating shaft is connected with the hollow screw rod, the outer rotating shaft is connected with the mixing drum, and the hollow screw rod The outer wall is provided with several inner shaft blades, and the inner wall of the mixing drum is provided with several outer shaft blades.
优选的,所述内轴叶片为螺旋状不锈钢叶片,所述外轴叶片为矩形不锈钢叶片。Preferably, the inner shaft blade is a helical stainless steel blade, and the outer shaft blade is a rectangular stainless steel blade.
优选的,所述多孔介质为多层钢丝网,所述填充物为钢棉,均匀填充在相邻层的钢丝网之间。Preferably, the porous medium is a multi-layer steel wire mesh, and the filler is steel wool, which is evenly filled between adjacent layers of steel wire mesh.
进一步的,所述搅拌筒的右上部设有密度检测计和PH检测计,所述气瓶上设有气压控制器。Further, a density detector and a pH detector are installed on the upper right part of the mixing drum, and an air pressure controller is installed on the gas cylinder.
进一步的,所述搅拌筒上设有矩形孔洞,所述搅拌筒的外侧靠近所述矩形孔洞一边的位置铰接设有矩形板,所述PH检测计可拆卸设置在所述矩形板的内侧,所述搅拌筒的外侧靠近所述矩形孔洞另外三边的位置固定设有凸块,所述凸块设有凹槽,所述矩形板的内侧设有3/4圈凸圈,所述凸圈与所述凹槽相适配,所述凸圈上设有锁孔,所述凸块上设有锁扣,所述锁孔与所述锁扣相适配。Further, the mixing drum is provided with a rectangular hole, and a rectangular plate is hinged on the outer side of the mixing drum close to one side of the rectangular hole, and the pH detector is detachably arranged on the inner side of the rectangular plate. The outer side of the mixing drum is fixed with bumps near the other three sides of the rectangular hole, the bumps are provided with grooves, and the inner side of the rectangular plate is provided with a 3/4 ring protruding ring, the protruding ring and The grooves are adapted, the protruding ring is provided with a locking hole, and the protrusion is provided with a lock, and the locking hole is adapted to the locking buckle.
优选的,所述气压控制器的读数为0.2kpa,所述烧瓶内采用的发泡液包括4g/L的发泡剂茶皂素,5g/L的稳泡剂十二烷基,2g/L的增稠剂聚丙烯酸钠,所述恒温加热器的温度设定为25摄氏度。Preferably, the reading of the air pressure controller is 0.2kpa, and the foaming liquid adopted in the flask includes the foaming agent tea saponin of 4g/L, the foam stabilizer lauryl of 5g/L, 2g/L The thickener is sodium polyacrylate, and the temperature of the constant temperature heater is set to 25 degrees Celsius.
进一步的,制备泡沫水泥浆的方法为:Further, the method for preparing foam cement slurry is:
步骤A:在发泡液内通入惰性气体气体制备泡沫,计算发泡液的发泡倍率Y,将制备完成的泡沫根据5:1的泡浆比与水泥浆混合搅拌得到试验用泡沫水泥浆,并测量得到泡沫水泥浆密度Z;Step A: Inject inert gas into the foaming liquid to prepare foam, calculate the expansion ratio Y of the foaming liquid, and mix the prepared foam with cement slurry according to the foam slurry ratio of 5:1 to obtain foam cement slurry for testing , and measure the foam cement slurry density Z;
步骤B:基于实验所计划制备泡沫水泥浆的用量X和泡沫水泥浆密度Z,计算实验所需泡沫的量,泡沫量为0.83X,据此制作发泡液;Step B: Calculate the amount of foam required for the experiment based on the amount X of the foamed cement slurry prepared in the experiment and the density Z of the foamed cement slurry, the amount of foam is 0.83X, and the foaming liquid is made accordingly;
步骤C:在气瓶内填充惰性气体,关闭气瓶阀门,调节气压控制器使得气瓶内气压为0.2kpa;Step C: Fill the gas cylinder with inert gas, close the valve of the gas cylinder, and adjust the air pressure controller so that the air pressure in the gas cylinder is 0.2kpa;
步骤D:将气瓶与气体入口管相连接,再气体入口管与T型三通管连通,然后将T型三通管的另外两个分支分别与烧瓶开口处的发泡液入口管和泡沫腔室左下端的开口管道相连通,烧瓶阀门关闭;Step D: Connect the gas cylinder with the gas inlet pipe, then connect the gas inlet pipe with the T-shaped tee pipe, and then connect the other two branches of the T-shaped tee pipe with the foaming liquid inlet pipe and the foaming liquid inlet pipe at the opening of the flask respectively. The open pipe at the lower left end of the chamber is connected, and the valve of the flask is closed;
步骤E:基于步骤B实验所需泡沫的量,选择容积合适的泡沫腔室与T型三通管相连通;Step E: Based on the amount of foam required for the experiment in step B, select a foam chamber with a suitable volume to communicate with the T-shaped tee pipe;
步骤F:同时打开气瓶阀门和烧瓶阀门,关闭泡沫出口管阀门,制备泡沫;Step F: Simultaneously open the gas cylinder valve and the flask valve, close the foam outlet pipe valve, and prepare foam;
步骤G:惰性气体在气压推动下,泡沫进入泡沫腔室逐渐上升,通过多孔介质和填充物;Step G: The inert gas is pushed by the air pressure, and the foam enters the foam chamber and gradually rises, passing through the porous medium and the filler;
步骤H:随着孔隙率的逐渐增大,泡沫孔径变大且均匀;Step H: as the porosity gradually increases, the foam pore size becomes larger and uniform;
步骤I:得到细腻,稳定,均匀的水基泡沫,储存在泡沫腔室的内部;Step I: Obtain fine, stable and uniform water-based foam, which is stored inside the foam chamber;
步骤J:基于泡浆比5:1和水胶比1:2.4,轻质氧化镁15%,粉煤灰25%,水泥60%,计算混合搅拌时所需的水、水泥、轻质氧化镁以及粉煤灰的用量并将其准备好;Step J: Calculate the water, cement, and light magnesia required for mixing based on the foam slurry ratio of 5:1 and water-cement ratio of 1:2.4, light magnesium oxide 15%, fly ash 25%, and cement 60%. and the amount of fly ash and its preparation;
步骤K:将水、水泥、轻质氧化镁以及粉煤灰混合搅拌,配置得到水泥浆;Step K: mixing and stirring water, cement, light magnesia and fly ash to prepare cement slurry;
步骤L:打开泡沫出口管阀门,将配置好的水泥浆倒入进浆口;Step L: Open the valve of the foam outlet pipe, and pour the prepared cement slurry into the slurry inlet;
步骤M:打开电机,中空螺旋杆顺时针旋转,搅拌筒逆时针旋转,泡沫从出泡圆孔排出,并与水泥浆一起螺旋向前运动;Step M: Turn on the motor, the hollow screw rod rotates clockwise, the mixing drum rotates counterclockwise, the foam is discharged from the foam hole, and moves forward in a spiral together with the cement slurry;
步骤N:根据密度检测计的读数读出泡沫水泥浆的密度;Step N: read the density of the foamed cement slurry according to the reading of the density detector;
步骤O:根据PH检测计读取泡沫水泥浆的PH值;Step 0: read the pH value of the foamed cement slurry according to the pH detector;
步骤P:制备所得的泡沫水泥浆从出浆口排出,关闭电机;Step P: The prepared foamed cement slurry is discharged from the slurry outlet, and the motor is turned off;
步骤Q:得到所需的泡沫水泥浆。Step Q: Obtain the required foam cement slurry.
优选的,制备泡沫水泥浆过程中的计算公式为:Preferably, the calculation formula in the process of preparing foamed cement slurry is:
C=0.426X×ZC=0.426X×Z
D=0.1775X×ZD=0.1775X×Z
E=0.1065X×ZE=0.1065X×Z
其中,X为实验所计划制备的泡沫水泥浆的体积,Y为为发泡液的发泡倍率,Z为试验测得泡沫水泥浆的密度,K为发泡液的密度,A为实验所需发泡液体积,B为搅拌水泥所需水的质量,C为所需水泥质量,D为所需粉煤灰的质量,E为所需轻质氧化镁的质量。Among them, X is the volume of the foamed cement slurry planned for the experiment, Y is the foaming ratio of the foaming liquid, Z is the density of the foamed cement slurry measured by the test, K is the density of the foaming liquid, and A is the required density of the experiment. The volume of foaming liquid, B is the quality of water required for mixing cement, C is the required quality of cement, D is the required quality of fly ash, and E is the required quality of light magnesium oxide.
本发明与现有技术相比,具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明所要解决的技术问题是,提供一种适用于制备水基泡沫并将其与水泥浆混合搅拌的装置,该装置通过不同气瓶提供制备泡沫所需的气体;通过烧瓶提供温度恒定的发泡液;通过发泡器制备细腻,稳定,均匀的水基泡沫;通过混合器将所制备水基泡沫与水泥浆混合搅拌,得到破泡率低,泡沫与水泥浆接触面积大,各项性能能够满足工程需要的泡沫水泥浆;通过设计的工作步骤控制发泡与混合的步调一致。此外,该装置的结构设计简洁,成本较低。The technical problem to be solved by the present invention is to provide a device suitable for preparing water-based foam and mixing it with cement slurry. The device provides the gas required for preparing foam through different gas cylinders; Foam liquid; fine, stable and uniform water-based foam is prepared through a foamer; the prepared water-based foam and cement slurry are mixed and stirred through a mixer to obtain a low foam breaking rate, a large contact area between the foam and the cement slurry, and various properties Foam cement slurry that can meet the needs of the project; control the foaming and mixing steps through the designed working steps. In addition, the structure design of the device is simple and the cost is low.
附图说明Description of drawings
图1为本发明一种适用于制备水基泡沫并将其与水泥浆混合搅拌的装置的示意图;Fig. 1 is a kind of schematic diagram of the device that is suitable for preparing water-based foam and mixing it with cement slurry of the present invention;
图2为本发明泡沫腔室内部示意图;Fig. 2 is a schematic diagram inside the foam chamber of the present invention;
图3为本发明自制PH计样式及测量原理。Fig. 3 is the style and measurement principle of the self-made pH meter of the present invention.
1-气瓶、2-气压控制器、3-气瓶阀门、4-气体入口管、5-T型三通管、6-烧瓶、7-恒温加热器、8-烧瓶阀门、9-发泡液入口管、10-泡沫腔室、11-多孔介质、12-填充物、13-排放管、14-泡沫出口管、15-泡沫出口管阀门、16-轴承、17-进浆口、18-内轴叶片、19-出泡圆孔、20-外轴叶片、21-搅拌筒、22-中空螺旋杆、23-密度检测计、24-出浆口、25-PH检测计、26-电机。1-gas cylinder, 2-air pressure controller, 3-gas cylinder valve, 4-gas inlet pipe, 5-T-type tee pipe, 6-flask, 7-constant temperature heater, 8-flask valve, 9-foaming Liquid inlet pipe, 10-foam chamber, 11-porous medium, 12-filler, 13-discharge pipe, 14-foam outlet pipe, 15-foam outlet pipe valve, 16-bearing, 17-slurry inlet, 18- Inner shaft blade, 19-foaming round hole, 20-outer shaft blade, 21-stirring drum, 22-hollow screw rod, 23-density detector, 24-pulp outlet, 25-PH detector, 26-motor.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其它实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.
实施例1Example 1
本发明实施例提供了一种发泡与混合设备,如图1所示,其中提供气体的设备为气瓶1,气瓶1配置有气压控制器2和气瓶阀门3;提供发泡液的设备为烧瓶6,置有恒温加热器7,活动底板以及烧瓶阀门8;发泡设备包括气体入口管4、发泡液入口管9、T型三通管5、泡沫腔室及其活动底板10、多孔介质11、填充物12、排放管13、泡沫出口管14以及泡沫出口管阀门15;所述设备通过所述气瓶1为发泡提供气体原料,基于气压控制器2控制通气时的气压,基于气瓶阀门3控制通气速度,基于所述气体入口管4通入气体,基于所述烧瓶6存放发泡液,基于所述恒温加热器7控制发泡液温度,基于所述活动底板控制烧瓶6开关,基于所述烧瓶阀门8控制通入液体的速度,基于发泡液入口管9通入发泡液,基于所述T型三通管5将气体入口管4,发泡液入口管9,发泡筒相连接,基于所述泡沫腔室及其活动底板10储存制备得到的水基泡沫,基于多孔介质11和填充物12使所制备泡沫细腻,均匀,稳定,基于所述发泡筒进行发泡全过程,排放管13可以将没有充分发泡的稀释液排出,基于所述排放管13排出未完全发泡的液体,基于所述泡沫出口管14将泡沫通入混合器,基于所述泡沫出口管阀门15控制通入时间。The embodiment of the present invention provides a kind of foaming and mixing equipment, as shown in Figure 1, wherein the equipment for providing gas is a gas cylinder 1, and the gas cylinder 1 is equipped with an air pressure controller 2 and a gas cylinder valve 3; the equipment for providing foaming liquid It is a flask 6 equipped with a constant temperature heater 7, a movable bottom plate and a flask valve 8; the foaming equipment includes a gas inlet pipe 4, a foaming liquid inlet pipe 9, a T-shaped tee pipe 5, a foam chamber and a movable bottom plate 10, Porous medium 11, filler 12, discharge pipe 13, foam outlet pipe 14 and foam outlet pipe valve 15; said equipment provides gas raw material for foaming through said gas cylinder 1, and the air pressure during ventilation is controlled based on air pressure controller 2, Control the venting speed based on the cylinder valve 3, feed gas based on the gas inlet pipe 4, store the foaming liquid based on the flask 6, control the temperature of the foaming liquid based on the constant temperature heater 7, and control the flask based on the movable bottom plate 6 switches, based on the flask valve 8 to control the speed of feeding the liquid, based on the foaming liquid inlet pipe 9 into the foaming liquid, based on the T-shaped tee pipe 5 the gas inlet pipe 4, the foaming liquid inlet pipe 9 , the foaming cylinder is connected, based on the foam chamber and its movable floor 10 to store the prepared water-based foam, based on the porous medium 11 and the filler 12, the prepared foam is fine, uniform and stable, based on the foaming cylinder Carry out the whole process of foaming, the discharge pipe 13 can discharge the diluent that is not fully foamed, discharge the liquid that is not completely foamed based on the discharge pipe 13, and feed the foam into the mixer based on the foam outlet pipe 14, based on the The foam outlet pipe valve 15 controls the passage time.
如图2所示,泡沫腔室10底部设置活动挡板,泡沫出口管14上设置阀门,可以较好的将泡沫储存于泡沫腔室之中,等待水泥浆混合完毕后打开阀门,可以精确控制泡沫与水泥浆同时通入混合器中,有效减少了材料的损耗和设备的磨损。泡沫腔室10有各种不同容积,同时泡沫腔室10为可拆卸式,可以根据工程所需泡沫的量精确选择不同容积的泡沫腔室10安装于发泡器中。泡沫腔室10左侧设置有活塞,表面设置有刻度,在阀门打开后可以通过压缩活塞精确推动泡沫进入后续的混合器中。As shown in Figure 2, a movable baffle is set at the bottom of the foam chamber 10, and a valve is set on the foam outlet pipe 14, so that the foam can be stored in the foam chamber preferably, and the valve can be opened after the cement slurry is mixed, which can precisely control Foam and cement slurry are passed into the mixer at the same time, effectively reducing material loss and equipment wear. The foam chambers 10 have various volumes, and the foam chambers 10 are detachable, and the foam chambers 10 with different volumes can be accurately selected and installed in the foam generator according to the amount of foam required by the project. A piston is provided on the left side of the foam chamber 10, and a scale is provided on the surface. After the valve is opened, the foam can be precisely pushed into the subsequent mixer by compressing the piston.
具体的,所述气压控制器2设置于所述气瓶1左上侧,所述气瓶阀门3位于气瓶1的出口处,所述气瓶1与所述气体入口管4连接,所述气体入口管4的右侧与所述T型三通管5的左端导口连接,所述气瓶1基于所述气体入口管4通入所需气体。所述恒温控制器7设置于所述烧瓶6外侧,所述烧瓶阀门8设置于所述烧瓶6出口处,所述烧瓶6与所述发泡液入口管9连接,所述发泡液入口管9下部与所述T型三通管5的上部导口连接,所述T型三通管5的右侧导口与所述发泡筒连接,完成对原材料的通入及发泡;所述发泡筒的放置形式采用垂直放置(气液运动方向与钢板重力方向相反)的方式,最下方为排放管13、内部为填充物12和多孔介质11、顶部为泡沫腔室及其挡板10,垂直放置的气液流向与重力方向相反的形式相当于引入了鼓泡效应,利于泡沫的生成。T型三通管5的设置,结构简单,易于加工制作,成本较低,可以同时将气体和发泡液通入发泡器内部,控制所得泡沫质量。Specifically, the air pressure controller 2 is arranged on the upper left side of the gas cylinder 1, the gas cylinder valve 3 is located at the outlet of the gas cylinder 1, the gas cylinder 1 is connected to the gas inlet pipe 4, and the gas cylinder 1 The right side of the inlet pipe 4 is connected to the left end of the T-shaped tee pipe 5 , and the gas cylinder 1 is fed with required gas based on the gas inlet pipe 4 . The thermostatic controller 7 is arranged on the outside of the flask 6, the flask valve 8 is arranged at the outlet of the flask 6, the flask 6 is connected to the foaming liquid inlet pipe 9, and the foaming liquid inlet pipe 9. The lower part is connected to the upper guide port of the T-shaped tee pipe 5, and the right guide port of the T-shaped tee pipe 5 is connected to the foaming tube to complete the feeding and foaming of raw materials; The foam cylinder is placed vertically (the gas-liquid movement direction is opposite to the gravity direction of the steel plate), the bottom is the discharge pipe 13, the interior is the filler 12 and the porous medium 11, and the top is the foam chamber and its baffle 10 , the vertically placed gas-liquid flow direction is opposite to the direction of gravity, which is equivalent to introducing a bubbling effect, which is beneficial to the generation of foam. The arrangement of the T-shaped three-way pipe 5 has a simple structure, is easy to process and manufacture, and has low cost. It can simultaneously pass gas and foaming liquid into the foamer to control the quality of the obtained foam.
优选的,烧瓶6倒置,烧瓶侧壁标有刻度,通入发泡液较为容易便捷,且能精确控制通入发泡液的体积。Preferably, the flask 6 is inverted, and the side wall of the flask is marked with scales, so that it is relatively easy and convenient to feed the foaming liquid, and the volume of the foaming liquid can be precisely controlled.
进一步的,气瓶1内填充的气体为二氧化碳,调节气压控制器2读数为0.2kpa,烧瓶6内采用的发泡液配比为茶皂素4g/L,选择的稳泡剂配比为十二烷基5g/L,增稠剂为聚丙烯酸钠2g/L,调节恒温加热器7将温度控制恒定在25摄氏度,通过气瓶1提供二氧化碳气体,通过烧瓶6提供所发泡液,二者混合进行发泡。所述发泡液无毒无污染。Further, the gas filled in the gas cylinder 1 is carbon dioxide, the reading of the air pressure controller 2 is adjusted to be 0.2kpa, the foaming liquid ratio adopted in the flask 6 is tea saponin 4g/L, and the selected foam stabilizer ratio is ten Dialkyl 5g/L, thickener is sodium polyacrylate 2g/L, regulates thermostatic heater 7 and temperature is controlled constant at 25 degrees centigrade, provides carbon dioxide gas by cylinder 1, provides institute's foaming liquid by flask 6, both Mix to foam. The foaming liquid is non-toxic and pollution-free.
进一步的,填充物12为钢棉,多孔介质11为钢丝网。所述钢丝网设置三层,所述钢丝网的孔径由下而上分别为0.1mm,0.5mm,1.0mm。钢棉填充在钢丝网之间。泡沫腔室10内设置钢丝网,钢丝网之间填充有钢棉,钢丝网的孔隙率逐渐增大,钢丝网和钢棉同时作用可形成湍流涡旋,而随着孔隙率的逐渐增大,泡沫孔径变大并均匀。多孔介质11采用的是钢丝网,填充物12采用钢棉,综合考虑了考工程实效性与经济适用性。Further, the filler 12 is steel wool, and the porous medium 11 is steel wire mesh. The steel wire mesh is provided with three layers, and the apertures of the steel wire mesh are 0.1 mm, 0.5 mm, and 1.0 mm from bottom to top. Steel wool is filled between the steel wire mesh. A steel wire mesh is arranged in the foam chamber 10, steel wool is filled between the steel mesh, the porosity of the steel mesh increases gradually, and the simultaneous action of the steel mesh and the steel wool can form a turbulent vortex, and as the porosity gradually increases, The foam cells become larger and uniform. The porous medium 11 is made of steel wire mesh, and the filler 12 is made of steel wool, which comprehensively considers the engineering effectiveness and economic applicability.
本发明的混合设备包括轴承16、进浆口17、内轴叶片18、出泡圆孔19、外轴叶片20、搅拌筒21、中空螺旋杆22、密度检测计23、出浆口24、PH检测计25、电机26。所述混合设备通过所述轴承16控制所述搅拌筒21、中空螺旋杆22转动,通过所述进浆口17引入未与泡沫混合的水泥浆液,通过所述出泡圆孔19使得发泡器所制泡沫流出,通过所述内轴叶片18、外轴叶片20对水泥浆和泡沫进行混合搅拌,通过所述搅拌筒21、中空螺旋杆22旋转带动叶片转动,通过所述出浆口24排出制备得到的二氧化碳泡沫水泥浆,通过电机26提供带动搅拌筒、中空螺旋旋转的动力,通过密度检测计23和PH检测计25测量泡沫的相关性能。The mixing equipment of the present invention comprises a bearing 16, a pulp inlet 17, an inner shaft blade 18, a bubble hole 19, an outer shaft blade 20, a mixing drum 21, a hollow screw rod 22, a density detector 23, a pulp outlet 24, a pH Detector 25, motor 26. The mixing device controls the rotation of the mixing drum 21 and the hollow screw 22 through the bearing 16, introduces the cement slurry that is not mixed with the foam through the slurry inlet 17, and makes the foamer through the foaming circular hole 19. The prepared foam flows out, and the cement slurry and foam are mixed and stirred by the inner shaft blade 18 and the outer shaft blade 20, and the blade is rotated by the rotation of the mixing drum 21 and the hollow screw rod 22, and is discharged through the slurry outlet 24 The prepared carbon dioxide foam cement slurry is powered by the motor 26 to drive the mixing drum and the hollow spiral, and the related properties of the foam are measured by the density detector 23 and the pH detector 25 .
具体的,所述搅拌筒21整体为水平放置,左端连接发泡设备中的泡沫出口管14,所述中空螺旋杆22位于其内部并与泡沫出口管14的右端相连,所述出泡圆孔19均匀设置于中空螺旋杆22上,搅拌筒21的右端设置有电机26。所述进浆口17和出浆口24分别位于搅拌筒的左上部和右下部。所述密度检测计23和PH检测计25分别设置在搅拌筒内侧,位于搅拌筒的最右端的上部。Specifically, the mixing drum 21 is placed horizontally as a whole, and the left end is connected to the foam outlet pipe 14 in the foaming equipment. The hollow screw rod 22 is located inside and connected to the right end of the foam outlet pipe 14. 19 is evenly arranged on the hollow screw rod 22, and the right end of the mixing drum 21 is provided with a motor 26. The slurry inlet 17 and the slurry outlet 24 are respectively located at the upper left part and the lower right part of the mixing drum. The density detector 23 and the pH detector 25 are respectively arranged inside the mixing drum, and are located at the upper part of the rightmost end of the mixing drum.
所述内轴叶片18设置在中空螺旋杆22外部,所述外轴叶片20设置在搅拌筒21内侧。The inner shaft blade 18 is arranged outside the hollow screw rod 22 , and the outer shaft blade 20 is arranged inside the mixing drum 21 .
所述轴承16分为内部轴承和外部轴承两种,其中内部轴承控制所述中空螺旋杆22的转动,外部轴承控制所述搅拌筒21的转动。通过所述电机26提供动力,通过所述轴承16控制所述中空螺旋杆22和搅拌筒21反方向转动,带动内轴叶片18和外轴叶片20转动,通过进浆口17射入水泥浆,通过出泡圆孔19使泡沫析出,通过内轴叶片18和外轴叶片20转动对水泥浆和泡沫进行混合搅拌,通过出浆口24排出所得二氧化碳泡沫水泥浆,通过密度检测计23和PH检测计25测量所制备泡沫水泥浆的相关性能。The bearing 16 is divided into two types: an internal bearing and an external bearing, wherein the internal bearing controls the rotation of the hollow screw rod 22 , and the external bearing controls the rotation of the mixing drum 21 . Power is provided by the motor 26, the hollow screw rod 22 and the mixing drum 21 are controlled to rotate in the opposite direction through the bearing 16, and the inner shaft blade 18 and the outer shaft blade 20 are driven to rotate, and the cement slurry is injected through the slurry inlet 17, The foam is precipitated through the foaming hole 19, the cement slurry and the foam are mixed and stirred by the rotation of the inner shaft blade 18 and the outer shaft blade 20, and the resulting carbon dioxide foam cement slurry is discharged through the slurry outlet 24, and is detected by the density detector 23 and the pH A meter 25 was used to measure the related properties of the prepared foam cement slurry.
内部外部轴承分别控制中空螺旋杆22和搅拌筒21的转动,提高装置的稳定性。采用电机26控制中空螺旋杆22和搅拌筒21旋转,减少了人力消耗。每圈螺旋叶片螺距中心开有一个出泡圆孔19作为泡沫出口,增大了泡沫与水泥浆的接触面积,也使得泡沫分布均匀,减少了破泡率。中空螺旋杆22和搅拌筒21以相反方向转动,同样增大了泡沫与水泥浆的接触面积,并且提高了泡沫与浆液的混合均匀程度。内轴叶片采用螺旋形,显著提高搅拌效率,增大接触面积,减少了破泡率。内外轴叶片均采用不锈钢材料,减少了与泡沫长时间接触后生锈,强度下降的可能。Internal and external bearings respectively control the rotation of the hollow screw rod 22 and the mixing drum 21, improving the stability of the device. The motor 26 is used to control the rotation of the hollow screw rod 22 and the mixing drum 21, which reduces manpower consumption. There is a foaming circular hole 19 in the pitch center of each spiral blade as the foam outlet, which increases the contact area between the foam and the cement slurry, makes the foam evenly distributed, and reduces the foam breaking rate. The hollow screw rod 22 and the mixing drum 21 rotate in opposite directions, which also increases the contact area between the foam and the cement slurry, and improves the mixing uniformity of the foam and the slurry. The inner shaft blade adopts spiral shape, which significantly improves the stirring efficiency, increases the contact area, and reduces the foam breaking rate. Both the inner and outer shaft blades are made of stainless steel, which reduces the possibility of rust and strength decline after long-term contact with the foam.
进一步的,所述出泡圆孔19的孔径为1.0mm,以便之前所制备泡沫析出。Further, the hole diameter of the foaming circular hole 19 is 1.0 mm, so that the previously prepared foam is separated out.
进一步的,所述内轴叶片18为螺旋形,所述外轴叶片20为矩形,采用的材料均为不锈钢,可以增加搅拌面积,减少破泡率,提高搅拌效率同时防治叶片生锈,强度降低。Further, the inner shaft blade 18 is helical, the outer shaft blade 20 is rectangular, and the materials used are all stainless steel, which can increase the stirring area, reduce the foam breaking rate, improve the stirring efficiency and prevent the blade from rusting and reduce the strength. .
进一步的,所述搅拌筒21的旋转方向为逆时针,所述中空螺旋杆22的旋转方向为顺时针。同样使得搅拌接触面积增加,混合更为均匀充分。Further, the rotation direction of the mixing drum 21 is counterclockwise, and the rotation direction of the hollow screw rod 22 is clockwise. It also increases the stirring contact area and makes the mixing more uniform and sufficient.
进一步的,所述密度检测器23为音叉浓度计,所述音叉浓度计的型号为LDS-2100型音叉密度计,密度的测量范围为0-3g/cm3。所述PH计的采用PH试纸测量泡沫水泥浆的PH值。Further, the density detector 23 is a tuning fork densitometer, the model of the tuning fork densitometer is LDS-2100 tuning fork densitometer, and the measuring range of density is 0-3g/cm3. The pH meter adopts pH test paper to measure the pH value of the foam cement slurry.
如图3所示,PH测试计25可以可拆卸放置在搅拌桶21内。优选的,所述搅拌筒21上设有矩形孔洞,所述搅拌筒21的外侧靠近所述矩形孔洞一边的位置铰接设有矩形板,所述PH检测计25可拆卸设置在所述矩形板的内侧,所述搅拌筒21的外侧靠近所述矩形孔洞另外三边的位置固定设有凸块,所述凸块设有凹槽,所述矩形板的内侧设有3/4圈凸圈,所述凸圈与所述凹槽相适配,所述凸圈上设有锁孔,所述凸块上设有锁扣,所述锁孔与所述锁扣相适配。配套结构的设置保证了密闭的同时,可拆卸防止PH测试计25。As shown in FIG. 3 , the pH tester 25 can be detachably placed in the mixing tank 21 . Preferably, the mixing drum 21 is provided with a rectangular hole, and the outside of the mixing drum 21 is hinged with a rectangular plate near one side of the rectangular hole, and the pH detector 25 is detachably arranged on the rectangular plate. Inside, the outside of the mixing drum 21 is fixedly provided with bumps near the other three sides of the rectangular hole. The protruding ring is adapted to the groove, the protruding ring is provided with a lock hole, and the protrusion is provided with a lock catch, and the lock hole is adapted to the lock catch. The setting of the supporting structure ensures the airtightness, and at the same time, the pH tester 25 can be detachable.
实施例2Example 2
通常,我们采用涡轮式发泡器制备二氧化碳水基泡沫,采用人工方法手动混合水泥浆和二氧化碳水基泡沫。这种方法所制备的泡沫不够均匀稳定,极易破裂,同时混合搅拌时水泥浆和泡沫接触不够充分,制作完成后的试块强度低,水泥浆中的泡沫破裂较多。本发明改良制造发泡与混合设备进行发泡和搅拌,所制备泡沫质量得到提升,但是由于未能在泡沫进入混合器之时同步通入水泥浆,也没有定量计算的公式,这导致了大量材料的浪费以及设备的过度磨损。由此进一步对此装置进行了改进,并得到计算公式计算所需原材料。改进后的工作全过程如下:Usually, we use a turbo foamer to prepare CO2 water-based foam, and manually mix the cement slurry and CO2 water-based foam by manual method. The foam prepared by this method is not uniform and stable enough, and it is very easy to break. At the same time, the contact between the cement slurry and the foam is not sufficient when mixing and stirring. The invention improves the manufacturing of foaming and mixing equipment for foaming and stirring, and the quality of the prepared foam is improved. However, because the cement slurry cannot be fed into the mixer simultaneously when the foam enters the mixer, and there is no formula for quantitative calculation, this results in a large amount of material waste and excessive wear and tear on equipment. Thus, the device is further improved, and the raw materials required for the calculation formula are obtained. The whole process of the improved work is as follows:
步骤A:选择发泡剂茶皂素,茶皂素的量为4g/L,稳泡剂十二烷基,十二烷基的量为5g/L,增稠剂为聚丙烯酸钠,聚丙烯酸钠的量为2g/L制备发泡液,固定发泡液温度为25摄氏度,通入二氧化碳气体制备少量泡沫,据此计算发泡液的发泡倍率Y。将制备完成的泡沫根据5:1的泡浆比与水泥浆混合搅拌得到泡沫水泥浆,并测量得到其密度Z。Step A: select whipping agent tea saponin, the amount of tea saponin is 4g/L, foam stabilizer dodecyl, the amount of dodecyl is 5g/L, thickener is sodium polyacrylate, polyacrylic acid The amount of sodium is 2g/L to prepare a foaming liquid, the temperature of the foaming liquid is fixed at 25 degrees Celsius, a small amount of foam is prepared by feeding carbon dioxide gas, and the foaming ratio Y of the foaming liquid is calculated accordingly. The prepared foam was mixed with cement slurry according to the foam slurry ratio of 5:1 to obtain foam cement slurry, and its density Z was measured.
步骤B:确定实验所需泡沫水泥浆的用量X,根据先前步骤A中的实验所得的泡沫水泥浆的密度Z,泡浆比5:1计算搅拌所需泡沫的量,选择发泡剂茶皂素,茶皂素的量为4g/L,稳泡剂十二烷基,十二烷基的量为5g/L,增稠剂为聚丙烯酸钠,聚丙烯酸钠的量为2g/L。根据步骤A得到发泡液的发泡倍率为Y,据此定量制作发泡剂稀释液,打开烧瓶6底部的活动挡板,将其通入烧瓶6,关闭挡板,关闭阀门,开启恒温加热器使其温度恒定为25摄氏度。Step B: Determine the amount X of the foam cement slurry required for the experiment, calculate the amount of foam required for stirring according to the density Z of the foam cement slurry obtained in the experiment in the previous step A, and the foam slurry ratio is 5:1, and select the foaming agent tea soap Plain, the amount of tea saponin is 4g/L, foam stabilizer lauryl, the amount of lauryl is 5g/L, thickener is sodium polyacrylate, and the amount of sodium polyacrylate is 2g/L. According to step A, the foaming rate of the foaming liquid is Y, and quantitatively make the foaming agent diluent accordingly, open the movable baffle at the bottom of the flask 6, pass it into the flask 6, close the baffle, close the valve, and turn on constant temperature heating Keep the temperature constant at 25°C.
步骤C:气瓶1内所填充的气体应该为惰性,本次实验为了探究二氧化碳泡沫水泥浆的各种性质,选择二氧化碳为发泡时所用的气体,获取相对应的气瓶,调节气压控制器,控制气压为0.2kpa,关闭阀门。Step C: The gas filled in the gas cylinder 1 should be inert. In order to explore the various properties of the carbon dioxide foam cement slurry in this experiment, choose carbon dioxide as the gas used for foaming, obtain the corresponding gas cylinder, and adjust the air pressure controller , control the air pressure to 0.2kpa, and close the valve.
步骤D:气体入口管4与T型三通管5连接,气体入口管4与气瓶连接;泡沫腔室10与T型三通管5的分支管连接,T型三通管5的另外一个分支管与烧瓶6连接;Step D: The gas inlet pipe 4 is connected to the T-shaped tee pipe 5, the gas inlet pipe 4 is connected to the gas cylinder; the foam chamber 10 is connected to the branch pipe of the T-shaped tee pipe 5, and the other branch of the T-shaped tee pipe 5 Branch pipe is connected with flask 6;
步骤E:每个泡沫腔室10容积不同,根据先前步骤B可知本次实验所需泡沫的量,据此挑选容积合适的泡沫腔室进行安装,将泡沫腔室左侧的活塞拉至最左侧。Step E: The volume of each foam chamber 10 is different. According to the previous step B, the amount of foam required for this experiment can be known. Based on this, select a foam chamber with a suitable volume for installation, and pull the piston on the left side of the foam chamber to the far left side.
步骤F:同时打开气瓶和烧瓶6的阀门,打开泡沫腔室底部的活动挡板,关闭泡沫入口管处的阀门,控制气体液体的流速,开始发泡。Step F: Simultaneously open the valves of the gas cylinder and flask 6, open the movable baffle at the bottom of the foam chamber, close the valve at the foam inlet pipe, control the flow rate of the gas and liquid, and start foaming.
步骤G:稀释的发泡剂溶液和一定压力的某种气体进入发泡筒下部,多孔介质11和填充物12的作用,泡沫在发泡筒内逐渐上升,打开泡沫腔室底部的挡板。Step G: The diluted blowing agent solution and a certain gas under certain pressure enter the lower part of the foaming cylinder, the porous medium 11 and the filler 12, the foam gradually rises in the foaming cylinder, and the baffle at the bottom of the foam chamber is opened.
步骤H:随着孔隙率的逐渐增大,泡沫孔径变大且均匀。Step H: With the gradual increase of porosity, the foam pore size becomes larger and uniform.
步骤I:得到细腻,稳定,均匀的水基泡沫,关闭泡沫腔室底部的挡板,使得泡沫储存在泡沫腔室内部。此时,发泡过程结束,我们得到实验所需的二氧化碳水基泡沫并将其储存在泡沫腔室内部,下面进行水泥浆的搅拌工作,并将其与泡沫同步通入混合其中。Step I: To obtain fine, stable and uniform water-based foam, close the baffle at the bottom of the foam chamber so that the foam is stored inside the foam chamber. At this point, the foaming process is over, and we get the carbon dioxide water-based foam required for the experiment and store it inside the foam chamber, then the cement slurry is stirred, and it is mixed with the foam synchronously.
步骤J:先前步骤B中确定了实验所需泡沫水泥浆的量X,通过泡浆比5:1和水胶比1:2.4以及各种胶凝材料所占比例——轻质氧化镁15%,粉煤灰25%,水泥60%,计算混合搅拌时所需的水、水泥、轻质氧化镁以及粉煤灰的用量并将其准备好。Step J: The amount X of the foam cement slurry required for the experiment was determined in the previous step B, through the ratio of foam slurry 5:1 and water-binder ratio 1:2.4 and the proportion of various cementitious materials - light magnesium oxide 15% , fly ash 25%, cement 60%, calculate the amount of water, cement, light magnesia and fly ash required for mixing and mixing and prepare them.
步骤K:将水与水泥及其他材料混合搅拌,得到水泥浆。Step K: mixing water with cement and other materials to obtain cement slurry.
步骤L:打开泡沫入口管处的阀门,根据实验要求缓慢推动活塞,使得泡沫进入混合器中,同时将先前所制备的水泥浆倒入混合器的进浆口,打开电机。Step L: Open the valve at the foam inlet pipe, slowly push the piston according to the experimental requirements, so that the foam enters the mixer, and at the same time pour the previously prepared cement slurry into the slurry inlet of the mixer, and turn on the motor.
步骤M:电机使中空螺旋杆顺时针转动,使搅拌筒逆时针转动,泡沫从出泡圆孔排出与水泥浆一起螺旋向前运动;螺旋形内轴叶片和矩形外轴叶片反方向同时搅拌混合。Step M: The motor rotates the hollow screw rod clockwise, which makes the mixing drum rotate counterclockwise, and the foam is discharged from the foaming hole and moves forward in a spiral with the cement slurry; the spiral inner shaft blade and the rectangular outer shaft blade are mixed in the opposite direction at the same time .
步骤N:根据音叉浓度计的读数读出泡沫水泥浆的密度Step N: Read the density of the foamed cement slurry according to the reading of the tuning fork concentration meter
步骤O:翻开PH检测计处的混合器侧壁,取出固定在侧壁上的PH试纸,根据试纸颜色读出泡沫水泥浆的PH值。Step O: Open the side wall of the mixer at the pH detector, take out the pH test paper fixed on the side wall, and read the pH value of the foam cement slurry according to the color of the test paper.
步骤P:制备所得的泡沫水泥浆从出浆口排出,关闭电机。Step P: The prepared foam cement slurry is discharged from the slurry outlet, and the motor is turned off.
步骤Q:得到所需的泡沫水泥浆。Step Q: Obtain the required foam cement slurry.
通过如下计算式计算本次实验所需水、水泥、粉煤灰、轻质氧化镁以及发泡液的量:Calculate the amount of water, cement, fly ash, light magnesia and foaming liquid required for this experiment by the following formula:
C=0.426X×ZC=0.426X×Z
D=0.1775X×ZD=0.1775X×Z
E=0.1065X×ZE=0.1065X×Z
其中,X为为实验前所定的所需泡沫水泥浆的体积,Y为为发泡液的发泡倍率,Z为先前实验根据密度计读出泡沫水泥浆的密度,K为发泡液的密度,A为实验所需发泡液体积,B为搅拌水泥所需水的质量,C为所需水泥质量,D为所需粉煤灰的质量,E为所需轻质氧化镁的质量。Among them, X is the volume of the required foam cement slurry determined before the experiment, Y is the foaming ratio of the foaming liquid, Z is the density of the foam cement slurry read by the densitometer in the previous experiment, and K is the density of the foaming liquid , A is the volume of foaming liquid required for the experiment, B is the quality of water required for mixing cement, C is the required quality of cement, D is the required quality of fly ash, and E is the required quality of light magnesium oxide.
本发明制备所得水基泡沫具有均匀的泡沫结构,较高的发泡倍数,一定的稳定时间。The water-based foam prepared by the invention has a uniform foam structure, a relatively high expansion ratio and a certain stable time.
基于抗压强度、密度两个最重要性能指标优选各材料组分配比后,对二氧化碳泡沫复合水泥浆液展开力学性能测定,包括结石率、析水率、凝结时间和流动度,对比泡沫水泥浆液性能标准分析二氧化碳泡沫水泥浆液注浆应用性,凝结时间采用典型维卡仪测定,流动度采用截锥圆模法测定,试验结果如下表所示:After optimizing the proportion of each material component based on the two most important performance indicators of compressive strength and density, the mechanical properties of the carbon dioxide foam composite cement slurry were measured, including stone formation rate, water separation rate, setting time and fluidity, and the performance of the foamed cement slurry was compared. The standard analyzes the applicability of carbon dioxide foam cement slurry grouting. The setting time is measured by a typical Vicat instrument, and the fluidity is measured by the truncated cone circular mold method. The test results are shown in the following table:
表1泡沫复合水泥浆液力学性能测定表Table 1 Determination of mechanical properties of foam composite cement slurry
从表可知,经外掺剂改性后的二氧化碳泡沫水泥结石体,抗压强度远远超过泡沫水泥强度标准,高于普通水泥结石体,密度、结石率和析水率均满足泡沫水泥浆液要求;泡沫水泥初凝时间为146min,终凝时间413min,满足凝结时间要求,较普通水泥浆液开始凝结时间45min、最终凝结时间390min较长,原因是浆液中大量自由水储存在泡沫体系的液膜中,自由水待泡沫消散后析出,延长了水化进程,同时泡沫的存在使得试样更加疏松多孔,延长水分的移动路径;流动度平均值为21cm,满足泡沫水泥流动度要求,较普通水泥浆液流动度16~18cm增大了约20%,说明水基泡沫的掺入增大了浆液材料的流动性。It can be seen from the table that the compressive strength of the carbon dioxide foam cement stone body modified by the external admixture far exceeds the strength standard of foam cement, and is higher than that of ordinary cement stone body, and the density, stone rate and water separation rate all meet the requirements of foam cement slurry The initial setting time of foam cement is 146 minutes, and the final setting time is 413 minutes, which meets the setting time requirements. It is longer than the initial setting time of 45 minutes and the final setting time of 390 minutes for ordinary cement grout, because a large amount of free water in the slurry is stored in the liquid film of the foam system , free water precipitates after the foam dissipates, which prolongs the hydration process. At the same time, the existence of foam makes the sample more loose and porous, prolonging the moving path of water; the average fluidity is 21cm, which meets the fluidity requirements of foam cement, which is higher than that of ordinary cement slurry The fluidity of 16-18cm increased by about 20%, indicating that the incorporation of water-based foam increased the fluidity of the slurry material.
本发明实施例提供了一种发泡与混合搅拌设备,该设备通过发泡器制备二氧化碳水基泡沫,通过混合器将二氧化碳水基泡沫与水泥浆进行混合搅拌,最终得到二氧化碳泡沫水泥浆用于现场工程,减少了二氧化碳的排放并为现场施工提供轻质高强的新型材料,成本低且对环境友好。The embodiment of the present invention provides a foaming and mixing equipment. The equipment prepares carbon dioxide water-based foam through a foamer, and mixes and stirs the carbon dioxide water-based foam and cement slurry through a mixer, and finally obtains carbon dioxide foam cement slurry for use in On-site engineering reduces carbon dioxide emissions and provides new light-weight, high-strength materials for on-site construction, which are low-cost and environmentally friendly.
总体上,该混设备具有泡沫破裂少,结构简单,混合均匀且可以连续生产大流量泡沫水泥浆的特点,同时该设备通过泡沫腔室的储存功能使得泡沫与水泥浆能够同时进入混合器进行搅拌,较少了材料的损耗以及设备的磨损。In general, the mixing equipment has the characteristics of less foam breakage, simple structure, uniform mixing and continuous production of large flow foam cement slurry. At the same time, the equipment uses the storage function of the foam chamber to allow foam and cement slurry to enter the mixer at the same time for mixing. , less material loss and equipment wear.
实际工程中,产生的泡沫水泥浆效果好坏主要取决于两个核心部件,及发泡器和混合器,本发明重新设计了孔隙式发泡器,现有技术关于这方面的设计较少。设计了双向搅拌型混合器,更贴切实际工程;In actual engineering, the effect of the foamed cement slurry produced mainly depends on two core components, the foamer and the mixer. The present invention redesigns the porous foamer, and there are few designs in the prior art in this regard. A two-way stirring mixer is designed, which is more suitable for practical engineering;
本申请通过发泡器和混合器的设计,可制备均匀细腻稳定的二氧化碳水基泡沫以及破泡率低,接触面积大,混合均匀的泡沫水泥浆。同时该设备结构简单、成本低廉、易于加工制作,可靠性高,产生的泡沫水泥浆能满足现场施工的要求。In this application, through the design of the foamer and the mixer, uniform, delicate and stable carbon dioxide water-based foam can be prepared, as well as foam cement slurry with low foam breaking rate, large contact area and uniform mixing. At the same time, the equipment has the advantages of simple structure, low cost, easy processing and high reliability, and the foamed cement slurry produced can meet the requirements of on-site construction.
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CN107139320A (en) * | 2017-06-26 | 2017-09-08 | 江苏中路交通科学技术有限公司 | A kind of high-performance foam concrete process units |
CN107225688A (en) * | 2017-07-20 | 2017-10-03 | 广东省机械研究所 | A kind of light soil process units and its autocontrol method |
CN109970404A (en) * | 2019-05-07 | 2019-07-05 | 河海大学 | A kind of shell foam concrete and preparation device and preparation method thereof |
CN210651189U (en) * | 2019-06-06 | 2020-06-02 | 山东省交通规划设计院 | Foaming device capable of controlling bubbles and metering |
CN110585947A (en) * | 2019-09-20 | 2019-12-20 | 西南石油大学 | A foam drilling fluid generating device |
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