CN102849810A - Novel combination type evaporation condenser - Google Patents

Novel combination type evaporation condenser Download PDF

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CN102849810A
CN102849810A CN201210321694XA CN201210321694A CN102849810A CN 102849810 A CN102849810 A CN 102849810A CN 201210321694X A CN201210321694X A CN 201210321694XA CN 201210321694 A CN201210321694 A CN 201210321694A CN 102849810 A CN102849810 A CN 102849810A
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combination type
novel combination
condenser
type vaporizer
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吴宏
李育隆
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Beihang University
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Abstract

本发明公开了一种适用于同时存在着蒸发和冷凝两种换热过程的新型组合式蒸发冷凝器,包括由法兰连接的容器,以及由旋转轴带动的由多个盘面组成起蒸发作用的旋转蒸发盘、与旋转蒸发盘盘面平行放置的冷凝管。其主要特征是:冷凝管直列分布,两组旋转换热盘与冷凝管以小间距交错排列。该新型组合式的蒸发冷凝器将蒸发器和冷凝器合二为一,结构紧凑,换热效率高。

Figure 201210321694

The invention discloses a novel combined evaporative condenser suitable for two heat exchange processes of evaporating and condensing at the same time. Rotary evaporator, condenser tube placed parallel to the surface of the rotary evaporator. Its main features are: the condensing pipes are arranged in a straight line, and the two sets of rotating heat exchange plates and the condensing pipes are arranged alternately at small intervals. The new combined evaporative condenser combines the evaporator and the condenser into one, with compact structure and high heat exchange efficiency.

Figure 201210321694

Description

一种新型组合式蒸发冷凝器A New Combined Evaporation Condenser

技术领域 technical field

海水淡化、污水处理、液体浓缩等化工行业中,在实现工艺流程的过程中往往同时需要一个蒸发设备和一个冷凝设备,而蒸发设备和冷凝设备效率的高低又会对整个系统的效率有着重要的影响。本发明设计一种新型组合式蒸发冷凝器,适用于同时存在着蒸发和冷凝两种换热过程的工艺设备。这种新型组合式的蒸发冷凝器将蒸发器和冷凝器合二为一,以达到紧凑系统结构,提高工艺流程效率的目的。In seawater desalination, sewage treatment, liquid concentration and other chemical industries, an evaporation device and a condensation device are often required in the process of realizing the process, and the efficiency of the evaporation device and the condensation device will have an important impact on the efficiency of the entire system. Influence. The invention designs a novel combined evaporative condenser, which is suitable for process equipment with two heat exchange processes of evaporation and condensation. This new combined evaporative condenser combines the evaporator and the condenser into one to achieve a compact system structure and improve process efficiency.

背景技术 Background technique

在海水淡化、污水处理、液体蒸馏浓缩等化工行业的工艺流程中,往往会同时有蒸发和冷凝两种换热过程。在采用压汽蒸馏方法的污水处理工艺中,蒸发器用于将废水液由液态蒸发为气态,蒸发出来的水蒸气依靠压缩机提高压力和温度,然后进入到冷凝器中冷凝为纯净水。显然在这个工艺过程中废水液在蒸发器中由液态变为气态的时候吸收热量,而水蒸气在冷凝器中冷凝为纯净水的时候放出热量。目前的工艺设备通常都是两个独立工作的蒸发器和冷凝器,蒸发器与冷凝器通过管路相连,结构复杂,操作不便,容易结垢,循环泵的使用又使系统需消耗大量的泵功,上述原因使得整个工艺系统的效率低下。本发明提出一种新型组合式蒸发冷凝器,其蒸发器采用两组旋转蒸发盘,冷凝器采用直列式分布的冷凝管,两组旋转蒸发盘与冷凝管以小间距交错排列,从而将蒸发器与冷凝器组合为一体,不仅使得系统结构紧凑,而且可以利用冷凝过程放出的热量来维持蒸发过程所需要吸收的热量,节省了资源,提高了系统的工作效率。采用这种组合式的蒸发冷凝器,可以使同时存在蒸发和冷凝两种换热过程的工艺流程的系统效率大大提高。In the process of chemical industry such as seawater desalination, sewage treatment, liquid distillation and concentration, there are often two heat transfer processes of evaporation and condensation at the same time. In the sewage treatment process using the pressure steam distillation method, the evaporator is used to evaporate the wastewater liquid from liquid to gaseous state. The evaporated water vapor depends on the compressor to increase the pressure and temperature, and then enters the condenser to condense into pure water. Obviously, in this process, the waste water absorbs heat when it changes from liquid to gas in the evaporator, and the water vapor releases heat when it condenses into pure water in the condenser. The current process equipment usually consists of two independently working evaporators and condensers. The evaporator and the condenser are connected through pipelines. The structure is complicated, the operation is inconvenient, and it is easy to scale. The use of circulating pumps makes the system consume a lot of pumps. The above-mentioned reasons make the efficiency of the whole process system low. The invention proposes a new type of combined evaporation condenser, the evaporator adopts two sets of rotating evaporating pans, the condenser adopts in-line distributed condensing pipes, and the two sets of rotating evaporating pans and condensing pipes are arranged alternately at small intervals, so that the evaporator Combined with the condenser, it not only makes the system compact, but also can use the heat released during the condensation process to maintain the heat absorbed by the evaporation process, saving resources and improving the working efficiency of the system. The use of this combined evaporative condenser can greatly improve the system efficiency of a technological process in which two heat exchange processes of evaporation and condensation exist at the same time.

发明内容Contents of the invention

本发明目的是提供一种新型组合式蒸发冷凝器,适用于同时存在着蒸发和冷凝两种换热过程的工艺设备。该结构包括由法兰(9)连接的容器(3),以及由旋转轴(10)带动的由多个盘面组成起蒸发作用的旋转蒸发盘(2)、与旋转蒸发盘(2)盘面平行放置的冷凝管(8)。其主要特征是:冷凝管(8)直列分布,两组旋转换热盘(2)与冷凝管(8)以小间距交错排列,旋转蒸发盘(2)由定位环(10)进行间隔定位,旋转轴(11)在冷凝管(8)的上方,容器(3)一端布置有分气腔(7),另一端布置有集水腔(4),容器(3)的集水腔(4)一侧还开有排污口(5)。此外在容器(3)中还布置有气液分离网(1),底部布置加热块(6)。The object of the present invention is to provide a novel combined evaporative condenser, which is suitable for process equipment with two heat exchange processes of evaporation and condensation. The structure includes a container (3) connected by a flange (9), and a rotary evaporator (2) driven by a rotating shaft (10) composed of a plurality of disks for evaporation, parallel to the surface of the rotary evaporator (2) Place the condenser tube (8). Its main features are: the condensing pipes (8) are arranged in a straight line, two sets of rotating heat exchange plates (2) and the condensing pipes (8) are arranged alternately at small intervals, and the rotating evaporating plates (2) are positioned at intervals by the positioning ring (10). The rotating shaft (11) is above the condensation pipe (8), the container (3) is arranged with an air distribution chamber (7) at one end, and the other end is arranged with a water collection chamber (4), and the water collection chamber (4) of the container (3) One side also has a sewage outlet (5). In addition, a gas-liquid separation net (1) is arranged in the container (3), and a heating block (6) is arranged at the bottom.

本发明的这种新型组合式蒸发冷凝器的优点在于:1)冷凝器采用直列式分布的冷凝管,大大提高了系统的可靠性。2)旋转式的蒸发盘可以使盘表面的液体全部蒸发,提高了蒸发效率。3)旋转蒸发盘可根据蒸发量的不同分为一组、两组或者多组,适合于各种蒸发场合。4)组合式的蒸发冷凝器,可以节省管路中的热量损失以及循环泵功,提高系统的效率。5)旋转式的蒸发盘可以在旋转的过程中在一定程度上减小冷凝管和盘面的结垢速度。The advantages of the new combined evaporative condenser of the present invention are: 1) The condenser adopts in-line distributed condensing pipes, which greatly improves the reliability of the system. 2) The rotating evaporator can evaporate all the liquid on the surface of the plate, which improves the evaporation efficiency. 3) The rotary evaporator can be divided into one group, two groups or multiple groups according to the different evaporation capacity, which is suitable for various evaporation occasions. 4) The combined evaporative condenser can save heat loss in the pipeline and circulation pump work, and improve the efficiency of the system. 5) The rotating evaporator can reduce the fouling speed of the condenser tube and the disk surface to a certain extent during the rotation process.

附图说明 Description of drawings

图1本发明的新型组合式蒸发冷凝器结构主视图Fig. 1 front view of the structure of the novel combined evaporative condenser of the present invention

图2本发明的新型组合式蒸发冷凝器结构侧视图Figure 2 is a side view of the structure of the novel combined evaporative condenser of the present invention

图3本发明的新型组合式蒸发冷凝器结构俯视图Figure 3 is a top view of the structure of the novel combined evaporative condenser of the present invention

图中:1.气液分离网    2.旋转蒸发盘    3.容器      4.集水腔In the figure: 1. Gas-liquid separation net 2. Rotary evaporator 3. Container 4. Water collection chamber

      5.排污口        6.加热块        7.分气腔    8.冷凝管5. Sewage outlet 6. Heating block 7. Air distribution chamber 8. Condenser tube

      9.法兰          10.定位环       11.旋转轴9. Flange 10. Locating ring 11. Rotary shaft

具体实施方式Detailed ways

下面将结合附图对本发明作进一步的详细说明。The present invention will be further described in detail below in conjunction with the accompanying drawings.

附图示出了本发明的新型组合式蒸发冷凝器结构,在工作过程中,工质液体盛载在容器(3)中,旋转轴(11)轴心稍微高于液面,而冷凝器的冷凝管束全部位于液面下方。旋转蒸发盘(2)通过旋转携带起液体并且在液面上部空间中蒸发,其蒸发量的大小通过旋转蒸发盘(2)的转速以及旋转蒸发盘(2)的组数来控制。蒸发后的蒸气首先通过气液分离网(1),分离出气体并排出容器(3)。该气体而后经过压缩机使其温度压力升高,继而通到容器(3)的分气腔(7)中,分气腔(7)将蒸汽均匀的分配给冷凝管(8)。由于刚通入冷凝管(8)的气体温度稍高于容器(3)中液体温度,因此存在一个换热温差,该温差使得冷凝管(8)中的气体冷凝为液体,并且放出热量。同时该温差可以维持容器(3)中液体的继续蒸发,蒸发时所需的热量即由冷凝放出的热量而得到。当然容器(3)中的液体初始时蒸发所需要的热量由加热块(6)提供,系统正常运转之后加热块(6)便停止工作,右冷凝放出的热量来维持蒸发。当气体在冷凝管(8)中凝结为液体后,便流入集水腔(4)中。在污水处理工艺中,最终废水处理后的残渣通过排污口(5)排出。当然在浓缩工艺中,浓缩液也通过排污口(5)排出。旋转蒸发盘(2)不仅可以增大液体的蒸发面积,而且可以搅动液体,容器(3)中的液体混合的更均匀,在污水处理的工艺中,旋转式的蒸发盘(2)还可以在旋转的过程中在一定程度上减小冷凝管和盘面的结垢速度。旋转蒸发盘(2)与冷凝管(8)以小间距交错排列,不仅将蒸发器与冷凝器组合为一体使系统结构更为紧凑,而且可以使蒸发过程和冷凝过程的换热更为强烈。The accompanying drawings show the structure of the new combined evaporative condenser of the present invention. During the working process, the working medium liquid is contained in the container (3), and the axis of the rotating shaft (11) is slightly higher than the liquid level, while the condenser The condensing tube bundles are all located below the liquid surface. The rotary evaporator (2) carries the liquid through rotation and evaporates in the space above the liquid surface, and the amount of evaporation is controlled by the rotation speed of the rotary evaporator (2) and the number of groups of the rotary evaporator (2). The evaporated vapor first passes through the gas-liquid separation net (1), and the gas is separated and discharged out of the container (3). The gas then passes through the compressor to increase its temperature and pressure, and then passes into the gas distribution chamber (7) of the container (3), and the gas distribution chamber (7) distributes the steam evenly to the condensation pipe (8). Since the temperature of the gas just passed into the condenser tube (8) is slightly higher than the liquid temperature in the container (3), there is a heat exchange temperature difference, which makes the gas in the condenser tube (8) condense into liquid and release heat. At the same time, the temperature difference can maintain the continuous evaporation of the liquid in the container (3), and the heat required for evaporation is obtained from the heat released by condensation. Of course, the heat required for the initial evaporation of the liquid in the container (3) is provided by the heating block (6). After the system is in normal operation, the heating block (6) stops working, and the heat released by condensation is used to maintain evaporation. After the gas condenses into liquid in the condensation pipe (8), it flows into the water collection chamber (4). In the sewage treatment process, the residue after the final wastewater treatment is discharged through the sewage outlet (5). Of course, in the concentration process, the concentrated liquid is also discharged through the sewage outlet (5). The rotary evaporator (2) can not only increase the evaporation area of the liquid, but also stir the liquid, and the liquid in the container (3) can be mixed more evenly. In the process of sewage treatment, the rotary evaporator (2) can also be used in During the rotation process, the fouling speed of the condenser tube and the disk surface is reduced to a certain extent. The rotary evaporator (2) and the condensing tube (8) are alternately arranged at small intervals, which not only integrates the evaporator and the condenser to make the system more compact, but also makes the heat exchange between the evaporation process and the condensation process more intense.

本发明经过制作的样机的实测表明:可调节的蒸发量使系统的应用更加灵活,直列式的冷凝管使系统更加可靠,并且冷凝管中的蒸汽与容器中的液体可以实现1-4℃的小温差换热,具有非常高的换热效率。The actual measurement of the manufactured prototype of the present invention shows that the adjustable evaporation makes the application of the system more flexible, the in-line condensation pipe makes the system more reliable, and the steam in the condensation pipe and the liquid in the container can achieve a temperature of 1-4°C. Small temperature difference heat transfer, with very high heat transfer efficiency.

Claims (10)

1. novel combination type vaporizer-condenser, comprise container (3), by turning axle (10) drive by a plurality of cards has formed Evaporation rotary evaporation dish (2), with the prolong (8) of the parallel placement of rotary evaporation dish (2) card, it is characterized in that: the card of prolong (8) and rotary evaporation dish (2) is interlocked and is spaced.
2. novel combination type vaporizer-condenser according to claim 1 is characterized in that: described prolong (8) distribution in upright arrangement.
3. novel combination type vaporizer-condenser according to claim 1 is characterized in that: the top and the bottom of described container (3) connect by flange (9).
4. novel combination type vaporizer-condenser according to claim 1 is characterized in that: gas-liquid separation net (1) is arranged on the described container (3).
5. novel combination type vaporizer-condenser according to claim 1, it is characterized in that: described turning axle (11) is in the top of prolong (8).
6. novel combination type vaporizer-condenser according to claim 1, it is characterized in that: described container (3) one ends are furnished with a minute air cavity (7), and container (3) the other end is furnished with collect cavity (4).
7. novel combination type vaporizer-condenser according to claim 1 is characterized in that: described container (3) bottom layout heat block (6).
8. novel combination type vaporizer-condenser according to claim 1, it is characterized in that: described container (3) is furnished with sewage draining exit (5) in collect cavity (4) one sides.
9. novel combination type vaporizer-condenser according to claim 1, it is characterized in that: described rotary evaporation dish (2) carries out positioned at intervals by retaining ring (10).
10. novel combination type vaporizer-condenser according to claim 1, it is characterized in that: described rotary evaporation dish (2) can be divided into according to the difference of steam output one group, two groups or many groups.
CN201210321694XA 2012-09-03 2012-09-03 Novel combination type evaporation condenser Pending CN102849810A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105347411A (en) * 2014-08-20 2016-02-24 张迎立 Water purification treatment system and water purification treatment process
CN105617704A (en) * 2016-02-24 2016-06-01 江苏瑞达环保科技有限公司 Evaporation and condensation tank used for mechanical vapor compression distillation process and provided with separation chamber
CN106237637A (en) * 2016-10-16 2016-12-21 石家庄英之杰化工机械有限公司 A kind of horizontal rotating disk vaporizer
CN109696063A (en) * 2018-12-28 2019-04-30 朱玲燕 A kind of rotating disc type thin film evaporation cooling tower

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CN102589199A (en) * 2012-03-13 2012-07-18 吴思 Combined wheel plate type evaporator condenser

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1570354A (en) * 1920-12-31 1926-01-19 Westinghouse Electric & Mfg Co Locomotive surface condenser
JPS60220101A (en) * 1984-04-13 1985-11-02 Jinichi Nishimura Disc-type decompression evaporation separator
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CN102589199A (en) * 2012-03-13 2012-07-18 吴思 Combined wheel plate type evaporator condenser

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105347411A (en) * 2014-08-20 2016-02-24 张迎立 Water purification treatment system and water purification treatment process
CN105617704A (en) * 2016-02-24 2016-06-01 江苏瑞达环保科技有限公司 Evaporation and condensation tank used for mechanical vapor compression distillation process and provided with separation chamber
CN106237637A (en) * 2016-10-16 2016-12-21 石家庄英之杰化工机械有限公司 A kind of horizontal rotating disk vaporizer
CN109696063A (en) * 2018-12-28 2019-04-30 朱玲燕 A kind of rotating disc type thin film evaporation cooling tower

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Application publication date: 20130102