CN116407856A - A three-dimensional moving spiral automatic cleaning falling film evaporator - Google Patents
A three-dimensional moving spiral automatic cleaning falling film evaporator Download PDFInfo
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- CN116407856A CN116407856A CN202111644718.0A CN202111644718A CN116407856A CN 116407856 A CN116407856 A CN 116407856A CN 202111644718 A CN202111644718 A CN 202111644718A CN 116407856 A CN116407856 A CN 116407856A
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- 238000004140 cleaning Methods 0.000 title claims abstract description 77
- 239000011552 falling film Substances 0.000 title claims abstract description 22
- 238000010438 heat treatment Methods 0.000 claims abstract description 78
- 239000007788 liquid Substances 0.000 claims abstract description 26
- 238000013461 design Methods 0.000 claims abstract description 22
- 239000010408 film Substances 0.000 claims abstract description 17
- 230000000630 rising effect Effects 0.000 claims abstract description 3
- 238000009825 accumulation Methods 0.000 claims description 7
- 230000008859 change Effects 0.000 claims description 5
- 230000001174 ascending effect Effects 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 238000012546 transfer Methods 0.000 abstract description 9
- 238000009826 distribution Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 230000007774 longterm Effects 0.000 abstract description 3
- 238000005299 abrasion Methods 0.000 abstract description 2
- 230000002265 prevention Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000002301 combined effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005315 distribution function Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
- B01D1/12—Evaporators with vertical tubes and forced circulation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/22—Evaporating by bringing a thin layer of the liquid into contact with a heated surface
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28G—CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
- F28G15/00—Details
- F28G15/02—Supports for cleaning appliances, e.g. frames
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28G—CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
- F28G9/00—Cleaning by flushing or washing, e.g. with chemical solvents
- F28G9/005—Cleaning by flushing or washing, e.g. with chemical solvents of regenerative heat exchanger
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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Abstract
Description
技术领域technical field
本发明的一种三维运动螺旋自动清洗式降膜蒸发器,主要涉及列管降膜蒸发器、换热器的管内污垢的自动清洗和传热强化。The invention relates to a three-dimensional moving spiral automatic cleaning falling film evaporator, which mainly relates to the automatic cleaning and heat transfer enhancement of the dirt in the tubes of the tube falling film evaporator and heat exchanger.
背景技术Background technique
现有蒸发器面对加热管内的污垢问题,大多数没有自动清洗技术,几乎都是采用周期性停车清洗的办法处理。周期平均的传热系数一般只有无垢时的1/3—2/3,无论产能损失和能量损失都很大。Existing evaporators face the problem of fouling in the heating pipes, most of which do not have automatic cleaning technology, and almost all of them adopt the method of periodic parking and cleaning. The cycle average heat transfer coefficient is generally only 1/3-2/3 of the time without scale, and both capacity loss and energy loss are very large.
对于这种容易结垢溶液的蒸发,强制循环蒸发器是采用得比较多的一种选择,但是付出的代价太高。例如,高盐废水的某国产MVR热泵列管蒸发器,220KW的热泵,需要配置110KW的强制循环泵,使加热管内的平均流速高达1.8m/s,利用其悬浮的盐晶实现流态化冲刷来生产,延缓结垢和延长生产运行时间,不仅大幅度降低热泵蒸发装置的节能效率,而且传热系数是仍然非常低,只有350(w/m2.℃),还需要每两周停车清洗一次。For the evaporation of this easy-to-scaling solution, the forced circulation evaporator is a more widely used option, but the price paid is too high. For example, a domestic MVR heat pump tube evaporator for high-salt wastewater, a 220KW heat pump, needs to be equipped with a 110KW forced circulation pump to make the average flow rate in the heating tube as high as 1.8m/s, and use its suspended salt crystals to achieve fluidized flushing To produce, delay fouling and prolong production operation time, not only greatly reduce the energy saving efficiency of the heat pump evaporation device, but also the heat transfer coefficient is still very low, only 350 (w/m 2 .℃), and it needs to be stopped every two weeks for cleaning once.
近几年公开的降膜式自动清洗技术专利,例如,ZL201110038777.3,一种管内自动清洗防垢降膜式蒸发装置;ZL201711042017.3,波流阀自动清洗式竖管降膜蒸发器。除了自动清洗螺旋外,还需要布膜器、往复动力弹簧、安装固定动力弹簧的架盘,上管箱高度要求大,安装技术要求比较高,总体结构太复杂,不利于工程要求的高可靠性。Falling film automatic cleaning technology patents published in recent years, for example, ZL201110038777.3, an in-tube automatic cleaning anti-scaling falling film evaporator; ZL201711042017.3, wave flow valve automatic cleaning vertical pipe falling film evaporator. In addition to the automatic cleaning screw, it also needs a membrane distributor, a reciprocating power spring, and a frame for installing a fixed power spring. The height of the upper tube box is required to be high, and the installation technical requirements are relatively high. The overall structure is too complicated, which is not conducive to the high reliability required by the project. .
发明内容Contents of the invention
本发明提出的一种三维运动螺旋自动清洗式降膜蒸发器,通过巧妙的三维运动机结构设计,大大简化其自动清洗机构的整体方案,提高可靠性,便于安装,而且很好地保留了现有的三维运动自动清洗功能、全管程旋流布膜和换热管内对流传热强化的技术优势。A three-dimensional moving spiral automatic cleaning falling film evaporator proposed by the present invention greatly simplifies the overall scheme of its automatic cleaning mechanism through the ingenious structural design of the three-dimensional moving machine, improves reliability, facilitates installation, and well retains the existing It has the technical advantages of three-dimensional motion automatic cleaning function, full tube swirl film distribution and enhanced convective heat transfer in the heat exchange tube.
本发明的技术方案为:Technical scheme of the present invention is:
一种三维运动螺旋自动清洗式降膜蒸发器,主要部件有上管箱、三维运动机、加热室、加热管、自动清洗螺旋、分离室、循环泵。A three-dimensional moving spiral automatic cleaning falling film evaporator, the main components include an upper tube box, a three-dimensional moving machine, a heating chamber, a heating pipe, an automatic cleaning spiral, a separation chamber, and a circulating pump.
加热管内设置自动清洗螺旋。自动清洗螺旋上部的直线轴段,穿过三维运动机的轴孔后,钩头轴段悬挂在三维运动机的端面轨道上。An automatic cleaning spiral is arranged in the heating tube. The linear shaft section on the upper part of the automatic cleaning screw passes through the shaft hole of the three-dimensional kinematic machine, and the hook head shaft section is suspended on the end track of the three-dimensional kinematic machine.
三维运动机有三维运动机身管、端面轨道、轴承毂、轴孔、平衡孔、十字固定架、螺旋齿。三维运动机身管利用十字固定架和螺旋齿固定安装在加热管的进口段。十字固定架的宽度尺寸B要求比加热管之间的中心距大1mm以上,利用相邻加热管的十字固定架自转时的必然相互卡住,非常可靠地避免发生自转的可能性。The three-dimensional motion machine has a three-dimensional motion body tube, an end track, a bearing hub, a shaft hole, a balance hole, a cross holder, and a helical tooth. The three-dimensional motion fuselage tube is fixedly installed on the inlet section of the heating tube by means of a cross bracket and a helical tooth. The width dimension B of the cross holder is required to be more than 1 mm larger than the center distance between the heating tubes, and the cross holders of adjacent heating tubes are bound to be locked when they rotate, so that the possibility of rotation can be avoided very reliably.
螺旋齿的齿高2~6mm,设计原则是加热管内的设计流速愈大,取值也愈大。螺旋齿的齿数是2~4,加热管内径愈大,设计的螺旋齿数愈多。螺旋齿的齿顶园与加热管内壁为小于0.15mm的过盈装配固定。螺旋齿的螺旋角γ范围是20°~35°,加热管内径愈大,螺旋角γ取值就愈小。The tooth height of the helical teeth is 2-6mm. The design principle is that the greater the design flow velocity in the heating tube, the greater the value. The number of teeth of the helical teeth is 2 to 4, and the larger the inner diameter of the heating tube is, the more the number of helical teeth is designed. The tooth top circle of the helical tooth and the inner wall of the heating tube are fixed by an interference fit less than 0.15mm. The range of the helix angle γ of the helical teeth is 20° to 35°, the larger the inner diameter of the heating tube, the smaller the value of the helix angle γ.
端面轨道的轴向高度变化是斜坡角α上升、斜坡角β下降。端面轨道的上升段一般取大半圆周,并且通常取200~280°,目的是力求有比较大的上下往复运动的行程。自动清洗螺旋的自转动力矩愈大,上升段的端面轨道设计的斜坡角α也愈大。The axial height change of the end track is that the slope angle α increases and the slope angle β decreases. The rising section of the end track generally takes a larger half of the circle, and usually takes 200-280°, the purpose is to strive for a relatively large up and down reciprocating stroke. The greater the self-rotation moment of the self-cleaning screw, the greater the slope angle α of the end track design of the ascending section.
轴孔直径2~3mm,比制造自动清洗螺旋的钢丝外径大0.05~0.20mm。轴承毂厚度2~4mm。The diameter of the shaft hole is 2-3 mm, which is 0.05-0.20 mm larger than the outer diameter of the steel wire used to manufacture the self-cleaning spiral. The thickness of the bearing hub is 2-4mm.
平衡孔的作用是使加热管内的二次蒸汽与上管箱内的蒸汽压保持基本平衡,保障积液层液体能够稳定顺畅地通过螺旋齿之间的流道,并且还有一定的速度流到加热管内壁去均匀成膜。平衡孔直径加热管内径愈大,平衡孔直径取值也愈大。平衡孔距离加热管管口的高度H2,要求比平稳运行操作的积液层H1深度大30mm以上。The function of the balance hole is to maintain a basic balance between the secondary steam in the heating tube and the steam pressure in the upper tube box, so as to ensure that the liquid in the accumulation layer can pass through the flow channel between the spiral teeth stably and smoothly, and there is still a certain speed to flow to the Heating the inner wall of the tube to form a uniform film. Balance hole diameter The larger the inner diameter of the heating tube, the larger the value of the balance hole diameter. The height H 2 of the balance hole from the nozzle of the heating tube is required to be more than 30mm greater than the depth of the effusion layer H 1 for smooth operation.
平稳运行操作的积液层H1深度范围为50~100mm。设计原则主要是考虑蒸发器加热温差愈大,取值也愈大;其次是上管箱的直径愈大、设计流量愈大,取值也需要比较大。The depth of effusion layer H1 for smooth running operation ranges from 50 to 100mm. The design principle is mainly to consider that the larger the heating temperature difference of the evaporator, the larger the value; the second is that the larger the diameter of the upper tube box and the larger the design flow rate, the larger the value also needs to be.
自动清洗螺旋采用直径1.5~2.2mm的不锈钢钢丝制造。自动清洗螺旋的外径与加热管内壁之间的间隙为3~7mm,加热管直径愈大、设计流量愈大,取值也就比较大。自动清洗螺旋的螺距为加热管内径的(1.3~1.9)倍。不锈钢钢丝直径和螺距的设计取值依据加热管内径和流速大小,并且与加热管内径和流速大小都为一致性的关系。自动清洗螺旋的长度比加热管短100-400mm。The self-cleaning spiral is made of stainless steel wire with a diameter of 1.5-2.2mm. The gap between the outer diameter of the self-cleaning spiral and the inner wall of the heating tube is 3-7mm. The larger the diameter of the heating tube and the larger the design flow rate, the larger the value. The pitch of the self-cleaning spiral is (1.3-1.9) times the inner diameter of the heating tube. The design values of the diameter and pitch of the stainless steel wire are based on the inner diameter and flow velocity of the heating tube, and are consistent with the inner diameter and flow velocity of the heating tube. The length of the self-cleaning spiral is 100-400mm shorter than the heating tube.
蒸发器运行时,循环料液自进液管进入上管箱后,先经过均布齿圈360°均匀地进入上管箱的积液层。利用深度H1的50~100mm积液层,保障流入每根加热管的流量大小基本均匀。对于加热管内降膜流的实际流速大小,反复百多次的模拟试验实测结果,都一致的表明高达1.3~2.2m/s。自动清洗螺旋在这样高流速的液膜冲击下,不仅发生每分钟数百次的径向随机振动,敲击加热管内壁的污垢,实现自动清洗;而且自动清洗螺旋对降膜液流的导流作用,使得整根加热管内壁的液膜都转变为螺旋线流,不仅产生对流传热强化作用,更重要的是能够非常有效的保障自上而下都具有很强的周向均匀布膜功能,从新机制上避免发生局部干壁和快速结垢。When the evaporator is running, the circulating feed liquid enters the upper tube box from the liquid inlet pipe, and then enters the liquid accumulation layer of the upper tube box evenly through the uniformly distributed ring gear 360°. Use the 50-100mm effusion layer at the depth H1 to ensure that the flow rate flowing into each heating tube is basically uniform. As for the actual flow velocity of the falling film flow in the heating tube, the actual measurement results of the simulated test repeated over a hundred times all consistently show that it is as high as 1.3-2.2m/s. Under the impact of such a high-velocity liquid film, the automatic cleaning screw not only generates hundreds of radial random vibrations per minute, knocking the dirt on the inner wall of the heating tube to realize automatic cleaning; but also the automatic cleaning screw guides the falling film flow The effect makes the liquid film on the inner wall of the whole heating tube change into a helical flow, which not only produces convective heat transfer enhancement, but more importantly, it can effectively ensure a strong circumferential uniform film distribution function from top to bottom , from the new mechanism to avoid local dry wall and rapid scaling.
自动清洗螺旋使液膜都转变为螺旋线流的同时,依据牛顿第三定律,自动清洗螺旋也获得了液膜反作用提供的自转动力矩其值还比较大,足以保障自转的动力需要。自动清洗螺旋自转时,在自动清洗螺旋顶段钩头轴与端面轨道相互作用下,沿着端面轨道不断地上升下降,往复运动。由于自动清洗螺旋的自转运动和上下往复运动,既增强了自动清洗螺旋的自动清洗防垢的能力,又大大提高了对加热管内壁振动敲击清洗的均匀性。While the self-cleaning screw transforms the liquid film into a helical flow, according to Newton's third law, the self-cleaning screw also obtains the rotation dynamic torque provided by the reaction of the liquid film. When the self-cleaning screw rotates, under the interaction between the hook head shaft of the top section of the self-cleaning screw and the end track, it continuously rises and falls along the end track, reciprocating. Due to the self-rotation and up-and-down reciprocating motion of the self-cleaning screw, the self-cleaning and anti-scaling ability of the self-cleaning screw is enhanced, and the uniformity of vibrating and knocking cleaning on the inner wall of the heating tube is greatly improved.
基于自动清洗螺旋的自动清洗防垢、对流传热强化、和全管程的周向布膜的三种功能的共同作用,比较理想的实现了降膜蒸发器长期稳定的连续高效生产的目标。Based on the combined effect of the three functions of automatic cleaning and anti-scaling of the automatic cleaning spiral, enhanced convective heat transfer, and circumferential film distribution throughout the tube, it is ideal to achieve the goal of long-term stable continuous high-efficiency production of the falling film evaporator.
由于自动清洗螺旋在沿着端面轨道上升段时很有效的减速作用,成功地控制其转速始终不超过每分钟120转,杜绝自动清洗螺旋与加热管内壁之间发生磨损的可能性,很好地满足工程的高可靠性要求。Due to the effective deceleration effect of the self-cleaning screw when it rises along the end track, its speed is successfully controlled to no more than 120 revolutions per minute, eliminating the possibility of abrasion between the self-cleaning screw and the inner wall of the heating tube, which is very good Meet the high reliability requirements of the project.
附图说明Description of drawings
图1是本发明的一种三维运动螺旋自动清洗式降膜蒸发器的总图Fig. 1 is the general diagram of a kind of three-dimensional motion spiral self-cleaning type falling film evaporator of the present invention
图2是三维运动机的剖视图Figure 2 is a cross-sectional view of the three-dimensional exercise machine
图3是三维运动机正视图Figure 3 is a front view of the three-dimensional exercise machine
图4是端面轨道高度的圆周360°展开图Figure 4 is a 360° development view of the circumference of the end track height
具体实施方式Detailed ways
图中的 01顶视镜 02上管箱 03液位计管 04均布齿圈 05管板 06三维运动机 07加热室 08自动清洗螺旋 09加热蒸汽进口分布室 10加热管 11冷凝水管 12二次蒸汽出口管 13汽液分离室 14循环泵 15加料管 16不凝气排放管 17进料管 18积液层 19钩头轴段20端面轨道 21轴承毂 22轴孔 23平衡孔 24三维运动机身管 25十字固定架 26直线轴段27螺旋齿01
一种三维运动螺旋自动清洗式降膜蒸发器,主要部件有上管箱02、三维运动机06、加热室07、加热管10、自动清洗螺旋08、汽液分离室13、循环泵14。A three-dimensional moving spiral automatic cleaning falling film evaporator, the main components are the
加热管10内设置自动清洗螺旋08。自动清洗螺旋08上部的直线轴段26,穿过三维运动机06的轴孔22后,钩头轴段19悬挂在三维运动机06的端面轨道20上。An
三维运动机06有三维运动机身管24、端面轨道20、轴承毂21、轴孔22、平衡孔23、十字固定架25、螺旋齿27。三维运动机身管24利用十字固定架25和螺旋齿27固定安装在加热管07的进口段。十字固定架25的宽度尺寸B要求比加热管07之间的中心距大1mm以上,利用相邻加热管07的十字固定架自转时的必然相互卡住,非常可靠地避免自转发生的可能性。Three-
螺旋齿27的齿高2~6mm,设计原则是加热管07内的设计流速愈大,取值也愈大。螺旋齿27的齿数是2~4,加热管07内径愈大,设计的螺旋齿27的齿数愈多。螺旋齿27的齿顶园与加热管07内壁为小于0.15mm的过盈装配固定。螺旋齿27的螺旋角γ取值范围是20°~35°,加热管27内径愈大,螺旋角γ设计值就愈小。The tooth height of the
端面轨道20的轴向高度变化是斜坡角α上升、斜坡角β下降。端面轨道20的上升段一般取大半圆周,并且通常取200~280°,目的是力求有比较大的上下往复运动的行程。自动清洗螺旋08的自转动力矩愈大,上升段的端面轨道20的斜坡角α也愈大。The axial height change of the
轴孔22直径2~3mm,比制造自动清洗螺旋08的钢丝外径大0.05~0.20mm。轴承毂21的厚度2~4mm。The
平衡孔22的作用是使加热管10内的二次蒸汽与上管箱02内的蒸汽压保持基本平衡,保障积液层18的液体稳定顺畅地通过螺旋齿27之间的流道,并且有一定的速度流到加热管10内壁去均匀成膜。平衡孔22直径加热管10内径愈大,平衡孔22直径取值也愈大。平衡孔22距离加热管10管口的高度H2,要求比平稳运行操作的积液层18的深度H1大30mm以上。The role of the
平稳运行操作的积液层18深度H1范围为50~100mm。设计原则主要是考虑蒸发器加热温差愈大,取值也愈大;其次是上管箱02的直径愈大、设计流量愈大,取值也需要比较大。The depth H 1 of the
自动清洗螺旋08采用直径1.5~2.2mm的不锈钢钢丝制造。自动清洗螺旋08的外径与加热管10内壁之间的间隙为3~7mm,加热管10直径愈大、设计流量愈大,取值也就比较大。自动清洗螺旋08的螺距为加热管10内径的(1.3~1.9)倍。不锈钢钢丝直径和螺距的设计取值依据加热管10内径和流速大小,并且与加热管10内径和流速大小都为一致性的关系。自动清洗螺旋08的长度比加热管10短100-400mm。The
蒸发器运行时,循环料液自进液管17进入上管箱02后,先经过均布齿圈04以360°方向均匀地进入上管箱02的积液层18。利用深度H1的50~100mm积液层18,保障流入每根加热管10的流量大小基本均匀。对于加热10管内降膜流的实际流速大小,反复百多次的模拟实测结果,都一致的表明高达1.3~2.2m/s。自动清洗螺旋08在这样高流速的液膜冲击下,不仅发生每分钟数百次的径向随机振动,敲击加热管10内壁的污垢,实现自动清洗;而且自动清洗螺旋08对降膜液流的导流作用,使得整根加热管10内壁的液膜都转变为螺旋线流,不就产生对流传热强化作用,更重要的是能够非常有效的保障自上而下都具有很强的周向均匀布膜功能,从新机制上避免发生局部干壁和快速结垢。When the evaporator is in operation, the circulating feed liquid enters the
自动清洗螺旋08使液膜都转变为螺旋线流的同时,依据牛顿第三定律,自动清洗螺旋08也获得了液膜的反作用提供的自转动力矩,其值还比较大,足以保障自转的动力需要。自动清洗螺旋08自转时,在自动清洗螺旋08顶段的钩头轴段19与端面轨道20相互作用下,沿着端面轨道20不断地上升、下降,往复运动。由于自动清洗螺旋08的自转运动和上下往复运动,增强了自动清洗螺旋08的自动清洗防垢的能力,还大大提高了对加热管10内壁振动敲击清洗的均匀性。While the self-cleaning
基于自动清洗螺旋08的自动清洗防垢、对流传热强化、和全管程的周向布膜的三种功能的共同作用,比较理想的实现了降膜蒸发器长期稳定、连续高效生产的目标。Based on the combined effect of the three functions of automatic cleaning and anti-scaling of the
由于自动清洗螺旋08在沿着端面轨道20上升段时很有效的减速作用,成功地控制其转速始终不超过每分钟120转,杜绝自动清洗螺旋08与加热管10内壁之间发生磨损的可能性,很好地满足工程基本要求的高可靠性。Due to the effective deceleration effect of the self-cleaning
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