WO2022142183A1 - 一种模拟气象环境的蒸发浓缩设备 - Google Patents

一种模拟气象环境的蒸发浓缩设备 Download PDF

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Publication number
WO2022142183A1
WO2022142183A1 PCT/CN2021/101476 CN2021101476W WO2022142183A1 WO 2022142183 A1 WO2022142183 A1 WO 2022142183A1 CN 2021101476 W CN2021101476 W CN 2021101476W WO 2022142183 A1 WO2022142183 A1 WO 2022142183A1
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WIPO (PCT)
Prior art keywords
evaporation
waste water
liquid discharge
simulating
meteorological environment
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PCT/CN2021/101476
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English (en)
French (fr)
Inventor
曾四鸣
高燕宁
刘克成
张立军
韩鹤松
Original Assignee
国网河北省电力有限公司电力科学研究院
国家电网有限公司
国网河北能源技术服务有限公司
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Publication of WO2022142183A1 publication Critical patent/WO2022142183A1/zh

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/048Purification of waste water by evaporation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/043Details
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/10Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
    • C02F1/12Spray evaporation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus

Definitions

  • the invention relates to the technical field of wastewater treatment, in particular to an evaporation and concentration device for simulating a meteorological environment.
  • Wastewater treatment is to use physical, chemical and biological methods to treat wastewater to purify wastewater and reduce pollution, so as to achieve wastewater recycling and reuse, and make full use of water resources.
  • Evaporation equipment is also called evaporator. It is a device that concentrates a solution or separates crystals from a solution by heating. It is mainly composed of heating chamber and evaporation chamber.
  • the heating chamber is the part that heats the solution with steam and makes it boil, but some devices have additional boiling chambers.
  • the evaporation chamber also known as the separation chamber, is the part that separates the gas and liquid.
  • the steam produced by boiling in the heating chamber (or boiling chamber) has a large amount of liquid foam, and in the separation chamber with a large space, the liquid foam can be separated from the steam due to self-condensation or the action of the indoor foam trap.
  • the steam is usually pumped by a vacuum pump to the condenser for condensation, and the condensate is discharged from the bottom of the condenser.
  • the purpose of the present invention is to provide an evaporation and concentration device that simulates a meteorological environment, so as to solve the problems raised in the above-mentioned background art.
  • the present invention provides the following technical solutions:
  • An evaporative concentration device simulating a meteorological environment including an evaporative concentrator; a baffle plate is vertically installed inside the evaporative concentrator, and the baffle plate divides the inside of the evaporative concentrator into a waste water pool and a condensed water pool, and the waste water pool and the condensed water pool The upper parts are communicated with each other through the steam channel; the evaporation concentrator is located at the upper part of the waste water tank and is connected with a drain pipe;
  • a circulating pump is included, the liquid inlet end of the circulating pump is connected with a waste liquid discharge pipe, a concentrated liquid discharge port is opened at the bottom of the waste water pool, and the concentrated liquid discharge port is communicated with the waste liquid discharge pipe, so The liquid discharge end of the circulating pump is communicated with the liquid discharge pipe through a connecting pipe.
  • it also includes a liquid inlet pipe and a filter, the liquid inlet pipe is communicated with the filter, and the filter is communicated with the connecting pipe.
  • the spray mechanism includes a turntable that is rotatably installed at the liquid discharge end of the drain pipe, the bottom of the turntable is evenly provided with a number of spray heads, the center of the turntable is provided with a liquid inlet, and the liquid inlet is connected to the drain pipe.
  • the liquid inlet is also communicated with the nozzle through several infusion pipes.
  • a plurality of through holes are evenly opened on the turntable.
  • the upper part of the baffle plate is rotatably installed with a deflector through a bracket, and the deflector includes a rotating shaft rotatably mounted on the bracket and a plurality of deflectors fixed on the shaft side of the rotating shaft.
  • it also includes a cooling water discharge port opened at the bottom of the condensing water pool and an exhaust gas processor communicated with the evaporative concentrator.
  • the exhaust gas processor includes a cylinder body communicated with the evaporative concentrator, and a coarse filter screen, a fine filter screen and an activated carbon layer are sequentially installed in the cylinder body along the flow direction of the exhaust gas.
  • the side of the baffle facing the condensing water pool is rotated and installed with several mixers from top to bottom in sequence, and the mixer includes a rotating shaft that is rotatably installed on the baffle and a screw that is fixedly installed on the rotating shaft. leaf.
  • a first gear is fixedly installed on the connecting end of the rotating shaft and the baffle plate, two adjacent first gears are connected by a second gear, and a deceleration motor is also fixedly installed on the baffle plate , a third gear is fixedly installed at the output end of the reduction motor, and the third gear meshes with the first gear.
  • the beneficial effects of the present invention are as follows: the present invention is provided with a baffle plate vertically inside the evaporative concentrator, and the baffle plate divides the interior of the evaporative concentrator into a waste water pool and a condensed water pool.
  • the upper part is connected with each other through the steam channel, and the heated waste water is fed into the spray mechanism by the drain pipe, and the waste water is sprayed into the waste water pool through the spray mechanism.
  • the waste liquid flows into the bottom of the waste water pool, and the water vapor is condensed to form a water flow accumulation and the bottom of the condensation pool, so as to simulate the meteorological environment of water evaporation and rainfall in a closed environment, and perform evaporation and concentration treatment on the waste water.
  • FIG. 1 is a schematic structural diagram of Embodiment 1 of an evaporative concentration device simulating a meteorological environment.
  • FIG. 2 is a schematic structural diagram of a spray mechanism in an evaporative concentration device simulating a meteorological environment.
  • FIG. 3 is a schematic structural diagram of Embodiment 2 of the evaporation and concentration equipment for simulating the meteorological environment.
  • FIG. 4 is a schematic structural diagram of an exhaust gas processor in Embodiment 3 of an evaporation and concentration apparatus simulating a meteorological environment.
  • an evaporative concentrating device simulating a meteorological environment includes an evaporative concentrator 4; a baffle 13 is vertically installed inside the evaporative concentrator 4, and the baffle 13 condenses the evaporation
  • the interior of the device 4 is divided into a waste water pool and a condensed water pool, and the upper part of the waste water pool and the condensed water pool is communicated with each other through the steam passage; the evaporative concentrator 4 is located in the upper part of the waste water pool and is connected with a drain pipe 5, and the evaporation concentrator 4 is located in the waste water pool.
  • a spray mechanism 6 is installed on the upper part of the hood, and the spray mechanism 6 is communicated with the drain pipe 5, and the heated waste water is fed into the spray mechanism 6 from the drain pipe 5, and the waste water is sprayed into the wastewater pool through the spray mechanism 6.
  • the water vapor flows upwards and enters the condensing water pool through the steam channel, the waste liquid flows into the bottom of the waste water pool, and the water vapor condenses and gathers into the water flow and the bottom of the condensing water pool.
  • a circulating pump 19 is also included.
  • the liquid inlet end of the circulating pump 19 is connected with a waste liquid discharge pipe 18.
  • a concentrated liquid discharge port 17 is opened at the bottom of the waste water tank.
  • the concentrated liquid discharge port 17 is connected to the waste liquid.
  • the liquid discharge pipe 18 communicates with each other.
  • the liquid discharge end of the circulating pump 19 is communicated with the liquid discharge pipe 5 through the connecting pipe 3, and is used for circulating the waste water into the waste water tank, so that the waste water is gradually concentrated and crystallized.
  • a liquid inlet pipe 1 and a filter 2 are also included.
  • the liquid inlet pipe 1 is communicated with the filter 2, and the filter 2 is communicated with the connecting pipe 3 for filtering the waste water entering the waste water tank.
  • the spray mechanism 6 includes a turntable 21 that is rotatably installed on the liquid discharge end of the liquid discharge pipe 5, a plurality of spray heads 23 are evenly opened at the bottom of the turntable 21, and a liquid inlet 24 is opened at the center of the turntable 21.
  • the liquid inlet 24 is communicated with the liquid discharge pipe 5 , and the liquid inlet 24 is also communicated with the spray head 23 through a plurality of infusion pipes 25 for passing waste water into the spray head 23 for spraying.
  • a plurality of through holes 22 are evenly opened on the turntable 21 for the discharge and flow of water vapor, so as to prevent the spray mechanism 6 from hindering the flow of water vapor.
  • a deflector 14 is rotatably mounted on the upper part of the baffle 13 through a bracket 15 , and the deflector 14 includes a rotating shaft rotatably mounted on the bracket 15 and a plurality of The guide plate drives the rotating shaft to rotate, and the rotating shaft drives the guide plate to move to speed up the flow of water vapor, so that the water vapor quickly flows into the condensing water pool.
  • it also includes a cooling water outlet at the bottom of the condensing pool and a waste gas processor 12 communicated with the evaporative concentrator 4 for treating and discharging waste gas during the waste water evaporation process.
  • an evaporative concentrating device simulating a meteorological environment includes an evaporative concentrator 4; a baffle 13 is vertically installed inside the evaporative concentrator 4, and the baffle 13 condenses the evaporation
  • the interior of the device 4 is divided into a waste water pool and a condensed water pool, and the upper part of the waste water pool and the condensed water pool is communicated with each other through the steam passage; the evaporative concentrator 4 is located in the upper part of the waste water pool and is connected with a drain pipe 5, and the evaporation concentrator 4 is located in the waste water pool.
  • a spray mechanism 6 is installed on the upper part of the hood, and the spray mechanism 6 is communicated with the drain pipe 5, and the heated waste water is fed into the spray mechanism 6 from the drain pipe 5, and the waste water is sprayed into the wastewater pool through the spray mechanism 6.
  • the water vapor flows upwards and enters the condensing water pool through the steam channel, the waste liquid flows into the bottom of the waste water pool, and the water vapor condenses and gathers into the water flow and the bottom of the condensing water pool.
  • a circulating pump 19 is also included.
  • the liquid inlet end of the circulating pump 19 is connected with a waste liquid discharge pipe 18.
  • a concentrated liquid discharge port 17 is opened at the bottom of the waste water tank.
  • the concentrated liquid discharge port 17 is connected to the waste liquid.
  • the liquid discharge pipe 18 is connected, and the liquid discharge end of the circulating pump 19 is connected with the liquid discharge pipe 5 through the connecting pipe 3 for circulating the waste water into the waste water tank, so that the waste water is gradually concentrated and crystallized.
  • a liquid inlet pipe 1 and a filter 2 are also included.
  • the liquid inlet pipe 1 is communicated with the filter 2, and the filter 2 is communicated with the connecting pipe 3 for filtering the waste water entering the waste water tank.
  • the spray mechanism 6 includes a turntable 21 rotatably mounted on the liquid discharge end of the liquid discharge pipe 5, a plurality of spray heads 23 are evenly opened at the bottom of the turntable 21, and a liquid inlet 24 is opened at the center of the turntable 21,
  • the liquid inlet 24 is communicated with the liquid discharge pipe 5 , and the liquid inlet 24 is also communicated with the spray head 23 through a plurality of liquid infusion pipes 25 , so as to pass waste water into the spray head 23 for spraying.
  • a plurality of through holes 22 are evenly opened on the turntable 21 for the discharge and flow of water vapor, so as to prevent the spray mechanism 6 from hindering the flow of water vapor.
  • a deflector 14 is rotatably mounted on the upper part of the baffle 13 through a bracket 15 , and the deflector 14 includes a rotating shaft rotatably mounted on the bracket 15 and a plurality of The guide plate drives the rotating shaft to rotate, and the rotating shaft drives the guide plate to move to speed up the flow of water vapor, so that the water vapor quickly flows into the condensing water pool.
  • it also includes a cooling water outlet at the bottom of the condensing pool and a waste gas processor 12 communicated with the evaporative concentrator 4 for treating and discharging waste gas during the waste water evaporation process.
  • Embodiment 1 Please refer to FIG. 3 , the difference between this embodiment and Embodiment 1 is:
  • the side of the baffle plate 13 facing the condensing water pool is sequentially rotated and installed with a plurality of mixers 16 from top to bottom.
  • the spiral blade on the shaft drives the spiral blade to rotate through the rotating shaft, agitates the incoming high-temperature steam, rapidly reduces the temperature of the steam, and makes the steam converge into a water flow.
  • a first gear 27 is fixedly installed at the connecting end of the rotating shaft and the baffle 13, and two adjacent first gears 27 are connected by a second gear 28, and the baffle 13 is also fixedly installed with a reduction motor 29, the output end of the reduction motor 29 is fixedly installed with a third gear 30, and the third gear meshes with the first gear 27 for driving the rotation shaft to rotate.
  • an evaporative concentrator 4 that simulates a meteorological environment, including an evaporative concentrator 4; a baffle 13 is vertically installed inside the evaporative concentrator 4, and the baffle 13 concentrates the evaporation
  • the interior of the device 4 is divided into a waste water pool and a condensed water pool, and the upper part of the waste water pool and the condensed water pool is communicated with each other through the steam passage; the evaporative concentrator 4 is located in the upper part of the waste water pool and is connected with a drain pipe 5, and the evaporation concentrator 4 is located in the waste water pool.
  • a spray mechanism 6 is installed on the upper part of the hood, and the spray mechanism 6 is communicated with the drain pipe 5, and the heated waste water is fed into the spray mechanism 6 from the drain pipe 5, and the waste water is sprayed into the wastewater pool through the spray mechanism 6.
  • the water vapor flows upward and enters the condensing water pool through the steam channel, the waste liquid flows into the bottom of the waste water pool, and the water vapor condenses and gathers into the water flow and the bottom of the condensing water pool.
  • a circulating pump 19 is also included, the liquid inlet end of the circulating pump 19 is connected with a waste liquid discharge pipe 18, and a concentrated liquid discharge port 17 is opened at the bottom of the waste water tank, and the concentrated liquid discharge port 17 is connected with the waste liquid.
  • the liquid discharge pipe 18 is connected, and the liquid discharge end of the circulating pump 19 is connected with the liquid discharge pipe 5 through the connecting pipe 3 for circulating the waste water into the waste water tank, so that the waste water is gradually concentrated and crystallized.
  • a liquid inlet pipe 1 and a filter 2 are also included.
  • the liquid inlet pipe 1 is communicated with the filter 2, and the filter 2 is communicated with the connecting pipe 3 for filtering the waste water entering the waste water tank.
  • the spray mechanism 6 includes a turntable 21 rotatably installed on the liquid discharge end of the liquid discharge pipe 5, the bottom of the turntable 21 is evenly provided with a plurality of spray heads 23, and the center of the turntable 21 is provided with a liquid inlet 24,
  • the liquid inlet 24 is communicated with the liquid discharge pipe 5 , and the liquid inlet 24 is also communicated with the spray head 23 through a plurality of infusion pipes 25 for passing waste water into the spray head 23 for spraying.
  • a plurality of through holes 22 are evenly opened on the turntable 21 for the discharge and flow of water vapor, so as to prevent the spray mechanism 6 from hindering the flow of water vapor.
  • the upper part of the baffle 13 is rotatably installed with a deflector 14 through a bracket 15
  • the deflector 14 includes a rotating shaft rotatably mounted on the bracket 15 and a plurality of The guide plate drives the rotating shaft to rotate, and the rotating shaft drives the guide plate to move to speed up the flow of water vapor, so that the water vapor quickly flows into the condensing water pool.
  • it also includes a cooling water outlet at the bottom of the condensing pool and a waste gas processor 12 communicated with the evaporative concentrator 4 for treating and discharging waste gas during the waste water evaporation process.
  • the side of the baffle plate 13 facing the condensing water pool is rotated and installed with a number of mixers 16 from top to bottom.
  • the rotating shaft drives the spiral blades to rotate, agitating the incoming high-temperature steam, rapidly reducing the steam temperature, and making the steam converge into a water flow.
  • a first gear 27 is fixedly installed at the connecting end of the rotating shaft and the baffle 13, and two adjacent first gears 27 are connected by a second gear 28, and the baffle 13 is also fixedly installed with a reduction motor 29, the output end of the reduction motor 29 is fixedly installed with a third gear 30, and the third gear meshes with the first gear 27 for driving the rotation shaft to rotate.
  • the difference between this embodiment and Embodiment 1-2 is that the exhaust gas processor 12 includes a cylindrical body 31 that communicates with the evaporative concentrator 4 .
  • the filter screen 34, the fine filter screen 33 and the activated carbon layer 32 are used for layer-by-layer treatment of the exhaust gas.
  • a baffle plate is vertically installed inside the evaporative concentrator, and the baffle plate divides the inside of the evaporative concentrator into a waste water pool and a condensing water pool.
  • the heated waste water is fed into the mechanism, and the waste water is sprayed into the waste water pool through the spray mechanism.
  • the water vapor flows upward and enters the condensing water pool through the steam channel, and the waste liquid flows into the bottom of the waste water pool.
  • the water vapor condenses It converges into the bottom of the water flow accumulation and condensation pool, so as to simulate the meteorological environment of water evaporation and rainfall in a closed environment, and conduct evaporation and concentration treatment of wastewater.

Abstract

本发明公开了一种模拟气象环境的蒸发浓缩设备,包括蒸发浓缩器;所述蒸发浓缩器内部竖直安装有挡板,挡板将蒸发浓缩器的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通;所述蒸发浓缩器位于废水池的上部连通有排液管,蒸发浓缩器位于废水池的上部安装有喷淋机构,喷淋机构与排液管连通。本发明由排液管向喷淋机构中通入加热后的废水,废水经喷淋机构向废水池中喷洒,废水喷洒过程中,水蒸气向上流动并通过蒸汽通道进入冷凝水池中,废液流入废水池池底,水蒸气冷凝后汇聚成水流存积与冷凝水池底部,从而在密闭环境中模拟水蒸发和降雨的气象环境,对废水进行蒸发浓缩处理。

Description

一种模拟气象环境的蒸发浓缩设备 技术领域
本发明涉及废水处理技术领域,具体是一种模拟气象环境的蒸发浓缩设备。
背景技术
废水处理就是利用物理、化学和生物的方法对废水进行处理,使废水净化,减少污染,以至达到废水回收、复用,充分利用水资源。将废水中各污染物分离出来或将其转化成无害物质的过程。
蒸发设备又称蒸发器。是通过加热使溶液浓缩或从溶液中析出晶粒的设备。主要由加热室和蒸发室两个部分组成。加热室是用蒸汽将溶液加热并使之沸腾的部分,但有些设备则另有沸腾室。蒸发室又称分离室,是使气液分离的部分。加热室(或沸腾室)中沸腾所产生的蒸气带有大量的液沫,到了空间较大的分离室,液沫由于自身凝聚或室内的捕沫器等的作用而得以与蒸气分离。蒸气常用真空泵抽引到冷凝器进行凝缩,冷凝液由器底排出。
现有技术中的蒸发浓缩设备结构复杂,效率低下,而且工人操作麻烦,针对以上现状,迫切需要开发一种模拟气象环境的蒸发浓缩设备,以克服当前实际应用中的不足。
技术问题
本发明的目的在于提供一种模拟气象环境的蒸发浓缩设备,以解决上述背景技术中提出的问题。
技术解决方案
为实现上述目的,本发明提供如下技术方案:
一种模拟气象环境的蒸发浓缩设备,包括蒸发浓缩器;所述蒸发浓缩器内部竖直安装有挡板,挡板将蒸发浓缩器的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通;所述蒸发浓缩器位于废水池的上部连通有排液管,蒸发浓缩器位于废水池的上部安装有喷淋机构,喷淋机构与排液管连通。
作为本发明进一步的方案:包括有循环泵,循环泵的进液端连通有废液排出管,所述废水池池底开设有浓液排出口,浓液排出口与废液排出管连通,所述循环泵的排液端通过连接管与排液管连通。
作为本发明进一步的方案:还包括有进液管和过滤器,进液管与过滤器连通,过滤器与连接管连通。
作为本发明进一步的方案:所述喷淋机构包括转动安装于排液管排液端的转盘,转盘的底部均匀开设有若干喷头,转盘的圆心处开设有进液口,进液口与排液管连通,进液口还通过若干输液管与喷头连通。
作为本发明进一步的方案:所述转盘上均匀开设有若干通孔。
作为本发明进一步的方案:所述挡板的上部通过支架转动安装有导流器,导流器包括转动安装于支架的转动轴和若干固定安装于转动轴轴侧的导流板。
作为本发明进一步的方案:还包括有开设于冷凝水池底部的冷却水排出口和与蒸发浓缩器连通的废气处理器。
作为本发明进一步的方案:所述废气处理器包括与蒸发浓缩器连通的筒体,筒体内部沿废气流动方向依次安装有粗滤网、精细滤网和活性炭层。
作为本发明进一步的方案:所述挡板朝向冷凝水池的一侧自上而下依次转动安装有若干混合器,混合器包括转动安装于挡板上的旋转轴和固定安装于旋转轴上的螺旋叶。
作为本发明进一步的方案:所述旋转轴与挡板的连接端固定安装有第一齿轮,相邻两个第一齿轮之间通过第二齿轮连接,所述挡板上还固定安装有减速电机,减速电机的输出端固定安装有第三齿轮,第三齿轮与第一齿轮啮合。
有益效果
与现有技术相比,本发明的有益效果是:本发明在蒸发浓缩器内部竖直安装有挡板,挡板将蒸发浓缩器的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通,由排液管向喷淋机构中通入加热后的废水,废水经喷淋机构向废水池中喷洒,废水喷洒过程中,水蒸气向上流动并通过蒸汽通道进入冷凝水池中,废液流入废水池池底,水蒸气冷凝后汇聚成水流存积与冷凝水池底部,从而在密闭环境中模拟水蒸发和降雨的气象环境,对废水进行蒸发浓缩处理。
附图说明
图1为模拟气象环境的蒸发浓缩设备实施例1的结构示意图。
图2为模拟气象环境的蒸发浓缩设备中喷淋机构的结构示意图。
图3为模拟气象环境的蒸发浓缩设备实施例2的结构示意图。
图4为模拟气象环境的蒸发浓缩设备实施例3中废气处理器的结构示意图。
图中:1-进液管、2-过滤器、3-连接管、4-蒸发浓缩器、5-排液管、6-喷淋机构、7-从动齿轮、8-连接齿轮、9-主动齿轮、10-驱动电机、11-旋转轴、12-废气处理器、13-挡板、14-导流器、15-支架、16-冷却水排出口、17-浓液排出口、18-废液排出管、19-循环泵、20-加热器、21-转盘、22-通孔、23-喷头、24-进液口、25-输液管、26-混合器、27-第一齿轮、28-第二齿轮、29-减速电机、30-第三齿轮、31-筒体、32-活性炭层、33-精细滤网、34-粗滤网。
本发明的实施方式
下面结合具体实施方式对本专利的技术方案作进一步详细地说明。
下面详细描述本专利的实施例,所述实施例的示例在附图中示出,其中自始至终相同或类似的标号表示相同或类似的元件或具有相同或类似功能的元件。下面通过参考附图描述的实施例是示例性的,仅用于解释本专利,而不能理解为对本专利的限制。
在本专利的描述中,需要理解的是,术语“中心”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本专利和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本专利的限制。
在本专利的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“设置”应做广义理解,例如,可以是固定相连、设置,也可以是可拆卸连接、设置,或一体地连接、设置。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本专利中的具体含义。
实施例1
请参阅图1-2,本发明实施例中,一种模拟气象环境的蒸发浓缩设备,包括蒸发浓缩器4;所述蒸发浓缩器4内部竖直安装有挡板13,挡板13将蒸发浓缩器4的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通;所述蒸发浓缩器4位于废水池的上部连通有排液管5,蒸发浓缩器4位于废水池的上部安装有喷淋机构6,喷淋机构6与排液管5连通,由排液管5向喷淋机构6中通入加热后的废水,废水经喷淋机构6向废水池中喷洒,废水喷洒过程中,水蒸气向上流动并通过蒸汽通道进入冷凝水池中,废液流入废水池池底,水蒸气冷凝后汇聚成水流存积与冷凝水池底部。
在本发明实施例中,还包括有循环泵19,循环泵19的进液端连通有废液排出管18,所述废水池池底开设有浓液排出口17,浓液排出口17与废液排出管18连通。
所述循环泵19的排液端通过连接管3与排液管5连通,用于将废水循环通入废水池中,使废水逐渐浓缩结晶。
在本发明实施例中,还包括有进液管1和过滤器2,进液管1与过滤器2连通,过滤器2与连接管3连通,用于对进入废水池中的废水进行过滤。
在本发明实施例中,所述喷淋机构6包括转动安装于排液管5排液端的转盘21,转盘21的底部均匀开设有若干喷头23,转盘21的圆心处开设有进液口24,进液口24与排液管5连通,进液口24还通过若干输液管25与喷头23连通,用于将废水通入喷头23中进行喷洒。
需要说明的是,在本发明实施例中:所述转盘21上均匀开设有若干通孔22,用于供水蒸气排出流动,避免喷淋机构6阻碍水蒸气流动。
在本发明又一实施例中,所述挡板13的上部通过支架15转动安装有导流器14,导流器14包括转动安装于支架15的转动轴和若干固定安装于转动轴轴侧的导流板,驱动转动轴旋转,转动轴带动导流板运动加快水蒸气流动使水蒸气快速流入冷凝水池中。
在本发明又一实施例中,还包括有开设于冷凝水池底部的冷却水排出口和与蒸发浓缩器4连通的废气处理器12,用于将废水蒸发过程中的废气处理后排出。
实施例2
请参阅图1-2,本发明实施例中,一种模拟气象环境的蒸发浓缩设备,包括蒸发浓缩器4;所述蒸发浓缩器4内部竖直安装有挡板13,挡板13将蒸发浓缩器4的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通;所述蒸发浓缩器4位于废水池的上部连通有排液管5,蒸发浓缩器4位于废水池的上部安装有喷淋机构6,喷淋机构6与排液管5连通,由排液管5向喷淋机构6中通入加热后的废水,废水经喷淋机构6向废水池中喷洒,废水喷洒过程中,水蒸气向上流动并通过蒸汽通道进入冷凝水池中,废液流入废水池池底,水蒸气冷凝后汇聚成水流存积与冷凝水池底部。
在本发明实施例中,还包括有循环泵19,循环泵19的进液端连通有废液排出管18,所述废水池池底开设有浓液排出口17,浓液排出口17与废液排出管18连通,所述循环泵19的排液端通过连接管3与排液管5连通,用于将废水循环通入废水池中,使废水逐渐浓缩结晶。
在本发明实施例中,还包括有进液管1和过滤器2,进液管1与过滤器2连通,过滤器2与连接管3连通,用于对进入废水池中的废水进行过滤。
在本发明实施例中,所述喷淋机构6包括转动安装于排液管5排液端的转盘21,转盘21的底部均匀开设有若干喷头23,转盘21的圆心处开设有进液口24,进液口24与排液管5连通,进液口24还通过若干输液管25与喷头23连通,用于将废水通入喷头23中进行喷洒。
需要说明的是,在本发明实施例中,所述转盘21上均匀开设有若干通孔22,用于供水蒸气排出流动,避免喷淋机构6阻碍水蒸气流动。
在本发明又一实施例中,所述挡板13的上部通过支架15转动安装有导流器14,导流器14包括转动安装于支架15的转动轴和若干固定安装于转动轴轴侧的导流板,驱动转动轴旋转,转动轴带动导流板运动加快水蒸气流动使水蒸气快速流入冷凝水池中。
在本发明又一实施例中,还包括有开设于冷凝水池底部的冷却水排出口和与蒸发浓缩器4连通的废气处理器12,用于将废水蒸发过程中的废气处理后排出。
请参阅图3,本实施例与实施例1的不同之处在于:
在本发明实施例中:所述挡板13朝向冷凝水池的一侧自上而下依次转动安装有若干混合器16,混合器16包括转动安装于挡板13上的旋转轴和固定安装于旋转轴上的螺旋叶,通过旋转轴带动螺旋叶转动,对通入的高温蒸汽进行搅动,快速降低蒸汽温度,使蒸汽汇聚成水流。
进一步的,在本发明实施例中:所述旋转轴与挡板13的连接端固定安装有第一齿轮27,相邻两个第一齿轮27之间通过第二齿轮28连接,所述挡板13上还固定安装有减速电机29,减速电机29的输出端固定安装有第三齿轮30,第三齿轮与第一齿轮27啮合,用于驱动旋转轴转动。
实施例3
请参阅图1-2,本发明实施例中:一种模拟气象环境的蒸发浓缩设备,包括蒸发浓缩器4;所述蒸发浓缩器4内部竖直安装有挡板13,挡板13将蒸发浓缩器4的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通;所述蒸发浓缩器4位于废水池的上部连通有排液管5,蒸发浓缩器4位于废水池的上部安装有喷淋机构6,喷淋机构6与排液管5连通,由排液管5向喷淋机构6中通入加热后的废水,废水经喷淋机构6向废水池中喷洒,废水喷洒过程中,水蒸气向上流动并通过蒸汽通道进入冷凝水池中,废液流入废水池池底,水蒸气冷凝后汇聚成水流存积与冷凝水池底部。
在本发明实施例中:还包括有循环泵19,循环泵19的进液端连通有废液排出管18,所述废水池池底开设有浓液排出口17,浓液排出口17与废液排出管18连通,所述循环泵19的排液端通过连接管3与排液管5连通,用于将废水循环通入废水池中,使废水逐渐浓缩结晶。
在本发明实施例中,还包括有进液管1和过滤器2,进液管1与过滤器2连通,过滤器2与连接管3连通,用于对进入废水池中的废水进行过滤。
在本发明实施例中:所述喷淋机构6包括转动安装于排液管5排液端的转盘21,转盘21的底部均匀开设有若干喷头23,转盘21的圆心处开设有进液口24,进液口24与排液管5连通,进液口24还通过若干输液管25与喷头23连通,用于将废水通入喷头23中进行喷洒。
需要说明的是,在本发明实施例中:所述转盘21上均匀开设有若干通孔22,用于供水蒸气排出流动,避免喷淋机构6阻碍水蒸气流动。
在本发明又一实施例中:所述挡板13的上部通过支架15转动安装有导流器14,导流器14包括转动安装于支架15的转动轴和若干固定安装于转动轴轴侧的导流板,驱动转动轴旋转,转动轴带动导流板运动加快水蒸气流动使水蒸气快速流入冷凝水池中。
在本发明又一实施例中,还包括有开设于冷凝水池底部的冷却水排出口和与蒸发浓缩器4连通的废气处理器12,用于将废水蒸发过程中的废气处理后排出。
请参阅图3,本实施例与实施例1的不同之处在于:在本发明实施例中,
所述挡板13朝向冷凝水池的一侧自上而下依次转动安装有若干混合器16,混合器16包括转动安装于挡板13上的旋转轴和固定安装于旋转轴上的螺旋叶,通过旋转轴带动螺旋叶转动,对通入的高温蒸汽进行搅动,快速降低蒸汽温度,使蒸汽汇聚成水流。
进一步的,在本发明实施例中:所述旋转轴与挡板13的连接端固定安装有第一齿轮27,相邻两个第一齿轮27之间通过第二齿轮28连接,所述挡板13上还固定安装有减速电机29,减速电机29的输出端固定安装有第三齿轮30,第三齿轮与第一齿轮27啮合,用于驱动旋转轴转动。
请参阅图4,本实施例与实施例1-2的不同之处在于:所述废气处理器12包括与蒸发浓缩器4连通的筒体31,筒体31内部沿废气流动方向依次安装有粗滤网34、精细滤网33和活性炭层32,用于对废气进行逐层处理。
本发明在蒸发浓缩器内部竖直安装有挡板,挡板将蒸发浓缩器的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通,由排液管向喷淋机构中通入加热后的废水,废水经喷淋机构向废水池中喷洒,废水喷洒过程中,水蒸气向上流动并通过蒸汽通道进入冷凝水池中,废液流入废水池池底,水蒸气冷凝后汇聚成水流存积与冷凝水池底部,从而在密闭环境中模拟水蒸发和降雨的气象环境,对废水进行蒸发浓缩处理。
以上的仅是本发明的优选实施方式,应当指出,对于本领域的技术人员来说,在不脱离本发明构思的前提下,还可以作出若干变形和改进,这些也应该视为本发明的保护范围,这些都不会影响本发明实施的效果和专利的实用性。

Claims (10)

  1. 一种模拟气象环境的蒸发浓缩设备,包括蒸发浓缩器(4);其特征在于,所述蒸发浓缩器(4)内部竖直安装有挡板(13),挡板(13)将蒸发浓缩器(4)的内部分为废水池和冷凝水池,废水池和冷凝水池的上部通过蒸汽通道相互连通;所述蒸发浓缩器(4)位于废水池的上部连通有排液管(5),蒸发浓缩器(4)位于废水池的上部安装有喷淋机构(6),喷淋机构(6)与排液管(5)连通。
  2. 根据权利要求1所述的模拟气象环境的蒸发浓缩设备,其特征在于,包括有循环泵(19),循环泵(19)的进液端连通有废液排出管(18),所述废水池池底开设有浓液排出口(17),浓液排出口(17)与废液排出管(18)连通,所述循环泵(19)的排液端通过连接管(3)与排液管(5)连通。
  3. 根据权利要求2所述的模拟气象环境的蒸发浓缩设备,其特征在于,还包括有进液管(1)和过滤器(2),进液管(1)与过滤器(2)连通,过滤器(2)与连接管(3)连通。
  4. 根据权利要求3所述的模拟气象环境的蒸发浓缩设备,其特征在于,所述喷淋机构(6)包括转动安装于排液管(5)排液端的转盘(21),转盘(21)的底部均匀开设有若干喷头(23),转盘(21)的圆心处开设有进液口(24),进液口(24)与排液管(5)连通,进液口(24)还通过若干输液管(25)与喷头(23)连通。
  5. 根据权利要求4所述的模拟气象环境的蒸发浓缩设备,其特征在于,所述转盘(21)上均匀开设有若干通孔(22)。
  6. 根据权利要求5所述的模拟气象环境的蒸发浓缩设备,其特征在于,所述挡板(13)的上部通过支架(15)转动安装有导流器(14),导流器(14)包括转动安装于支架(15)的转动轴和若干固定安装于转动轴轴侧的导流板。
  7. 根据权利要求1所述的模拟气象环境的蒸发浓缩设备,其特征在于,还包括有开设于冷凝水池底部的冷却水排出口和与蒸发浓缩器(4)连通的废气处理器(12)。
  8. 根据权利要求7所述的模拟气象环境的蒸发浓缩设备,其特征在于,所述废气处理器(12)包括与蒸发浓缩器(4)连通的筒体(31),筒体(31)内部沿废气流动方向依次安装有粗滤网(34)、精细滤网(33)和活性炭层(32)。
  9. 根据权利要求1所述的模拟气象环境的蒸发浓缩设备,其特征在于,所述挡板(13)朝向冷凝水池的一侧自上而下依次转动安装有若干混合器(16),混合器(16)包括转动安装于挡板(13)上的旋转轴和固定安装于旋转轴上的螺旋叶。
  10. 根据权利要求9所述的模拟气象环境的蒸发浓缩设备,其特征在于,所述旋转轴与挡板(13)的连接端固定安装有第一齿轮(27),相邻两个第一齿轮(27)之间通过第二齿轮(28)连接,所述挡板(13)上还固定安装有减速电机(29),减速电机(29)的输出端固定安装有第三齿轮(30),第三齿轮与第一齿轮(27)啮合。
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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112707459A (zh) * 2020-12-28 2021-04-27 国网河北省电力有限公司电力科学研究院 一种模拟气象环境的蒸发浓缩设备
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004105819A (ja) * 2002-09-17 2004-04-08 Sanken Setsubi Kogyo Co Ltd 廃熱回収型脱気用水製造システム
CN203715317U (zh) * 2014-01-14 2014-07-16 辽宁科技大学 一种高盐水低温循环蒸发结晶装置
CN203741071U (zh) * 2014-01-17 2014-07-30 北京万邦达环保技术股份有限公司 蒸发浓缩设备
CN106391342A (zh) * 2016-11-29 2017-02-15 洛阳隆华传热节能股份有限公司 一种旋转喷头
CN206215400U (zh) * 2016-11-29 2017-06-06 洛阳隆华传热节能股份有限公司 一种旋转喷头
CN112707459A (zh) * 2020-12-28 2021-04-27 国网河北省电力有限公司电力科学研究院 一种模拟气象环境的蒸发浓缩设备

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111569471A (zh) * 2020-04-16 2020-08-25 浙江农林大学暨阳学院 一种汽油蒸汽回收装置

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004105819A (ja) * 2002-09-17 2004-04-08 Sanken Setsubi Kogyo Co Ltd 廃熱回収型脱気用水製造システム
CN203715317U (zh) * 2014-01-14 2014-07-16 辽宁科技大学 一种高盐水低温循环蒸发结晶装置
CN203741071U (zh) * 2014-01-17 2014-07-30 北京万邦达环保技术股份有限公司 蒸发浓缩设备
CN106391342A (zh) * 2016-11-29 2017-02-15 洛阳隆华传热节能股份有限公司 一种旋转喷头
CN206215400U (zh) * 2016-11-29 2017-06-06 洛阳隆华传热节能股份有限公司 一种旋转喷头
CN112707459A (zh) * 2020-12-28 2021-04-27 国网河北省电力有限公司电力科学研究院 一种模拟气象环境的蒸发浓缩设备

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115028221A (zh) * 2022-07-20 2022-09-09 江苏新宏大集团有限公司 一种节能环保型工业废水浓缩装置
CN115738314A (zh) * 2022-11-15 2023-03-07 泊头市航澄机械制造有限公司 多功能真空提取浓缩机组
CN116426366A (zh) * 2023-06-09 2023-07-14 山东大树生命健康科技有限公司 一种生产星形狍菌素的海洋链霉菌发酵优化系统
CN116426366B (zh) * 2023-06-09 2023-09-08 山东大树生命健康科技有限公司 一种生产星形狍菌素的海洋链霉菌发酵优化系统
CN116727389A (zh) * 2023-08-08 2023-09-12 佳木斯大学 一种用于临床医学的积液存储容器清洁设备
CN116727389B (zh) * 2023-08-08 2023-10-17 佳木斯大学 一种用于临床医学的积液存储容器清洁设备
CN116947268A (zh) * 2023-09-20 2023-10-27 海普欧环保集团有限公司 一种高盐废水脱盐处理装置
CN116947268B (zh) * 2023-09-20 2023-12-22 海普欧环保集团有限公司 一种高盐废水脱盐处理装置
CN117263296A (zh) * 2023-11-21 2023-12-22 山东戴克生物科技有限公司 一种二甲硝咪唑生产废水收纳装置及方法
CN117263296B (zh) * 2023-11-21 2024-02-02 山东戴克生物科技有限公司 一种二甲硝咪唑生产废水收纳装置及方法
CN117263297A (zh) * 2023-11-24 2023-12-22 山东无棣海丰电缆有限公司 一种用于高盐浓水的处理装置
CN117263297B (zh) * 2023-11-24 2024-02-13 山东三岳化工有限公司 一种用于高盐浓水的处理装置

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