CN109320041B - Slurry treatment system - Google Patents
Slurry treatment system Download PDFInfo
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- CN109320041B CN109320041B CN201811227948.5A CN201811227948A CN109320041B CN 109320041 B CN109320041 B CN 109320041B CN 201811227948 A CN201811227948 A CN 201811227948A CN 109320041 B CN109320041 B CN 109320041B
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- 239000002002 slurry Substances 0.000 title claims abstract 22
- 239000007788 liquid Substances 0.000 claims abstract description 58
- 238000010926 purge Methods 0.000 claims abstract description 39
- 238000012423 maintenance Methods 0.000 claims abstract description 30
- 238000012545 processing Methods 0.000 claims abstract description 4
- 238000003756 stirring Methods 0.000 claims abstract description 4
- 239000008394 flocculating agent Substances 0.000 claims abstract 6
- 238000000034 method Methods 0.000 claims description 5
- 239000004744 fabric Substances 0.000 claims description 3
- 239000007769 metal material Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 7
- 230000032258 transport Effects 0.000 description 5
- 238000010276 construction Methods 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/06—Sludge reduction, e.g. by lysis
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
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Abstract
Description
技术领域technical field
本发明涉及泥浆处理相关领域,具体涉及一种泥浆处理系统。The invention relates to the related field of mud treatment, in particular to a mud treatment system.
背景技术Background technique
随着科学技术的发展以及经济的发展,泥浆的用量越来越大,目前城市内的泥浆主要来源于建筑工程泥浆、市政污泥以及河道淤泥,随着城市化进程的不断加快,高层、超高层建筑、地铁、高速道路、大型桥梁等各类工程的建设越来越多,泥浆的产生量也越来越大。目前泥浆的处理方式主要有以下几种:1)罐装车(泥浆车)外运,该方式是将现场产生的泥浆直接通过泥浆泵提升至泥浆车中,通过泥浆车将泥浆运送到城市郊外的空闲场地进行自然干化;2)现场沉淀干化,该方式需要在施工现场修建沉淀池,将产生的泥浆排入其中,进行自然沉淀和干化;3)离心脱水,可以采用离心机对建筑泥浆进行脱水。With the development of science and technology and economic development, the amount of mud used is increasing. At present, the mud in the city mainly comes from construction engineering mud, municipal sludge and river silt. With the continuous acceleration of urbanization, high-rise, super There are more and more constructions of various projects such as high-rise buildings, subways, expressways, and large bridges, and the amount of mud produced is also increasing. At present, there are mainly the following ways to deal with mud: 1) Tanker truck (mud truck) for external transportation. This method is to directly lift the mud generated on site into the mud truck through the mud pump, and transport the mud to the outskirts of the city through the mud truck. 2) On-site sedimentation and drying, this method needs to build a sedimentation tank at the construction site, discharge the generated mud into it, and carry out natural sedimentation and drying; 3) Centrifugal dehydration, a centrifuge can be used to Construction mud is dewatered.
针对第3种方式“离心脱水”。在实际使用中,存在以下问题。For the third method "centrifugal dehydration". In actual use, there are the following problems.
1、现有技术的离心机外筒需要尺寸较大,原因是外筒容纳相对固态的泥部分,并要排出,其存在空间的浪费,但并不能因此缩小外筒的直径,因为缩小了以后不足以容纳大量的泥部分,因此造成困扰,解决手段往往是直接使用大直径外筒,但不符合小型化精细化的设计趋势。1. The outer cylinder of the centrifuge in the prior art needs to be larger in size, because the outer cylinder contains relatively solid mud and needs to be discharged, and there is a waste of space, but the diameter of the outer cylinder cannot be reduced because of the reduction. It is not enough to accommodate a large number of mud parts, so it causes troubles. The solution is often to directly use a large-diameter outer cylinder, but it does not meet the design trend of miniaturization and refinement.
2、现有技术的离心机缺乏维护手段,其清洗时只能清洗一部分,存在清洗死角。2. The centrifuge in the prior art lacks maintenance means, and only a part can be cleaned when it is cleaned, and there is a cleaning dead angle.
3、现有技术的离心机有一部分设有排液管或者集液管,其往往暴露在滚筒中,经受离心颗粒冲刷,当泥浆中存在石子时,易旋转击坏排液管;为此的解决办法往往是增大排液管的材料硬度,然而其提高了成本。3. A part of the centrifuge in the prior art is provided with a drain pipe or a liquid collecting pipe, which is often exposed in the drum and subjected to the erosion of centrifugal particles. When there are stones in the mud, it is easy to rotate and damage the drain pipe; for this reason The solution is often to increase the material hardness of the drain pipe, which however increases the cost.
4、现有技术的离心机下方设有卸料阀,然而其卸料阀直接受离心物料冲击,长时间后易产生松动甚至破坏。4. The bottom of the centrifuge in the prior art is provided with a discharge valve, but the discharge valve is directly impacted by the centrifuged material, which is prone to loosening or even damage after a long time.
5、现有技术的离心机长时间使用后,会堆积物料难以清除,即使水冲击也无法清除。5. After the centrifuge of the prior art is used for a long time, it will accumulate materials that are difficult to remove, even if it is impacted by water, it cannot be removed.
6、现有技术的泥浆处理系统,输送带输送时往往是随机落料到输送带上,无法控制,随机落料存在收集困难。6. In the mud processing system of the prior art, when the conveyor belt is conveying, the material is often randomly dropped onto the conveyor belt, which is uncontrollable, and it is difficult to collect the random material.
发明内容Contents of the invention
为了克服上述问题,本发明提出同时解决上述多种问题的方案。In order to overcome the above-mentioned problems, the present invention proposes a solution to simultaneously solve the above-mentioned multiple problems.
本发明解决其技术问题所采用的技术方案是:一种泥浆处理系统,包括集液箱、输送管道、离心机、离心机电机、控制阀、混合筒、絮凝剂泵、泥浆泵、泥浆池、混合筒电机、输送带、进泥管、卸料阀、支架;其中离心机包括第一弧、第二弧、第三弧、连接段、外壁、中壁、内壁、刮刀杆、刮刀、多功能槽、外维护盘、内维护盘、排液吹扫口、排液管顶壁、排液管、辅助吹扫口、排泥格栅;泥浆泵将泥浆池中的泥浆输送到混合筒,絮凝剂泵将絮凝剂输送到混合筒,混合筒电机驱动混合筒内部的叶片搅拌,混合筒与离心机之间连接控制阀,泥浆通过进泥管进入离心机,离心机排出的液体通过输送管道进入集液箱,离心机排出的泥通过卸料阀落在输送带上;所述泥浆处理系统还包括控制器;The technical solution adopted by the present invention to solve the technical problem is: a mud treatment system, including a liquid collection tank, a delivery pipeline, a centrifuge, a centrifuge motor, a control valve, a mixing cylinder, a flocculant pump, a mud pump, a mud tank, Mixing drum motor, conveyor belt, mud inlet pipe, discharge valve, bracket; the centrifuge includes the first arc, second arc, third arc, connecting section, outer wall, middle wall, inner wall, scraper rod, scraper, multi-function Groove, outer maintenance plate, inner maintenance plate, liquid discharge purge port, top wall of liquid discharge pipe, liquid discharge pipe, auxiliary purge port, mud discharge grille; the mud pump transports the mud in the mud pool to the mixing cylinder for flocculation The agent pump transports the flocculant to the mixing barrel, the mixing barrel motor drives the blades inside the mixing barrel to stir, the control valve is connected between the mixing barrel and the centrifuge, the mud enters the centrifuge through the mud inlet pipe, and the liquid discharged from the centrifuge enters through the delivery pipe The liquid collecting tank, the mud discharged from the centrifuge falls on the conveyor belt through the discharge valve; the mud processing system also includes a controller;
离心机与卸料阀都固定在所述支架上,离心机包括内筒和外筒,外筒包括第一弧、第二弧、第三弧、连接段,第一弧两端通过连接段分别连接第二弧与第三弧,第一弧的半径大于第二弧的半径,第一弧的半径大于第三弧的半径,第二弧与第三弧的半径相同,向下形成收口,收口的直径等于支架开口的直径,连接段不发生弯曲;所述内筒与所述外筒之间设有刮刀杆与刮刀,刮刀杆连接在内筒上,刮刀杆与刮刀的长度总和等于第二弧与第三弧到内筒的距离,小于连接段与第一弧到内筒的距离;所述内筒包括外壁、中壁、内壁,外壁与中壁之间的距离大于内壁与中壁之间的距离,所述排液管一部分在内壁与中壁之间,一部分在外壁与中壁之间;排液管与外壁之间留有空隙,排液管上设有径向向内朝向的排液管顶壁,排液管顶壁暴露在内壁外,排液管顶壁由金属材料制成;所述内壁为过滤层,其过滤后的液体通过排液管管壁上的小孔进入排液管;所述外壁、中壁、内壁上设有排泥格栅,所述排泥格栅将外壁与中壁之间的空间隔成若干子腔;Both the centrifuge and the discharge valve are fixed on the bracket. The centrifuge includes an inner cylinder and an outer cylinder. The outer cylinder includes a first arc, a second arc, a third arc, and a connecting section. The two ends of the first arc pass through the connecting section respectively. Connecting the second arc and the third arc, the radius of the first arc is greater than the radius of the second arc, the radius of the first arc is greater than the radius of the third arc, the radius of the second arc is the same as that of the third arc, forming a closing point downwards, closing The diameter is equal to the diameter of the bracket opening, and the connecting section does not bend; a scraper rod and a scraper are arranged between the inner cylinder and the outer cylinder, the scraper rod is connected to the inner cylinder, and the sum of the lengths of the scraper rod and the scraper is equal to the second The distance between the arc and the third arc and the inner cylinder is less than the distance between the connecting section and the first arc and the inner cylinder; the inner cylinder includes an outer wall, a middle wall, and an inner wall, and the distance between the outer wall and the middle wall is greater than the distance between the inner wall and the middle wall. The distance between the discharge pipe is partly between the inner wall and the middle wall, and a part is between the outer wall and the middle wall; there is a gap between the discharge pipe and the outer wall, and the discharge pipe is provided with radially inwardly facing The top wall of the discharge pipe, the top wall of the discharge pipe is exposed outside the inner wall, and the top wall of the discharge pipe is made of metal material; the inner wall is a filter layer, and the filtered liquid enters through the small holes on the wall of the discharge pipe Drainage pipe; the outer wall, the middle wall, and the inner wall are provided with a mud discharge grid, and the mud discharge grid divides the space between the outer wall and the middle wall into several sub-cavities;
所述内筒的一端设有外维护盘、内维护盘,外维护盘上设有多功能槽,所述内维护盘上设有排液吹扫口,所述排液吹扫口的位置对应于每个子腔的一端,多功能槽的数量与排液吹扫口的数量对应;所述内维护盘上还设有辅助吹扫口,所述辅助吹扫口的位置对应于内壁和中壁之间,通过外维护盘的转动,多功能槽交替对应排液吹扫口与辅助吹扫口;所述卸料阀包括第一气缸、第一闸板、承泥弧形壁、第二闸板、第二气缸、主体壁,离心机甩出的泥部分落在所述承泥弧形壁上,通过弧形壁卸载冲击能量并使泥由承泥弧形壁顺畅滑落到主体壁上,所述第一气缸于承泥弧形壁的上端驱动第一闸板,所述第二气缸于主体壁的上端驱动第二闸板。One end of the inner cylinder is provided with an outer maintenance plate and an inner maintenance plate, the outer maintenance plate is provided with a multifunctional groove, and the inner maintenance plate is provided with a liquid discharge purge port, and the position of the liquid discharge purge port corresponds to At one end of each sub-chamber, the number of multi-functional slots corresponds to the number of liquid discharge purge ports; the inner maintenance plate is also provided with auxiliary purge ports, and the positions of the auxiliary purge ports correspond to the inner wall and the middle wall. In between, through the rotation of the outer maintenance plate, the multi-functional tank alternately corresponds to the liquid discharge purge port and the auxiliary purge port; plate, the second cylinder, the main body wall, the mud thrown out by the centrifuge falls on the mud-bearing arc-shaped wall, the impact energy is unloaded through the arc-shaped wall and the mud slides smoothly from the mud-bearing arc-shaped wall to the main body wall, The first air cylinder drives the first ram on the upper end of the mud-bearing arc-shaped wall, and the second air cylinder drives the second ram on the upper end of the main body wall.
优选的,所述排液吹扫口的数量为四。Preferably, the number of the liquid discharge purge ports is four.
优选的,所述内筒内部设有开口连接进泥管。Preferably, an opening is provided inside the inner cylinder to connect to the mud inlet pipe.
优选的,所述控制阀为电动阀。Preferably, the control valve is an electric valve.
优选的,所述第一气缸、第二气缸驱动改为第一步进电机、第二步进电机驱动。Preferably, the driving of the first cylinder and the second cylinder is replaced by the driving of the first stepping motor and the second stepping motor.
优选的,所述过滤层为过滤布。Preferably, the filter layer is filter cloth.
优选的,所述第一气缸固定在所述支架上。Preferably, the first cylinder is fixed on the bracket.
优选的,所述第二气缸固定在所述主体壁上。Preferably, the second cylinder is fixed on the main body wall.
优选的,所述排液吹扫口旁设有浊度仪。Preferably, a turbidity meter is provided next to the liquid discharge purge port.
优选的,所述输送带末端设有收集容器。Preferably, a collection container is provided at the end of the conveyor belt.
本发明的有益效果是:The beneficial effects of the present invention are:
1、针对背景技术第1点,采用了多段式离心机外筒设计,既保留了足够的尺寸容纳泥部分,又节省了体积空间,同时离心机内筒与卸料阀的距离接近,更大辐射范围的泥可以直接进入卸料阀,避免先落在外筒再落入卸料阀,节省了步骤,避免了外筒中泥料堆积固化。1. Aiming at the first point of the background technology, a multi-stage centrifuge outer cylinder design is adopted, which not only retains enough size to accommodate the mud part, but also saves volume space, and at the same time, the distance between the centrifuge inner cylinder and the discharge valve is close and larger The mud in the radiation range can directly enter the discharge valve, avoiding falling into the outer cylinder first and then falling into the discharge valve, which saves steps and avoids the accumulation and solidification of mud in the outer cylinder.
2、针对背景技术第2点,采用了多功能槽交替与排液吹扫口、辅助吹扫口连通的方案,通过外维护盘与内维护盘的相对转动,实现交替。2. Aiming at the second point of the background technology, a scheme in which the multi-functional tanks alternately communicate with the liquid discharge purge port and the auxiliary purge port is adopted, and the alternation is realized through the relative rotation of the outer maintenance plate and the inner maintenance plate.
3、针对背景技术提出的第3点,采用了内筒壁三层设计,排液管埋设在三层壁之间进行排液。3. In view of the third point raised in the background technology, a three-layer design of the inner cylinder wall is adopted, and the liquid discharge pipe is buried between the three-layer walls for liquid drainage.
4、针对背景技术提出的第4点,设计出卸料阀的承泥壁与主体壁,通过承泥壁卸载掉离心的能量,使得落料更平稳,卸料阀使用寿命更长。4. Aiming at the fourth point of the background technology, the mud-bearing wall and the main body wall of the discharge valve are designed, and the centrifugal energy is unloaded through the mud-bearing wall, so that the discharge is more stable and the service life of the discharge valve is longer.
5、针对背景技术第5点,增设了刮板与连杆,设计在内外筒之间,提供更精细、效率更高的物料清洁。5. For
6、针对背景技术提出的第6点,工作状态时,首先开启第一闸板,关闭第二闸板,使得泥甩在承泥弧形壁上,并堆积在第二闸板上方,通过堆积的泥缓解落料冲击,然后开启所述第二闸板,使得泥落下,使得落料更平稳重量可控,卸料阀使用寿命更长,更重要的是由于积攒一段时间后一起落料,使得落料相对集中,便于在传送带末端进行收集。6. For the sixth point proposed in the background technology, in the working state, first open the first gate and close the second gate, so that the mud is thrown on the arc-shaped wall of the mud bearing and piled up on the second gate. The mud relieves the impact of falling material, and then opens the second gate to make the mud fall down, making the material fall more stable and weight controllable, and the service life of the discharge valve is longer. It makes the blanking relatively concentrated, which is convenient for collection at the end of the conveyor belt.
注:上述设计不分先后,每一条都使得本发明相对现有技术具有区别和显著的进步。Note: the above-mentioned designs are in no particular order, and each of them makes the present invention have difference and remarkable progress compared with the prior art.
附图说明Description of drawings
图1是本发明离心机与卸料阀整体示意图。Fig. 1 is an overall schematic diagram of a centrifuge and a discharge valve of the present invention.
图2是本发明离心机内筒剖视图。Fig. 2 is a sectional view of the inner cylinder of the centrifuge of the present invention.
图3是本发明离心机内筒主视图。Fig. 3 is a front view of the inner cylinder of the centrifuge of the present invention.
图4是本发明泥浆处理系统整体图。Fig. 4 is an overall view of the mud treatment system of the present invention.
图中,附图标记如下:In the figure, the reference signs are as follows:
1、第一弧2、第二弧3、第三弧4、连接段5、外壁6、中壁7、内壁8、刮刀杆9、刮刀10、支架11、第一气缸12、第一闸板13、承泥弧形壁14、第二闸板15、第二气缸16、主体壁17、多功能槽18、外维护盘19、内维护盘20、排液吹扫口21、排液管顶壁22、排液管23、辅助吹扫口24、排泥格栅25、集液箱26、输送管道27、离心机28、离心机电机29、控制阀30、混合筒31、絮凝剂泵32、泥浆泵33、泥浆池34、混合筒电机35、输送带36、进泥管37、卸料阀。1.
具体实施方式Detailed ways
下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
如图所示:一种泥浆处理系统,包括集液箱、输送管道、离心机、离心机电机、控制阀、混合筒、絮凝剂泵、泥浆泵、泥浆池、混合筒电机、输送带、进泥管、卸料阀、支架;其中离心机包括第一弧、第二弧、第三弧、连接段、外壁、中壁、内壁、刮刀杆、刮刀、多功能槽、外维护盘、内维护盘、排液吹扫口、排液管顶壁、排液管、辅助吹扫口、排泥格栅;泥浆泵将泥浆池中的泥浆输送到混合筒,絮凝剂泵将絮凝剂输送到混合筒,混合筒电机驱动混合筒内部的叶片搅拌,混合筒与离心机之间连接控制阀,泥浆通过进泥管进入离心机,离心机排出的液体通过输送管道进入集液箱,离心机排出的泥通过卸料阀落在输送带上;所述泥浆处理系统还包括控制器;As shown in the figure: a mud treatment system, including liquid collection tank, conveying pipeline, centrifuge, centrifuge motor, control valve, mixing cylinder, flocculant pump, mud pump, mud tank, mixing cylinder motor, conveyor belt, inlet Mud pipe, discharge valve, bracket; the centrifuge includes first arc, second arc, third arc, connecting section, outer wall, middle wall, inner wall, scraper rod, scraper, multi-functional tank, outer maintenance plate, inner maintenance Pan, liquid discharge purge port, top wall of liquid discharge pipe, liquid discharge pipe, auxiliary purge port, mud discharge grid; the mud pump transports the mud in the mud pool to the mixing cylinder, and the flocculant pump transports the flocculant to the mixing tank. The motor of the mixing cylinder drives the blades inside the mixing cylinder to stir. The control valve is connected between the mixing cylinder and the centrifuge. The mud enters the centrifuge through the mud inlet pipe. The mud falls on the conveyor belt through the discharge valve; the mud treatment system also includes a controller;
如图所示:离心机与卸料阀都固定在所述支架上,离心机包括内筒和外筒,外筒包括第一弧、第二弧、第三弧、连接段,第一弧两端通过连接段分别连接第二弧与第三弧,第一弧的半径大于第二弧的半径,第一弧的半径大于第三弧的半径,第二弧与第三弧的半径相同,向下形成收口,收口的直径等于支架开口的直径,连接段不发生弯曲;所述内筒与所述外筒之间设有刮刀杆与刮刀,刮刀杆连接在内筒上,刮刀杆与刮刀的长度总和等于第二弧与第三弧到内筒的距离,小于连接段与第一弧到内筒的距离;As shown in the figure: the centrifuge and the discharge valve are fixed on the bracket. The centrifuge includes an inner cylinder and an outer cylinder. The outer cylinder includes a first arc, a second arc, a third arc, and a connecting section. The ends are respectively connected to the second arc and the third arc through the connecting segment, the radius of the first arc is greater than the radius of the second arc, the radius of the first arc is greater than the radius of the third arc, the radius of the second arc is the same as that of the third arc, and A closing is formed at the bottom, the diameter of the closing is equal to the diameter of the bracket opening, and the connecting section does not bend; a scraper rod and a scraper are arranged between the inner cylinder and the outer cylinder, the scraper rod is connected to the inner cylinder, and the connection between the scraper rod and the scraper The sum of the lengths is equal to the distance from the second arc and the third arc to the inner cylinder, which is less than the distance from the connecting section and the first arc to the inner cylinder;
如图所示:所述内筒包括外壁、中壁、内壁,外壁与中壁之间的距离大于内壁与中壁之间的距离,所述排液管一部分在内壁与中壁之间,一部分在外壁与中壁之间;排液管与外壁之间留有空隙,排液管上设有径向向内朝向的排液管顶壁,排液管顶壁暴露在内壁外,排液管顶壁由金属材料制成;所述内壁为过滤层,其过滤后的液体通过排液管管壁上的小孔进入排液管;所述外壁、中壁、内壁上设有排泥格栅,所述排泥格栅将外壁与中壁之间的空间隔成若干子腔;所述内筒的一端设有外维护盘、内维护盘,外维护盘上设有多功能槽,所述内维护盘上设有排液吹扫口,所述排液吹扫口的位置对应于每个子腔的一端,多功能槽的数量与排液吹扫口的数量对应;所述内维护盘上还设有辅助吹扫口,所述辅助吹扫口的位置对应于内壁和中壁之间,通过外维护盘的转动,多功能槽交替对应排液吹扫口与辅助吹扫口;As shown in the figure: the inner cylinder includes an outer wall, a middle wall, and an inner wall. The distance between the outer wall and the middle wall is greater than the distance between the inner wall and the middle wall. A part of the drain pipe is between the inner wall and the middle wall, and a part is Between the outer wall and the middle wall; there is a gap between the drain pipe and the outer wall, the drain pipe is provided with a radially inward facing top wall of the drain pipe, the top wall of the drain pipe is exposed outside the inner wall, and the drain pipe The top wall is made of metal material; the inner wall is a filter layer, and the filtered liquid enters the drain pipe through the small holes on the wall of the drain pipe; the outer wall, middle wall, and inner wall are provided with mud discharge grilles , the mud discharge grid divides the space between the outer wall and the middle wall into several sub-cavities; one end of the inner cylinder is provided with an outer maintenance plate and an inner maintenance plate, and the outer maintenance plate is provided with a multifunctional groove. The internal maintenance plate is provided with a liquid discharge purge port, the position of the liquid discharge purge port corresponds to one end of each sub-cavity, and the number of multi-functional grooves corresponds to the number of liquid discharge purge ports; An auxiliary purge port is also provided. The position of the auxiliary purge port corresponds to the position between the inner wall and the middle wall. Through the rotation of the outer maintenance plate, the multi-functional tank alternately corresponds to the liquid discharge purge port and the auxiliary purge port;
如图所示:所述卸料阀包括第一气缸、第一闸板、承泥弧形壁、第二闸板、第二气缸、主体壁,离心机甩出的泥部分落在所述承泥弧形壁上,通过弧形壁卸载冲击能量并使泥由承泥弧形壁顺畅滑落到主体壁上,所述第一气缸于承泥弧形壁的上端驱动第一闸板,所述第二气缸于主体壁的上端驱动第二闸板。所述排液吹扫口的数量为四。所述内筒内部设有开口连接进泥管。所述控制阀为电动阀。所述第一气缸、第二气缸驱动改为第一步进电机、第二步进电机驱动。所述过滤层为过滤布。所述第一气缸固定在所述支架上。所述第二气缸固定在所述主体壁上。所述排液吹扫口旁设有浊度仪。所述输送带末端设有收集容器。As shown in the figure: the discharge valve includes a first cylinder, a first gate, a mud-bearing arc wall, a second gate, a second cylinder, and a main body wall. The mud thrown out by the centrifuge falls on the bearing On the mud arc-shaped wall, the impact energy is unloaded through the arc-shaped wall and the mud slides smoothly from the mud-bearing arc-shaped wall to the main body wall. The first cylinder drives the first gate on the upper end of the mud-bearing arc-shaped wall. The second air cylinder drives the second shutter on the upper end of the main body wall. The number of the liquid discharge purge ports is four. An opening is provided inside the inner cylinder to connect to the mud inlet pipe. The control valve is an electric valve. The drive of the first cylinder and the second cylinder is changed to the drive of the first stepper motor and the second stepper motor. The filter layer is filter cloth. The first air cylinder is fixed on the bracket. The second cylinder is fixed on the main body wall. A turbidity meter is arranged beside the liquid discharge purge port. A collection container is provided at the end of the conveyor belt.
上列详细说明是针对本发明可行实施例的具体说明,该实施例并非用以限制本发明的专利范围,凡未脱离本发明所为的等效实施或变更,均应包含于本案的专利范围中。The above detailed description is a specific description of the feasible embodiment of the present invention. This embodiment is not used to limit the patent scope of the present invention. Any equivalent implementation or change that does not deviate from the present invention should be included in the patent scope of this case. middle.
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Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4898571A (en) * | 1987-12-24 | 1990-02-06 | Klockner-Humboldt-Deutz Aktiengesellschaft | Solid bowl centrifuge |
| US6033564A (en) * | 1998-07-13 | 2000-03-07 | Phase, Inc. | Method of construction for density screening outer transport walls |
| US6939286B1 (en) * | 2002-04-29 | 2005-09-06 | Archon Technologies Inc. | Centrifuge for phase separation |
| JP2011064182A (en) * | 2009-09-18 | 2011-03-31 | Hokuetsu Kogyo Co Ltd | Control method for engine drive type air compressor and engine drive type air compressor |
| CN103706596A (en) * | 2012-09-28 | 2014-04-09 | 苏州久工自动化科技有限公司 | Gas purging and cleaning device |
| CN204509085U (en) * | 2015-03-24 | 2015-07-29 | 杭州沐阳建筑技术有限公司 | A kind of channel cleanout sludge dewatering system |
| CN106976930A (en) * | 2017-06-08 | 2017-07-25 | 长沙理工大学 | Hydrocyclone separator for sludge water, and treatment system and method for synchronous dissolution of sludge water concentration/coagulant |
| CN107930867A (en) * | 2017-11-29 | 2018-04-20 | 蚌埠市朗辰化工设备有限公司 | A kind of quickly discharging material device used for solid-liquid centrifugation machine |
| CN207402743U (en) * | 2017-09-18 | 2018-05-25 | 金石机器人常州股份有限公司 | The angular detent mechanism of differential casing |
| CN207462832U (en) * | 2017-11-14 | 2018-06-08 | 李国义 | A kind of gas filtration filter cylinder purges cleaner |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2410709B (en) * | 2004-02-07 | 2007-04-18 | Broadbent & Sons Ltd Thomas | Improving washing of separated solids in solid bowl and screen bowl decanting centrifuges |
-
2018
- 2018-10-22 CN CN201811227948.5A patent/CN109320041B/en not_active Expired - Fee Related
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4898571A (en) * | 1987-12-24 | 1990-02-06 | Klockner-Humboldt-Deutz Aktiengesellschaft | Solid bowl centrifuge |
| US6033564A (en) * | 1998-07-13 | 2000-03-07 | Phase, Inc. | Method of construction for density screening outer transport walls |
| US6939286B1 (en) * | 2002-04-29 | 2005-09-06 | Archon Technologies Inc. | Centrifuge for phase separation |
| JP2011064182A (en) * | 2009-09-18 | 2011-03-31 | Hokuetsu Kogyo Co Ltd | Control method for engine drive type air compressor and engine drive type air compressor |
| CN103706596A (en) * | 2012-09-28 | 2014-04-09 | 苏州久工自动化科技有限公司 | Gas purging and cleaning device |
| CN204509085U (en) * | 2015-03-24 | 2015-07-29 | 杭州沐阳建筑技术有限公司 | A kind of channel cleanout sludge dewatering system |
| CN106976930A (en) * | 2017-06-08 | 2017-07-25 | 长沙理工大学 | Hydrocyclone separator for sludge water, and treatment system and method for synchronous dissolution of sludge water concentration/coagulant |
| CN207402743U (en) * | 2017-09-18 | 2018-05-25 | 金石机器人常州股份有限公司 | The angular detent mechanism of differential casing |
| CN207462832U (en) * | 2017-11-14 | 2018-06-08 | 李国义 | A kind of gas filtration filter cylinder purges cleaner |
| CN107930867A (en) * | 2017-11-29 | 2018-04-20 | 蚌埠市朗辰化工设备有限公司 | A kind of quickly discharging material device used for solid-liquid centrifugation machine |
Non-Patent Citations (2)
| Title |
|---|
| 冯骉主编.《食品工程原理》.中国轻工业出版社,2013,(第第二版版),第107页. * |
| 费逸华 ; 周成蹊 ; .离心机系统在建筑泥浆减量化过程中的应用.建设科技.2015,(第05期),第108-109页. * |
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