WO2024087360A1 - 一种剥离液回收处理脱水装置 - Google Patents

一种剥离液回收处理脱水装置 Download PDF

Info

Publication number
WO2024087360A1
WO2024087360A1 PCT/CN2022/140378 CN2022140378W WO2024087360A1 WO 2024087360 A1 WO2024087360 A1 WO 2024087360A1 CN 2022140378 W CN2022140378 W CN 2022140378W WO 2024087360 A1 WO2024087360 A1 WO 2024087360A1
Authority
WO
WIPO (PCT)
Prior art keywords
wastewater
planetary
central
storage tank
stirring
Prior art date
Application number
PCT/CN2022/140378
Other languages
English (en)
French (fr)
Inventor
孙建东
秦龙飞
李俊霖
Original Assignee
联仕(昆山)化学材料有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 联仕(昆山)化学材料有限公司 filed Critical 联仕(昆山)化学材料有限公司
Publication of WO2024087360A1 publication Critical patent/WO2024087360A1/zh

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/048—Purification of waste water by evaporation
    • 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
    • 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
    • B01F27/95—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with stirrers having planetary motion, i.e. rotating about their own axis and about a sun axis
    • B01F27/951—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with stirrers having planetary motion, i.e. rotating about their own axis and about a sun axis with at least one stirrer mounted on the sun axis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/90—Heating or cooling systems
    • B01F35/92—Heating or cooling systems for heating the outside of the receptacle, e.g. heated jackets or burners
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/305—Treatment of water, waste water or sewage

Definitions

  • the invention relates to the technical field of wastewater treatment, in particular to a stripping liquid recovery and dehydration device.
  • Photoresist stripping liquid is a cleaning agent used in the chip packaging process. Its purpose is to remove the photoresist on the positive and negative electrodes of the packaged chip products, so it is also called photoresist stripping liquid. Its main components are organic ammonia and polar organic solvents, and it also contains light components represented mainly by water. After use, in addition to containing a small amount of photoresist particles, the main components of the stripping liquid are still organic ammonia and polar organic solvents. Therefore, the used stripping liquid can be recycled and dehydrated, and then purified by classification to make it valuable for reuse.
  • the existing technical means include heating the stripping liquid wastewater in the wastewater storage tank through an electric heating wire, and dehydrating the stripping liquid wastewater in the form of water bath heating through a cooling tower.
  • the dehydration method of heating in a water bath through a cooling tower has better heating uniformity and safety, but it still has the following problems to be solved: the central stirring blade cannot destroy the fluid boundary layer at the wall of the wastewater storage tank during the rotation process, resulting in low heat exchange efficiency between the stripping liquid wastewater inside the wastewater storage tank and the external heating water, and the dehydration process is time-consuming.
  • the present invention provides a stripping liquid recovery and dehydration device, which solves the problem that when the stripping liquid inside the wastewater storage tank is dehydrated by the existing water bath heating method, the heat exchange efficiency between the stripping liquid wastewater inside the wastewater storage tank and the external heating water is low, and the dehydration process is time-consuming.
  • a stripping liquid recovery and dehydration device comprising a dehydration tower and a wastewater storage tank arranged inside the dehydration tower, the upper part of the dehydration tower is provided with a heating water inlet, which is used to add hot water into the dehydration tower so that it can perform water bath heating on the wastewater storage tank, a central stirring component is provided in the center of the wastewater storage tank, a side stirring component is provided in the wastewater storage tank near the inner wall, a driving component is provided inside the dehydration tower, the driving component is used to drive the central stirring component and the side stirring component to rotate, a resistance sensing component is provided on the upper part of the central stirring component, the resistance sensing component is used to adjust the stirring depth of the central stirring component according to the liquid level height inside the wastewater storage tank, an adjusting sleeve component is provided outside the side stirring component, the rotation angle of the adjusting sleeve component is controlled by the resistance sensing component, and the adjusting s
  • the central stirring assembly includes a stirring rod and stirring blades, and the stirring blades are arranged in multiple groups at intervals along the axial direction of the stirring rod, and each group includes more than two stirring blades arranged at intervals around the circumference of the stirring rod.
  • the side stirring assembly includes a dragon shaft and a planetary shaft, and the dragon shaft is fixed at the lower end of the planetary shaft.
  • the drive assembly includes a motor, a planetary carrier, four planetary gears, a ring gear, a sun gear and a center shaft, the planetary carrier is fixedly connected to the output shaft of the motor, the center shaft is fixedly connected to the sun gear, the sun gear is respectively meshed with the four planetary gears, and the four planetary gears are also meshed with the ring gear.
  • the resistance sensing assembly includes a central spiral tube, a compression spring and a central guide column
  • the stirring rod is movably installed inside the central spiral tube
  • one end of the compression spring is fixedly connected to the central spiral tube
  • the other end of the compression spring is fixedly connected to the upper end of the stirring rod
  • the central guide column is fixedly installed on the outside of the stirring rod
  • a central spiral groove is provided on the outside of the central spiral tube
  • the central guide column is slidably fitted inside the central spiral groove.
  • the resistance sensing component also includes a movable ring, a limiting ring and a movable frame, the limiting ring is fixed on the outer circumferential surface of the stirring rod, the outer circumferential surface of the stirring rod is slidably provided with a movable ring above the limiting ring, and the outer circumferential surface of the movable ring is fixed with four movable frames in a circular arrangement.
  • the adjustment sleeve assembly includes a planetary spiral tube, a planetary guide pin, a planetary spiral groove and an adjustment sleeve, the planetary guide pin is slidably fitted in the planetary spiral groove, the planetary spiral groove is opened on the outer circumferential surface of the planetary spiral tube, the adjustment sleeve is fixedly arranged at the lower part of the planetary spiral tube, and the upper end of the adjustment sleeve has a discharge port for discharging the wastewater guided upward into a wastewater storage tank.
  • one end of the adjustment sleeve has a fan-shaped port.
  • a condensate recovery port is provided at the upper right end of the wastewater storage tank, an organic solvent recovery port is provided at the bottom of the wastewater storage tank, and a wastewater inlet is provided at the upper left end of the wastewater storage tank.
  • a stepped support ring is fixedly provided at the inner upper end of the dehydration tower, and a gear ring is fixedly arranged at the upper end of the stepped support ring.
  • the present invention provides a stripping liquid recovery and dehydration device, which has the following beneficial effects:
  • the stripping liquid recovery and dehydration device improves heat exchange efficiency and accelerates evaporation and discharge of water in the wastewater by destroying the steady state of the fluid boundary layer at the inner wall of the wastewater storage tank when the wastewater volume is large and the water content of the wastewater is large.
  • the heat exchange efficiency is improved by destroying the steady state of the flow boundary layer, and the benefit of promoting water evaporation is reduced.
  • the remaining wastewater is continuously guided and lifted upward to increase the flow area of the remaining wastewater, so that the water in the remaining wastewater is caused to evaporate and form water vapor for discharge, thereby achieving the purpose of improving dehydration efficiency.
  • FIG1 is a front view schematic diagram of the present invention.
  • Fig. 2 is a schematic cross-sectional view of the present invention
  • FIG3 is an enlarged schematic diagram of a part of the structure in FIG2;
  • Figure 4 is a schematic diagram of the location of the discharge port
  • FIG5 is a schematic diagram of the opening position of the fan-shaped port
  • FIG6 is a schematic diagram of the stirring rod connection structure
  • FIG7 is a schematic diagram of the structure of a drive assembly
  • FIG8 is a schematic diagram of a first state of the adjustment sleeve
  • FIG. 9 is a schematic diagram of the second state of the adjustment sleeve.
  • a stripping liquid recovery and treatment dehydration device comprising a dehydration tower 1 and a wastewater storage tank 2 arranged inside the dehydration tower 1, wherein the upper portion of the dehydration tower 1 is provided with a heating water inlet 25 for adding hot water into the dehydration tower 1 so that the wastewater storage tank 2 is heated by a water bath;
  • a central stirring assembly is rotatably provided inside the wastewater storage tank 2, and the central stirring assembly includes a stirring rod 12 and stirring blades 24.
  • the stirring blades 24 are arranged in multiple groups along the axial direction of the stirring rod 12, and each group includes more than two stirring blades 24 arranged at intervals around the stirring rod 12 in the circumferential direction.
  • a side stirring assembly is rotatably provided near the inner wall of the wastewater storage tank 2, and the side stirring assembly includes a dragon shaft 22 and a planetary shaft 6.
  • the dragon shaft 22 is fixedly arranged at the lower end of the planetary shaft 6.
  • a driving assembly is provided inside the dehydration tower 1, and the driving assembly includes a motor 3, a planetary carrier 4, four planetary gears 5, a ring gear 7, a sun gear 8 and a central shaft 9.
  • the planetary carrier 4 is fixedly connected to the output shaft of the motor 3, the central shaft 9 is fixedly connected to the sun gear 8, the sun gear 8 is meshed with the four planetary gears 5 respectively, and the four planetary gears 5 are also meshed with the ring gear 7.
  • a stepped support ring 29 is fixedly provided at the upper end of the inner part of the dehydration tower 1, and the ring gear 7 is fixedly arranged at the upper end of the stepped support ring 29;
  • the driving assembly is used to drive the central stirring assembly and the side stirring assembly to rotate.
  • a resistance sensing assembly is provided on the upper part of the central stirring assembly.
  • the resistance sensing assembly includes a central spiral tube 10, a compression spring 11 and a central guide column 14.
  • the stirring rod 12 is movably installed inside the central spiral tube 10.
  • One end of the compression spring 11 is fixedly connected to the central spiral tube 10, and the other end of the compression spring 11 is fixedly connected to the upper end of the stirring rod 12.
  • the central guide column 14 is fixedly installed on the outside of the stirring rod 12.
  • the outside of the central spiral tube 10 is provided with a central spiral groove 13.
  • the central guide column 14 is slidably fitted inside the central spiral groove 13.
  • the vertical height of the central spiral groove 13 needs to be limited.
  • the vertical height of the central spiral groove 13 should be at least equal to the vertical distance between the two groups of stirring blades 24. The purpose is to move the central guide column 14 upward along the central spiral groove 13 to move one group of stirring blades 24 out from below the liquid surface, thereby reducing the resistance of the stirring rod 12 to drive the stirring blades 24 to rotate.
  • the vertical height of the central spiral groove 13 should be compatible with the vertical height of the planetary spiral groove 20, so that when the central guide column 14 is at the highest position in the central spiral groove 13, the planetary guide column 18 is also at the highest position of the planetary spiral groove 20, so that the adjustment sleeve 21 is rotated to the position shown in Figure 8 at this time;
  • the resistance sensing component also includes a moving ring 15, a limiting ring 16 and a moving frame 17.
  • the limiting ring 16 is fixedly arranged on the outer peripheral surface of the stirring rod 12.
  • the outer peripheral surface of the stirring rod 12 is slidably provided with a moving ring 15 located above the limiting ring 16.
  • the outer peripheral surface of the moving ring 15 is fixedly provided with four moving frames 17 in a circular arrangement.
  • the resistance sensing component is used to adjust the stirring depth of the central stirring component according to the internal liquid level height of the wastewater storage tank 2.
  • An adjustment sleeve assembly is provided on the outside of the side stirring assembly, and the adjustment sleeve assembly includes a planetary spiral tube 19, a planetary guide post 18, a planetary spiral groove 20 and an adjustment sleeve 21.
  • One end of the adjustment sleeve 21 has a fan-shaped port 30.
  • the planetary guide post 18 slides in the planetary spiral groove 20.
  • the planetary spiral groove 20 is opened on the outer circumferential surface of the planetary spiral tube 19.
  • the adjustment sleeve 21 is fixedly arranged at the lower part of the planetary spiral tube 19.
  • the upper end of the adjustment sleeve 21 has a discharge port 23 for discharging the wastewater guided upward into the wastewater storage tank 2.
  • the rotation angle of the adjustment sleeve assembly is controlled by the resistance sensing assembly.
  • the adjustment sleeve assembly is used to switch the side stirring assembly from the function of destroying the fluid boundary layer to the function of guiding the wastewater upward by changing the rotation angle.
  • a condensate recovery port 27 is provided at the upper right end of the wastewater storage tank 2
  • an organic solvent recovery port 28 is provided at the bottom of the wastewater storage tank 2
  • a wastewater inlet 26 is provided at the upper left end of the wastewater storage tank 2.
  • the electrical components mentioned in this article are all connected to an external main controller and 220V mains electricity, and the main controller can be a conventional known device for controlling a computer or the like.
  • the stripping liquid wastewater is first added into the wastewater storage tank 2 through the wastewater inlet 26, and then hot water is added into the dehydration tower 1 through the heating water inlet 25, so that the volume of the stripping liquid wastewater reaches the maximum volume, and the heating water in the dehydration tower 1 also reaches the maximum volume position, and finally the motor 3 is started;
  • the motor 3 drives the planetary carrier 4 to start rotating, so that the planetary gear 5 rotates while revolving around the center position of the planetary carrier 4, and the planetary gear 5 drives the sun gear 8 to rotate, so the sun gear 8 drives the central shaft 9 to rotate, and the planetary gear 5 drives the planetary shaft 6 to rotate. Since the volume of wastewater inside the wastewater storage tank 2 is large at this time, the rotation resistance of the stirring rod 12 is large, and the compression amount of the compression spring 11 is not enough to drive the stirring rod 12 to rotate with the central spiral tube 10. At this time, the central guide column 14 connected to the upper end of the stirring rod 12 moves upward along the central spiral groove 13 to the highest position.
  • the compression amount of the compression spring 11 reaches the maximum, and at the same time, the uppermost group of stirring blades 24 move out from under the liquid surface.
  • the rotation resistance of the stirring rod 12 is reduced.
  • the stirring rod 12 rotates synchronously with the central spiral tube 10, and the stirring rod 12 drives multiple groups of stirring blades 24 to rotate to stir the wastewater inside the wastewater storage tank 2, so as to accelerate the evaporation and discharge of water in the wastewater inside the wastewater storage tank 2;
  • the stirring rod 12 moves upward to drive the moving ring 15 to move upward, and the moving frame 17 moves upward synchronously, so that the planetary guide column 18 moves upward along the planetary spiral tube 19, so that the planetary spiral tube 19 drives the adjustment sleeve 21 to rotate to the position of Figure 8.
  • the dragon shaft 22 rotates counterclockwise to generate a vortex at the fan-shaped port 30, so that the steady state of the fluid boundary layer at the inner wall of the wastewater storage tank 2 is destroyed.
  • the volume of wastewater in the wastewater storage tank 2 decreases.
  • the compression amount of the compression spring 11 gradually decreases, and the stirring rod 12 gradually moves downward.
  • the adjustment sleeve 21 deflects, the effect of destroying the fluid boundary layer gradually decreases, and the height to which the wastewater can be lifted by the dragon shaft 22 increases.
  • the fan-shaped port 30 is facing the inner wall of the wastewater storage tank 2, which is equivalent to being spliced with the inner wall of the wastewater storage tank 2 to form a closed chamber, so that the remaining wastewater is guided and lifted upward under the action of the dragon shaft 22, and is discharged downward from the discharge port 23 after being lifted to the highest position, which increases the flow area of the remaining wastewater and causes the water in the remaining wastewater to evaporate into water vapor and be discharged, thereby achieving the purpose of improving the dehydration efficiency;
  • the water content of the wastewater is large.
  • the steady state of the fluid boundary layer at the inner wall of the wastewater storage tank 2 is destroyed to improve the heat exchange efficiency and accelerate the evaporation and discharge of water in the wastewater.
  • the water content in the wastewater is reduced.
  • the benefit of promoting water evaporation by destroying the steady state of the flow boundary layer to improve the heat exchange efficiency is reduced.
  • the remaining wastewater is continuously guided and lifted upward to increase the flow area of the remaining wastewater, which causes the water in the remaining wastewater to evaporate and form water vapor for discharge, thereby achieving the purpose of improving the dehydration efficiency.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Physical Water Treatments (AREA)

Abstract

本发明公开了一种剥离液回收处理脱水装置，涉及废水处理技术领域，具体为一种剥离液回收处理脱水装置，包括脱水塔和设置在脱水塔内部的废水储罐，脱水塔的上部具有加热水进水口，用于将热水加入到脱水塔内部使其对废水储罐进行水浴加热。该剥离液回收处理脱水装置，在废水体积量较大时，通过破坏废水储罐内壁处的流体边界层的稳态，以提高换热效率，加速废水中的水分蒸发排出，在废水体积量减小后，通过破坏流动边界层的稳态来提高换热效率促进水蒸发的收益降低，此时通过将剩余废水不断向上引导提升，以增加剩余废水的流动面积，促使剩余废水中的水蒸发形成水蒸气排出，达到提高脱水效率的目的。

Description

一种剥离液回收处理脱水装置 技术领域
本发明涉及废水处理技术领域，具体为一种剥离液回收处理脱水装置。
背景技术
光阻剥离液是芯片封装工艺中使用的一种清洗药剂，其用途是将封装芯片产品正负极上的光刻胶移除，因此又称为光刻胶剥离液。其主要成分是有机氨和极性有机溶剂，此外还含有以水为主要代表的轻组分。剥离液在使用后，除含有少量的光刻胶颗粒外，其主要成分仍为有机氨和极性有机溶剂，因此可以对使用后的剥离液进行回收脱水，然后通过分类提纯，以使其具备再利用的价值。
在对剥离液进行回收脱水时，现有技术手段有通过电热丝对废水储罐中的剥离液废水进行加热，也有通过冷却塔以水浴加热的形式对剥离液废水进行脱水。相比较之下，通过冷却塔以水浴方式进行加热的脱水方式加热均匀性和安全性更好，但其仍存在以下问题需要解决：中心的搅动叶片在转动过程无法对废水储罐罐壁处的流体边界层形成破坏，从而导致废水储罐内部的剥离液废水和外部的加热水之间的换热效率低，脱水流程耗时长。
发明内容
针对现有技术的不足，本发明提供了一种剥离液回收处理脱水装置，解决了现有的水浴加热形式对废水储罐内部的剥离液进行脱水时，废水储罐内部的剥离液废水和外部的加热水之间的换热效率低，脱水流程耗时长的问题。
本发明技术方案如下：
为实现以上目的，本发明通过以下技术方案予以实现：一种剥离液回收处理脱水装置，包括脱水塔和设置在脱水塔内部的废水储罐，脱水塔的上部具有加热水进水口，用于将热水加入到脱水塔内部使其对废水储罐进行水浴加热，所述废水储罐中心转动设有中心搅动组件，所述废水储罐中靠近内壁位置处转动设有侧搅动组件，所述脱水塔的内部设有驱动组件，驱动组件用于驱动中心搅动组件和侧搅动组件转动，中心搅动组件的上部设有阻力感应组件，阻力感应组件用于根据废水储罐内部液位高度调节中心搅动组件的搅动深度，所述侧搅动组件的外部设有调整套管组件，所述调整套管组件的转动角度由阻力感应组件控制，调整套管组件用于通过转动角度的改变使得侧搅动组件从破坏流体边界层的功能切换为将废水向上引导的功能。
可选的，所述中心搅动组件包括搅动杆和搅动叶片，搅动叶片沿搅动杆的轴向间隔设置多组，每组包括两个以上绕搅动杆周向间隔设置的搅拌叶片。
可选的，所述侧搅动组件包括蛟龙轴和行星轴,蛟龙轴固定设于行星轴的下端。
可选的，所述驱动组件包括电机、行星架、四个行星轮、齿圈、太阳轮和中心轴,行星架与电机的输出轴固定连接，中心轴与太阳轮固定连接，所述太阳轮与四个行星轮分别啮合，四个行星轮还与齿圈啮合。
可选的，所述阻力感应组件包括中心螺旋管、压簧和中心导柱，所述搅动杆活动安装在中心螺旋管内部，压簧的一端固定连接与中心螺旋管固定连接，所述压簧的另一端与搅动杆的上端固定连接，所述中心导柱固定安装在搅动杆的外部，所述中心螺旋管的外部开设有中心螺旋槽,所述中心导柱滑动配合在中心螺旋槽内部。
可选的，所述阻力感应组件还包括移动环、限位环和移动架，所述限位环固定设于搅动杆的外周面上，所述搅动杆的外周面且位于限位环的上方可滑动的设有移动环，所述移动环的外周面以圆周排列的形式固定设有四个移动架。
可选的，所述调整套管组件包括行星螺旋管、行星导柱、行星螺旋槽和调整套管，所述行星导柱滑动配合在行星螺旋槽中，所述行星螺旋槽开设在行星螺旋管的外周面上，所述调整套管固定设于行星螺旋管的下部，所述调整套管的上端具有出料口，用于将向上引导的废水排出到废水储罐中。
可选的，所述调整套管的一端具有扇形端口。
可选的，所述废水储罐的上部右端设有冷凝水回收口，所述废水储罐的底部设有有机溶剂回收口，所述废水储罐的上部左端设有废水进水口。
可选的，所述脱水塔的内部上端固定设有阶梯状支撑环,齿圈固定设置在阶梯状支撑环上端。
有益效果
本发明提供了一种剥离液回收处理脱水装置，具备以下有益效果：
该剥离液回收处理脱水装置，在废水体积量较大时，此时废水的含水量大，通过破坏废水储罐内壁处的流体边界层的稳态，以提高换热效率，加速废水中的水分蒸发排出，在废水体积量减小后，此时废水中的含水量减小，通过破坏流动边界层的稳态来提高换热效率促进水蒸发的收益降低，此时通过将剩余废水不断向上引导提升，以增加剩余废水的流动面积， 促使剩余废水中的水蒸发形成水蒸气排出，达到提高脱水效率的目的。
附图说明
图1为本发明前视示意图；
图2为本发明剖视示意图；
图3为图2中部分结构放大示意图；
图4为出料口开设位置示意图；
图5为扇形端口开设位置示意图；
图6为搅动杆连接结构示意图；
图7为驱动组件结构示意图；
图8为调整套管第一状态示意图；
图9为调整套管第二状态示意图。
图中：1、脱水塔；2、废水储罐；3、电机；4、行星架；5、行星轮；6、行星轴；7、齿圈；8、太阳轮；9、中心轴；10、中心螺旋管；11、压簧；12、搅动杆；13、中心螺旋槽；14、中心导柱；15、移动环；16、限位环；17、移动架；18、行星导柱；19、行星螺旋管；20、行星螺旋槽；21、调整套管；22、蛟龙轴；23、出料口；24、搅动叶片；25、加热水进水口；26、废水进水口；27、冷凝水回收口；28、有机溶剂回收口；29、阶梯状支撑环；30、扇形端口。
具体实施方式
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。
请参阅图1至图9，本发明提供一种技术方案：一种剥离液回收处理脱水装置，包括脱水塔1和设置在脱水塔1内部的废水储罐2，脱水塔1的上部具有加热水进水口25，用于将热水加入到脱水塔1内部使其对废水储罐2进行水浴加热；
废水储罐2的内部转动设有中心搅动组件，中心搅动组件包括搅动杆12和搅动叶片24，搅动叶片24沿搅动杆12的轴向间隔设置多组，每组包括两个以上绕搅动杆12周向间隔设置的搅拌叶片24；
废水储罐2中靠近内壁位置处转动设有侧搅动组件，侧搅动组件包括蛟龙轴22和行星轴6,蛟龙轴22固定设于行星轴6的下端，脱水塔1的内部设有驱动组件，驱动组件包括电机3、 行星架4、四个行星轮5、齿圈7、太阳轮8和中心轴9,行星架4与电机3的输出轴固定连接，中心轴9与太阳轮8固定连接，太阳轮8与四个行星轮5分别啮合，四个行星轮5还与齿圈7啮合，脱水塔1的内部上端固定设有阶梯状支撑环29,齿圈7固定设置在阶梯状支撑环29上端；
驱动组件用于驱动中心搅动组件和侧搅动组件转动，中心搅动组件的上部设有阻力感应组件，阻力感应组件包括中心螺旋管10、压簧11和中心导柱14，搅动杆12活动安装在中心螺旋管10内部，压簧11的一端固定连接与中心螺旋管10固定连接，压簧11的另一端与搅动杆12的上端固定连接；
对于压簧11要进行说明的是，在废水储罐2内部的剩余废水体积减小至废水储罐2容积的二分之一时，压簧11此时的压缩弹力应足以驱动中心导柱14处于中心螺旋槽13的最低位置时，搅动杆12跟随中心螺旋管10进行转动；
中心导柱14固定安装在搅动杆12的外部，中心螺旋管10的外部开设有中心螺旋槽13,中心导柱14滑动配合在中心螺旋槽13内部，对于中心螺旋槽13需进行垂直高度要限定的是，中心螺旋槽13的垂直高度应至少等于两组的搅动叶片24之间的垂直距离，目的在于通过中心导柱14沿中心螺旋槽13向上运动来使得一组的搅动叶片24从液面下方移出，减小搅动杆12驱动搅动叶片24转动的阻力，同时中心螺旋槽13的垂直高度应和行星螺旋槽20的垂直高度相适配，以使得在中心导柱14处于中心螺旋槽13中最高位置时，行星导柱18也处于行星螺旋槽20的最高位置，从而使得此时调整套管21转动至图8位置；
阻力感应组件还包括移动环15、限位环16和移动架17，限位环16固定设于搅动杆12的外周面上，搅动杆12的外周面且位于限位环16的上方可滑动的设有移动环15，移动环15的外周面以圆周排列的形式固定设有四个移动架17，阻力感应组件用于根据废水储罐2内部液位高度调节中心搅动组件的搅动深度；
侧搅动组件的外部设有调整套管组件，调整套管组件包括行星螺旋管19、行星导柱18、行星螺旋槽20和调整套管21，调整套管21的一端具有扇形端口30，行星导柱18滑动配合在行星螺旋槽20中，行星螺旋槽20开设在行星螺旋管19的外周面上，调整套管21固定设于行星螺旋管19的下部，调整套管21的上端具有出料口23，用于将向上引导的废水排出到废水储罐2中，调整套管组件的转动角度由阻力感应组件控制，调整套管组件用于通过转动角度的改变使得侧搅动组件从破坏流体边界层的功能切换为将废水向上引导的功能。
作为本发明的一种优选技术方案：废水储罐2的上部右端设有冷凝水回收口27，废水储罐2的底部设有有机溶剂回收口28，废水储罐2的上部左端设有废水进水口26。
该文中出现的电器元件均与外界的主控器及220V市电电连接，并且主控器可为计算机等起到控制的常规已知设备。
该剥离液回收处理脱水装置，使用时，先将剥离液废水通过废水进水口26加入到废水储罐2内部，后将热水通过加热水进水口25加入到脱水塔1内部，使得剥离液废水的体积达到最大容积，脱水塔1中的加热水也达到最大容积位置，最后启动电机3；
电机3带动行星架4开始转动，从而行星轮5自转的同时绕着行星架4的中心位置公转，行星轮5带动太阳轮8转动，于是太阳轮8带动中心轴9转动，行星轮5带动行星轴6转动，由于此时废水储罐2内部的废水体积量大，因此搅动杆12的转动阻力大，压簧11的压缩量不足以驱动搅动杆12跟随中心螺旋管10转动，此时连接在搅动杆12上端的中心导柱14沿着中心螺旋槽13向上移动到最高位置，此时压簧11的被压缩量达到最大，同时最上端的一组搅动叶片24从液面下移出，此时搅动杆12的转动阻力减小，此时搅动杆12跟随中心螺旋管10同步转动，搅动杆12带动多组的搅动叶片24转动对废水储罐2内部的废水进行搅动，以加速废水储罐2内部的废水中的水蒸发排出；
同时搅动杆12向上移动带动移动环15跟随向上移动，移动架17同步向上移动，从而行星导柱18沿着行星螺旋管19向上移动，以使得行星螺旋管19带动调整套管21转动至图8位置，此时在行星轴6的转动作用下，蛟龙轴22逆时针转动，以在扇形端口30处产生涡旋，从而使得在废水储罐2内壁位置处的流体边界层的稳态被破坏，同时由于行星轴6跟随行星架4逆时针转动，从而相当于废水绕流调整套管21，从而在调整套管21的后方周期性的脱落出旋转方向相反，排列规则的双列线涡，经线性作用后形成卡门涡街，进一步的破坏废水储罐2内壁位置处的流体边界层的稳态，以使得废水储罐2内部的废水和脱水塔1内部的热水之间的换热效率更高，在废水含水量高的时候加速废水中的水蒸气排出，缩短脱水耗时；
随着废水脱水量的增加，废水储罐2中的废水体积量减小，在此过程中，压簧11的被压缩量逐渐减小，搅动杆12逐渐的向下运动，在此过程中，随着调整套管21的偏转，对流体边界层破坏的效应逐渐减小，废水可被蛟龙轴22提升的高度增加，从而在调整套管21逐渐转动至图9所示的位置时，此时扇形端口30朝向废水储罐2内壁位置，相当于和废水储罐2内壁拼接形成闭合的腔室，从而剩余的废水在蛟龙轴22的作用下被向上引导提升，提升至最 高位置后从出料口23向下排出，增加了剩余废水的流动面积，促使剩余废水中的水蒸发成水蒸气排出，达到提高脱水效率的目的；
综上，在废水体积量较大时，此时废水的含水量大，在废水量减少至废水储罐2容积的二分之一之前，通过破坏废水储罐2内壁处的流体边界层的稳态，以提高换热效率，加速废水中的水分蒸发排出，在废水体积量减小后，此时废水中的含水量减小，在废水量减小至废水储罐2容积的二分之一之后，通过破坏流动边界层的稳态来提高换热效率促进水蒸发的收益降低，此时通过将剩余废水不断向上引导提升，以增加剩余废水的流动面积，促使剩余废水中的水蒸发形成水蒸气排出，达到提高脱水效率的目的。
以上所述，仅为本发明较佳的具体实施方式，但本发明的保护范围并不局限于此，任何熟悉本技术领域的技术人员在本发明揭露的技术范围内，根据本发明的技术方案及其发明构思加以等同替换或改变，都应涵盖在本发明的保护范围之内。

Claims (10)

  1. 一种剥离液回收处理脱水装置，包括脱水塔(1)和设置在脱水塔(1)内部的废水储罐(2)，脱水塔(1)的上部具有加热水进水口(25)，用于将热水加入到脱水塔(1)内部使其对废水储罐(2)进行水浴加热，其特征在于：所述废水储罐(2)中心转动设有中心搅动组件，所述废水储罐(2)中靠近内壁位置处转动设有侧搅动组件，所述脱水塔(1)的内部设有驱动组件，驱动组件用于驱动中心搅动组件和侧搅动组件转动，中心搅动组件的上部设有阻力感应组件，阻力感应组件用于根据废水储罐(2)内部液位高度调节中心搅动组件的搅动深度，所述侧搅动组件的外部设有调整套管组件，所述调整套管组件的转动角度由阻力感应组件控制，调整套管组件用于通过转动角度的改变使得侧搅动组件从破坏流体边界层的功能切换为将废水向上引导的功能。
  2. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述中心搅动组件包括搅动杆(12)和搅动叶片(24)，搅动叶片(24)沿搅动杆(12)的轴向间隔设置多组，每组包括两个以上绕搅动杆(12)周向间隔设置的搅拌叶片(24)。
  3. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述侧搅动组件包括蛟龙轴(22)和行星轴(6),蛟龙轴(22)固定设于行星轴(6)的下端。
  4. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述驱动组件包括电机(3)、行星架(4)、四个行星轮(5)、齿圈(7)、太阳轮(8)和中心轴(9),行星架(4)与电机(3)的输出轴固定连接，中心轴(9)与太阳轮(8)固定连接，所述太阳轮(8)与四个行星轮(5)分别啮合，四个行星轮(5)还与齿圈(7)啮合。
  5. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述阻力感应组件包括中心螺旋管(10)、压簧(11)和中心导柱(14)，所述搅动杆(12)活动安装在中心螺旋管(10)内部，压簧(11)的一端固定连接与中心螺旋管(10)固定连接，所述压簧(11)的另一端与搅动杆(12)的上端固定连接，所述中心导柱(14)固定安装在搅动杆(12)的外部，所述中心螺旋管(10)的外部开设有中心螺旋槽(13),所述中心导柱(14)滑动配合在中心螺旋槽(13)内部。
  6. 根据权利要求5所述的一种剥离液回收处理脱水装置，其特征在于：所述阻力感 应组件还包括移动环(15)、限位环(16)和移动架(17)，所述限位环(16)固定设于搅动杆(12)的外周面上，所述搅动杆(12)的外周面且位于限位环(16)的上方可滑动的设有移动环(15)，所述移动环(15)的外周面以圆周排列的形式固定设有四个移动架(17)。
  7. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述调整套管组件包括行星螺旋管(19)、行星导柱(18)、行星螺旋槽(20)和调整套管(21)，所述行星导柱(18)滑动配合在行星螺旋槽(20)中，所述行星螺旋槽(20)开设在行星螺旋管(19)的外周面上，所述调整套管(21)固定设于行星螺旋管(19)的下部，所述调整套管(21)的上端具有出料口(23)，用于将向上引导的废水排出到废水储罐(2)中。
  8. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述调整套管(21)的一端具有扇形端口(30)。
  9. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述废水储罐(2)的上部右端设有冷凝水回收口(27)，所述废水储罐(2)的底部设有有机溶剂回收口(28)，所述废水储罐(2)的上部左端设有废水进水口(26)。
  10. 根据权利要求1所述的一种剥离液回收处理脱水装置，其特征在于：所述脱水塔(1)的内部上端固定设有阶梯状支撑环(29),齿圈(7)固定设置在阶梯状支撑环(29)上端。
PCT/CN2022/140378 2022-10-26 2022-12-20 一种剥离液回收处理脱水装置 WO2024087360A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202211314795.4A CN115367827A (zh) 2022-10-26 2022-10-26 一种剥离液回收处理脱水装置
CN202211314795.4 2022-10-26

Publications (1)

Publication Number Publication Date
WO2024087360A1 true WO2024087360A1 (zh) 2024-05-02

Family

ID=84074208

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2022/140378 WO2024087360A1 (zh) 2022-10-26 2022-12-20 一种剥离液回收处理脱水装置

Country Status (2)

Country Link
CN (1) CN115367827A (zh)
WO (1) WO2024087360A1 (zh)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115367827A (zh) * 2022-10-26 2022-11-22 联仕(昆山)化学材料有限公司 一种剥离液回收处理脱水装置
CN116576701B (zh) * 2023-07-14 2023-09-22 德阳劲达节能科技有限责任公司 一种高温废水的余热回收装置
CN117486294B (zh) * 2023-12-15 2024-04-09 江苏坤洋翰光能源技术集团有限公司 一种工业危废水处理系统及其处理方法

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100307984A1 (en) * 2009-06-08 2010-12-09 James Mortensen Immediate cleaning and recirculation of cleaning fluid and method of using same
CN108837546A (zh) * 2018-05-29 2018-11-20 四川久远化工技术有限公司 一种剥离液再生工艺段的水分去除方法
CN109734634A (zh) * 2019-02-21 2019-05-10 苏州晶洲装备科技有限公司 一种光阻剥离液废液回收配液装置
CN209113523U (zh) * 2018-11-20 2019-07-16 武汉欣朗科技有限公司 一种新型废水蒸馏釜
CN115367827A (zh) * 2022-10-26 2022-11-22 联仕(昆山)化学材料有限公司 一种剥离液回收处理脱水装置

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114100540A (zh) * 2021-11-04 2022-03-01 高翌乔 一种适用于液相化学反应的盘管式反应器

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100307984A1 (en) * 2009-06-08 2010-12-09 James Mortensen Immediate cleaning and recirculation of cleaning fluid and method of using same
CN108837546A (zh) * 2018-05-29 2018-11-20 四川久远化工技术有限公司 一种剥离液再生工艺段的水分去除方法
CN209113523U (zh) * 2018-11-20 2019-07-16 武汉欣朗科技有限公司 一种新型废水蒸馏釜
CN109734634A (zh) * 2019-02-21 2019-05-10 苏州晶洲装备科技有限公司 一种光阻剥离液废液回收配液装置
CN115367827A (zh) * 2022-10-26 2022-11-22 联仕(昆山)化学材料有限公司 一种剥离液回收处理脱水装置

Also Published As

Publication number Publication date
CN115367827A (zh) 2022-11-22

Similar Documents

Publication Publication Date Title
WO2024087360A1 (zh) 一种剥离液回收处理脱水装置
WO2020228551A1 (zh) 一种高效蒸发结晶装置
CN208817958U (zh) 一种用于香料加工的脱水烘干装置
CN110762974B (zh) 一种用于纺织加工的布料烘干装置
CN108592582B (zh) 一种摆转结合的铜箔快速烘干装置
CN213090333U (zh) 一种膨润土除湿干燥装置
CN210519993U (zh) 一种九体茶匹配生产装置
CN207253779U (zh) 高效旋叶式蒸发器
CN206009021U (zh) 一种具有烘干装置的高效的化工离心设备
CN205878776U (zh) 一种新型安瓶甩水机
CN208711055U (zh) 一种基于mvr技术的晶体浓缩析出装置
CN108434772A (zh) 一种新型蒸馏炉装置
CN207751240U (zh) 一种茶籽烘干机
CN112695141B (zh) 一种钢铁冶炼热渣节能处理装置
CN219398997U (zh) 降低耗能的碳酸丙烯酯精馏分离装置
CN209188153U (zh) 一种用于调料生产的蒸馏浓缩设备
CN214634126U (zh) 一种柠檬酸三乙酯生产中乙醇回收装置
CN219076350U (zh) 一种注塑供料干燥装置
CN216170131U (zh) 液硫脱气处理装置
CN221172597U (zh) 一种建筑防水材料生产用流体加热装置
CN214861203U (zh) 一种新型阿胶浆提取液浓缩装置
CN213687652U (zh) 一种用于带有机溶剂物料的专用烘干机
CN215995622U (zh) 一种用于中药加工的单效浓缩装置
CN219501588U (zh) 一种乳液预热式杀菌釜
CN209652643U (zh) 一种水力碎浆机

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 22963338

Country of ref document: EP

Kind code of ref document: A1