CN204219809U - Dispensing orifice is provided with the falling film evaporation device of necking segment - Google Patents
Dispensing orifice is provided with the falling film evaporation device of necking segment Download PDFInfo
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- CN204219809U CN204219809U CN201420663580.8U CN201420663580U CN204219809U CN 204219809 U CN204219809 U CN 204219809U CN 201420663580 U CN201420663580 U CN 201420663580U CN 204219809 U CN204219809 U CN 204219809U
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- 239000011552 falling film Substances 0.000 title claims abstract description 37
- 238000001704 evaporation Methods 0.000 title claims abstract description 32
- 230000008020 evaporation Effects 0.000 title claims abstract description 30
- 239000007788 liquid Substances 0.000 claims abstract description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 239000007791 liquid phase Substances 0.000 claims abstract description 21
- 238000009833 condensation Methods 0.000 claims description 18
- 230000005494 condensation Effects 0.000 claims description 18
- 230000008676 import Effects 0.000 claims 3
- 125000004122 cyclic group Chemical group 0.000 claims 2
- 238000007599 discharging Methods 0.000 claims 2
- 238000009834 vaporization Methods 0.000 claims 2
- 230000008016 vaporization Effects 0.000 claims 2
- 239000010408 film Substances 0.000 abstract description 21
- 238000005192 partition Methods 0.000 abstract description 17
- 230000000694 effects Effects 0.000 abstract description 13
- 239000000463 material Substances 0.000 abstract description 10
- 238000010438 heat treatment Methods 0.000 abstract description 7
- 230000007704 transition Effects 0.000 abstract description 5
- 230000009286 beneficial effect Effects 0.000 description 7
- 230000005484 gravity Effects 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000002918 waste heat Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本实用新型涉及料液蒸发浓缩领域,目的是提供一种分配孔设有缩颈段的降膜蒸发装置。一种分配孔设有缩颈段的降膜蒸发装置,包括降膜蒸发器和蒸气冷凝器;降膜蒸发器包括设有下隔板的壳体,蒸发室,若干个换热管,与壳体上部连接的分配器;分配器和下隔板将壳体分隔成上腔、中腔和下腔;换热管的下端插装于下隔板并与下腔连通;分配器设有个数与换热管个数相同的分配孔;分配孔包括两个主段,缩颈段,两个过渡段;每个换热管的上端与一个主段连通;壳体设有与上腔连通的料液进口孔,与中腔连通的加热介质进口和凝水出口,与下腔连通的气液混合出口;蒸发室设有气液混合进孔,蒸气出口孔和液相出口孔。该分配孔设有缩颈段的降膜蒸发装置能兼顾成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度。
The utility model relates to the field of evaporating and concentrating feed liquid, and aims to provide a falling film evaporating device in which a distribution hole is provided with a necking section. A falling film evaporator with a distribution hole provided with a necking section, including a falling film evaporator and a steam condenser; the falling film evaporator includes a shell with a lower partition, an evaporation chamber, several heat exchange tubes, and a shell The distributor connected to the upper part of the body; the distributor and the lower partition divide the shell into an upper chamber, a middle chamber and a lower chamber; the lower end of the heat exchange tube is inserted into the lower partition and communicated with the lower chamber; the distributor has a number of The number of distribution holes is the same as that of the heat exchange tubes; the distribution holes include two main sections, a necking section, and two transition sections; the upper end of each heat exchange tube communicates with a main section; the shell is provided with a The feed liquid inlet hole, the heating medium inlet and the condensed water outlet connected with the middle cavity, and the gas-liquid mixing outlet connected with the lower cavity; the evaporation chamber is equipped with a gas-liquid mixing inlet hole, a steam outlet hole and a liquid phase outlet hole. The falling film evaporator with the necking section in the distribution hole can take into account the film forming effect and uniformity and the falling speed of the material liquid flowing along the inner side of the heat exchange tube in film form.
Description
技术领域 technical field
本实用新型涉及料液蒸发浓缩领域,尤其是一种分配孔设有缩颈段的降膜蒸发装置。 The utility model relates to the field of evaporation and concentration of feed liquid, in particular to a falling film evaporation device in which a distribution hole is provided with a constriction section.
背景技术 Background technique
分配孔设有缩颈段的降膜蒸发装置包括降膜蒸发器和蒸气冷凝器;中国专利申请号:201410015375.5 的实用新型公开了一种降膜式蒸发器,包括外壳体和竖向设置于外壳体内部的上隔板、下隔板和换热管,上隔板和下隔板将外壳体内腔分割成第一腔体、第二腔体和第三腔体,第一腔体和第二腔体位于上隔板的两侧,第二腔体和第三腔体位于下隔板两侧,换热管一端插装于上隔板并与第一腔体连通,换热管另一端插装于下隔板并与第三腔体连通,第一腔体设有进料口,第三腔体设有出料管,降膜式蒸发器还包括蒸发室,出料管的出口设于蒸发室内,蒸发室上部设有喷射泵,蒸发室下部设有出料口。降膜蒸发器是一种用于料液蒸发浓缩的间壁式热交换设备;料液从进料口经第一腔流入换热管,在重力作用下料液成膜状沿换热管内侧流动下降,进入第二腔的加热介质对换热管外侧加热,换热管中料液的水分被加热汽化,产生的蒸汽与液相共同进入蒸发室进行汽液分离,液相由出料口排出,蒸汽进入蒸气冷凝器冷凝;换热管较粗时料液成膜状沿换热管内侧流动下降速度较快,但成膜效果和均匀性较差;换热管较细时成膜效果和均匀性较好,但料液成膜状沿换热管内侧流动下降速度较慢;为了克服传统的降膜蒸发装置存在成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度不能兼顾的不足;因此,设计一种成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度能兼顾的分配孔设有缩颈段的降膜蒸发装置,成为亟待解决的问题。 The falling film evaporator with a necking section in the distribution hole includes a falling film evaporator and a vapor condenser; the utility model of Chinese patent application number: 201410015375.5 discloses a falling film evaporator, including an outer shell and a vertically arranged on the outer shell The upper partition, the lower partition and the heat exchange tube inside the body, the upper partition and the lower partition divide the inner cavity of the outer shell into the first cavity, the second cavity and the third cavity, the first cavity and the second cavity The cavity is located on both sides of the upper partition, the second cavity and the third cavity are located on both sides of the lower partition, one end of the heat exchange tube is inserted into the upper partition and communicated with the first cavity, and the other end of the heat exchange tube is inserted into the Installed on the lower partition and communicated with the third chamber, the first chamber is provided with a feed port, the third chamber is provided with a discharge pipe, the falling film evaporator also includes an evaporation chamber, and the outlet of the discharge pipe is located at In the evaporation chamber, a jet pump is arranged on the upper part of the evaporation chamber, and a discharge port is arranged on the lower part of the evaporation chamber. The falling film evaporator is a partitioned heat exchange equipment used for the evaporation and concentration of the feed liquid; the feed liquid flows into the heat exchange tube from the feed port through the first chamber, and the feed liquid forms a film and flows along the inside of the heat exchange tube under the action of gravity Descending, the heating medium entering the second chamber heats the outside of the heat exchange tube, the moisture in the feed liquid in the heat exchange tube is heated and vaporized, and the generated steam and liquid phase enter the evaporation chamber together for vapor-liquid separation, and the liquid phase is discharged from the discharge port , the steam enters the steam condenser to condense; when the heat exchange tube is thicker, the feed liquid forms a film and flows along the inner side of the heat exchange tube at a faster descending speed, but the film forming effect and uniformity are poor; when the heat exchange tube is thinner, the film forming effect and The uniformity is good, but the material liquid forms a film and flows along the inner side of the heat exchange tube at a slower rate; in order to overcome the traditional falling film evaporation device, there is a film forming effect and uniformity and the material liquid forms a film and flows down along the inner side of the heat exchange tube The speed cannot be taken into account; therefore, it is urgent to design a falling film evaporation device with a distribution hole and a necking section that can take into account the film-forming effect and uniformity and the film-forming flow of the material liquid along the inner side of the heat exchange tube. The problem.
实用新型内容 Utility model content
本实用新型的目的是为了克服目前的降膜蒸发装置存在成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度不能兼顾的不足,提供一种成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度能兼顾的分配孔设有缩颈段的降膜蒸发装置。 The purpose of this utility model is to overcome the deficiencies of the film-forming effect and uniformity of the current falling-film evaporator and the inability to take into account the falling speed of the material liquid forming a film along the inner side of the heat exchange tube, and to provide a film-forming effect and uniformity and The feed liquid forms a film and flows along the inner side of the heat exchange tube. The distribution hole can take into account the falling speed and is equipped with a falling film evaporation device with a necking section.
本实用新型的具体技术方案是: Concrete technical scheme of the present utility model is:
一种分配孔设有缩颈段的降膜蒸发装置,包括降膜蒸发器和蒸气冷凝器;降膜蒸发器包括设有下隔板的壳体,蒸发室,若干个换热管,与壳体上部连接的分配器;分配器和下隔板将壳体分隔成上腔、中腔和下腔;换热管的下端插装于下隔板并与下腔连通;分配器设有个数与换热管个数相同的分配孔;分配孔包括两个直径与换热管内径相同的主段,直径小于主段直径的缩颈段,两个两端分别与缩颈段一端和一个主段的一端连接的过渡段;换热管的上端与分配器连接且每个换热管的上端与一个主段连通;壳体设有与上腔连通的料液进口孔,与中腔连通的加热介质进口和凝水出口,与下腔连通的气液混合出口;蒸发室设有与气液混合出口连通的气液混合进孔,位于顶部的蒸气出口孔和位于底部的液相出口孔。该分配孔设有缩颈段的降膜蒸发装置使用时,蒸汽从加热介质进口进入中腔对换热管外侧加热;料液从料液进口孔进入上腔,经分配孔分配进入换热管加热并在重力作用下成膜状沿换热管内侧流动下降,换热管中料液的水分被加热汽化,产生的蒸汽与液相经气液混合出口共同进入蒸发室进行汽液分离,液相由液相出口孔排出,蒸汽从蒸气出口孔排出进入蒸气冷凝器进行冷凝;该分配孔设有缩颈段的降膜蒸发装置的降膜蒸发器的分配器的分配孔具有利于成膜的缩颈段,主段与换热管内径相同,能兼顾成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度。 A falling film evaporator with a distribution hole provided with a necking section, including a falling film evaporator and a steam condenser; the falling film evaporator includes a shell with a lower partition, an evaporation chamber, several heat exchange tubes, and a shell The distributor connected to the upper part of the body; the distributor and the lower partition divide the shell into an upper chamber, a middle chamber and a lower chamber; the lower end of the heat exchange tube is inserted into the lower partition and communicated with the lower chamber; the distributor has a number of The number of distribution holes is the same as that of the heat exchange tubes; the distribution holes include two main sections with the same diameter as the inner diameter of the heat exchange tubes, and a necking section with a diameter smaller than the diameter of the main section, and the two ends are respectively connected to one end of the necking section and a main section. The transition section connected to one end of the section; the upper end of the heat exchange tube is connected to the distributor and the upper end of each heat exchange tube is connected to a main section; the shell is provided with a feed liquid inlet hole connected to the upper cavity, and a Heating medium inlet and condensed water outlet, gas-liquid mixing outlet connected to the lower chamber; the evaporation chamber is provided with a gas-liquid mixing inlet connected to the gas-liquid mixing outlet, a steam outlet hole at the top and a liquid phase outlet hole at the bottom. When using the falling film evaporation device with the necking section in the distribution hole, the steam enters the middle cavity from the heating medium inlet to heat the outside of the heat exchange tube; the feed liquid enters the upper cavity from the feed liquid inlet hole, and is distributed into the heat exchange tube through the distribution hole It is heated and forms a film under the action of gravity to flow down along the inside of the heat exchange tube. The moisture in the feed liquid in the heat exchange tube is heated and vaporized, and the generated steam and liquid phase enter the evaporation chamber through the gas-liquid mixing outlet for vapor-liquid separation. The phase is discharged from the liquid phase outlet hole, and the steam is discharged from the steam outlet hole into the steam condenser for condensation; the distribution hole of the distributor of the falling film evaporator of the falling film evaporator with the necking section is provided with the distribution hole that is conducive to film formation. The necking section, the main section has the same inner diameter as the heat exchange tube, which can take into account the film forming effect and uniformity and the falling speed of the material liquid flowing along the inner side of the heat exchange tube in a film shape.
作为优选,所述的蒸气冷凝器包括冷凝室,位于冷凝室下方的循环水箱,喷射泵,多级离心泵;冷凝室包括设有冷凝进口且形状为鼓形的侧围壁和设有水腔并与侧围壁上端连接的进水盘;进水盘的上端面设有与水腔连通的进水孔;进水盘的下端面设有与水腔连通的出水孔组;多级离心泵分别与进水孔和循环水箱连接;喷射泵分别与蒸气出口孔和冷凝进口连接。从蒸气出口孔排出的蒸汽在喷射泵作用下经冷凝进口进入侧围壁中;在多级离心泵作用下,循环水箱中的冷却水经进水孔、水腔从出水孔组进入侧围壁中对蒸汽进行冷凝;蒸汽冷凝器结构简单,冷却效果好且循环使用冷却水节约用水。 Preferably, the steam condenser includes a condensation chamber, a circulating water tank located below the condensation chamber, a jet pump, and a multistage centrifugal pump; the condensation chamber includes a drum-shaped side wall provided with a condensation inlet and a water cavity The water inlet tray connected with the upper end of the side wall; the upper end surface of the water inlet tray is provided with a water inlet hole connected with the water chamber; the lower end surface of the water inlet tray is provided with a water outlet hole group connected with the water chamber; the multi-stage centrifugal pump They are respectively connected to the water inlet hole and the circulating water tank; the jet pump is respectively connected to the steam outlet hole and the condensation inlet. The steam discharged from the steam outlet hole enters the side wall through the condensing inlet under the action of the jet pump; under the action of the multi-stage centrifugal pump, the cooling water in the circulating water tank enters the side wall from the water outlet hole group through the water inlet hole and the water cavity The steam is condensed in the middle; the structure of the steam condenser is simple, the cooling effect is good, and the cooling water is recycled to save water.
作为优选,所述的上腔和蒸气出口孔之间设有平衡阀。通过平衡阀可以调节上腔和蒸发室的压力的相对平衡,利于料液在重力作用下成膜状沿换热管内侧流动下降。 Preferably, a balance valve is provided between the upper chamber and the steam outlet hole. The relative balance of pressure in the upper chamber and the evaporation chamber can be adjusted through the balance valve, which is beneficial for the material liquid to flow and descend in the form of a film along the inner side of the heat exchange tube under the action of gravity.
作为优选,所述的分配孔设有缩颈段的降膜蒸发装置还包括进料泵,截止阀,出料泵;进料泵通过截止阀与料液进口孔连接;出料泵与液相出口孔连接。进料泵利于料液进入上腔,截止阀用于控制料液进入上腔的流量;出料泵利于液相由液相出口孔排出。 As a preference, the falling film evaporation device with the necking section in the distribution hole also includes a feed pump, a stop valve, and a discharge pump; the feed pump is connected to the feed liquid inlet hole through the stop valve; the discharge pump is connected to the liquid phase Outlet hole connection. The feed pump facilitates the feed liquid to enter the upper chamber, and the stop valve is used to control the flow of the feed liquid into the upper chamber; the discharge pump facilitates the liquid phase to be discharged from the liquid phase outlet hole.
与现有技术相比,本实用新型的有益效果是:该分配孔设有缩颈段的降膜蒸发装置的降膜蒸发器的分配器的分配孔具有利于成膜的缩颈段,主段与换热管内径相同,能兼顾成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度。蒸汽冷凝器结构简单,冷却效果好且循环使用冷却水节约用水。通过平衡阀可以调节上腔和蒸发室的压力的相对平衡,利于料液在重力作用下成膜状沿换热管内侧流动下降。蒸汽从蒸气出口孔排出在压缩机作用下进入中腔余热利用。进料泵利于料液进入上腔,截止阀用于控制料液进入上腔的流量;出料泵利于液相由液相出口孔排出。 Compared with the prior art, the utility model has the beneficial effects that: the distribution hole of the distributor of the falling film evaporator of the falling film evaporator with the necking section is provided with a necking section which is beneficial to film formation, and the main section It is the same as the inner diameter of the heat exchange tube, which can take into account the film-forming effect and uniformity and the falling speed of the material liquid flowing along the inner side of the heat exchange tube in a film-like manner. The structure of the steam condenser is simple, the cooling effect is good, and the cooling water is recycled to save water. The relative balance of pressure in the upper chamber and the evaporation chamber can be adjusted through the balance valve, which is beneficial for the material liquid to flow and descend in the form of a film along the inner side of the heat exchange tube under the action of gravity. The steam is discharged from the steam outlet hole and enters the middle cavity under the action of the compressor for waste heat utilization. The feed pump facilitates the feed liquid to enter the upper chamber, and the stop valve is used to control the flow of the feed liquid into the upper chamber; the discharge pump facilitates the liquid phase to be discharged from the liquid phase outlet hole.
附图说明 Description of drawings
图1是本实用新型的一种结构示意图; Fig. 1 is a kind of structural representation of the utility model;
图2是图1中分配器的放大图。 Figure 2 is an enlarged view of the dispenser of Figure 1 .
图中:下隔板-1、壳体-2、料液进口孔-21、加热介质进口-22、凝水出口-23、气液混合出口-24、蒸发室-3、气液混合进孔-31、蒸气出口孔-32、液相出口孔-33、换热管-4、分配器-5、分配孔-51、主段-52、缩颈段-53、过渡段-54、进料泵-6、截止阀-7、出料泵-8、上腔-9、中腔-10、下腔-11、平衡阀-12、冷凝室-13、冷凝进口-131、侧围壁-132、水腔-133、进水盘-134、进水孔-135、出水孔组-136、循环水箱-14、喷射泵-15、多级离心泵-16。 In the figure: lower partition-1, shell-2, feed liquid inlet hole-21, heating medium inlet-22, condensed water outlet-23, gas-liquid mixing outlet-24, evaporation chamber-3, gas-liquid mixing inlet hole -31, steam outlet hole-32, liquid phase outlet hole-33, heat exchange tube-4, distributor-5, distribution hole-51, main section-52, necking section-53, transition section-54, feed Pump-6, globe valve-7, discharge pump-8, upper chamber-9, middle chamber-10, lower chamber-11, balance valve-12, condensation chamber-13, condensation inlet-131, side walls-132 , water cavity-133, water inlet tray-134, water inlet hole-135, water outlet hole group-136, circulating water tank-14, jet pump-15, multistage centrifugal pump-16.
具体实施方式 Detailed ways
下面结合附图所示对本实用新型进行进一步描述。 Below in conjunction with shown in the accompanying drawings the utility model is further described.
如附图1、附图2所示:一种分配孔设有缩颈段的降膜蒸发装置,包括降膜蒸发器和蒸气冷凝器;降膜蒸发器包括设有下隔板1的壳体2,蒸发室3,十个换热管4,与壳体2上部连接的分配器5,进料泵6,截止阀7,出料泵8;十个换热管4沿圆周均布;分配器5和下隔板1将壳体2分隔成上腔9、中腔10和下腔11;换热管4的下端插装于下隔板1并与下腔11连通;分配器5设有个数与换热管4个数相同的十个分配孔51;分配孔51包括两个直径与换热管4内径相同的主段52,直径小于主段52直径的缩颈段53,两个两端分别与缩颈段53一端和一个主段52的一端连接的过渡段54;所述的过渡段54的形状为锥台形。换热管4的上端与分配器5下端面焊接且每个换热管4的上端与一个主段52连通;壳体2设有与上腔9连通的料液进口孔21,与中腔10连通的加热介质进口22和凝水出口23,与下腔11连通的气液混合出口24;蒸发室3设有与气液混合出口24连通的气液混合进孔31,位于顶部的蒸气出口孔32和位于底部的液相出口孔33;蒸气出口孔32与蒸气冷凝器连接。 As shown in Figure 1 and Figure 2: a falling film evaporation device with a necking section in the distribution hole, including a falling film evaporator and a steam condenser; the falling film evaporator includes a shell with a lower partition 1 2. Evaporation chamber 3, ten heat exchange tubes 4, distributor 5 connected to the upper part of shell 2, feed pump 6, stop valve 7, discharge pump 8; ten heat exchange tubes 4 are evenly distributed along the circumference; The housing 2 is divided into an upper chamber 9, a middle chamber 10 and a lower chamber 11 by the device 5 and the lower partition 1; the lower end of the heat exchange tube 4 is inserted into the lower partition 1 and communicated with the lower chamber 11; the distributor 5 is provided Ten distribution holes 51 with the same number as the heat exchange tubes 4; the distribution holes 51 include two main sections 52 with the same diameter as the inner diameter of the heat exchange tubes 4, and a necking section 53 with a diameter smaller than the diameter of the main section 52, two A transition section 54 whose two ends are respectively connected to one end of the necking section 53 and one end of a main section 52; the shape of the transition section 54 is a truncated cone. The upper end of the heat exchange tube 4 is welded to the lower end of the distributor 5 and the upper end of each heat exchange tube 4 communicates with a main section 52; The connected heating medium inlet 22 and the condensed water outlet 23, the gas-liquid mixing outlet 24 communicating with the lower chamber 11; 32 and the liquid phase outlet hole 33 at the bottom; the vapor outlet hole 32 is connected with the steam condenser.
本实施例中,所述的蒸气冷凝器包括冷凝室13,位于冷凝室13下方的循环水箱14,喷射泵15,多级离心泵16;冷凝室13包括设有冷凝进口131且形状为鼓形的侧围壁132和设有水腔133并与侧围壁132上端焊接的进水盘134;进水盘134的上端面设有与水腔133连通的进水孔135;进水盘134的下端面设有与水腔133连通的出水孔组136;多级离心泵16分别与进水孔135和循环水箱14连接;喷射泵15分别与蒸气出口孔32和冷凝进口131连接。 In the present embodiment, the steam condenser includes a condensation chamber 13, a circulating water tank 14 located below the condensation chamber 13, a jet pump 15, and a multistage centrifugal pump 16; the condensation chamber 13 includes a condensing inlet 131 and a drum shape The side wall 132 and the water inlet tray 134 that is provided with a water cavity 133 and welded with the upper end of the side wall 132; The lower end surface is provided with a water outlet hole group 136 communicating with the water cavity 133; the multistage centrifugal pump 16 is respectively connected with the water inlet hole 135 and the circulating water tank 14; the jet pump 15 is connected with the steam outlet hole 32 and the condensation inlet 131 respectively.
进料泵6通过截止阀7与料液进口孔21连接。出料泵8与液相出口孔33连接;所述的上腔9和蒸气出口孔32之间设有平衡阀12。 The feed pump 6 is connected to the feed liquid inlet hole 21 through the shut-off valve 7 . The discharge pump 8 is connected to the liquid phase outlet hole 33; a balance valve 12 is provided between the upper chamber 9 and the steam outlet hole 32.
该分配孔设有缩颈段的降膜蒸发装置使用时,蒸汽从加热介质进口22进入中腔10对换热管4外侧加热;料液从料液进口孔21进入上腔9,经分配孔51分配进入换热管4加热并在重力作用下成膜状沿换热管4内侧流动下降,换热管4中料液的水分被加热汽化,产生的蒸汽与液相经气液混合出口24共同进入蒸发室3进行汽液分离,液相由液相出口孔33排出,蒸汽在喷射泵15作用下从蒸气出口孔32排出经冷凝进口131进入侧围壁132中;在多级离心泵16作用下,循环水箱14中的冷却水经进水孔135、水腔133从出水孔组136进入侧围壁132中对蒸汽进行冷凝。 When the falling film evaporator with the distribution hole is equipped with a necking section, the steam enters the middle cavity 10 from the heating medium inlet 22 to heat the outside of the heat exchange tube 4; the feed liquid enters the upper cavity 9 from the feed liquid inlet hole 21, and passes through the distribution hole 51 is distributed into the heat exchange tube 4 to be heated, and under the action of gravity, it forms a film and flows down along the inner side of the heat exchange tube 4. The moisture in the feed liquid in the heat exchange tube 4 is heated and vaporized, and the generated steam and liquid phase pass through the gas-liquid mixing outlet 24 Together enter the evaporation chamber 3 for vapor-liquid separation, the liquid phase is discharged from the liquid phase outlet hole 33, and the steam is discharged from the steam outlet hole 32 under the action of the jet pump 15 and enters the side wall 132 through the condensation inlet 131; in the multi-stage centrifugal pump 16 Under the action, the cooling water in the circulating water tank 14 enters the side wall 132 from the water outlet hole group 136 through the water inlet hole 135 and the water cavity 133 to condense the steam.
该实用新型的有益效果是:该分配孔设有缩颈段的降膜蒸发装置的降膜蒸发器的分配器的分配孔具有利于成膜的缩颈段,主段与换热管内径相同,能兼顾成膜效果和均匀性及料液成膜状沿换热管内侧流动下降速度。蒸汽冷凝器结构简单,冷却效果好且循环使用冷却水节约用水。通过平衡阀可以调节上腔和蒸发室的压力的相对平衡,利于料液在重力作用下成膜状沿换热管内侧流动下降。蒸汽从蒸气出口孔排出在压缩机作用下进入中腔余热利用。进料泵利于料液进入上腔,截止阀用于控制料液进入上腔的流量;出料泵利于液相由液相出口孔排出。 The beneficial effect of this utility model is: the distribution hole of the distributor of the falling film evaporator of the falling film evaporator with the necking section provided with the distribution hole has a necking section which is beneficial to film formation, and the inner diameter of the main section is the same as that of the heat exchange tube. It can take into account the film-forming effect and uniformity as well as the film-forming liquid flowing along the inner side of the heat exchange tube and the falling speed. The structure of the steam condenser is simple, the cooling effect is good, and the cooling water is recycled to save water. The relative balance of pressure in the upper chamber and the evaporation chamber can be adjusted through the balance valve, which is beneficial for the material liquid to flow and descend in the form of a film along the inner side of the heat exchange tube under the action of gravity. The steam is discharged from the steam outlet hole and enters the middle cavity under the action of the compressor for waste heat utilization. The feed pump facilitates the feed liquid to enter the upper chamber, and the stop valve is used to control the flow of the feed liquid into the upper chamber; the discharge pump facilitates the liquid phase to be discharged from the liquid phase outlet hole.
本实用新型可改变为多种方式对本领域的技术人员是显而易见的,这样的改变不认为脱离本实用新型的范围。所有这样的对所述领域的技术人员显而易见的修改,将包括在本权利要求的范围之内。 It is obvious to those skilled in the art that the present utility model can be changed in many ways, and such changes are not considered to depart from the scope of the present utility model. All such modifications obvious to those skilled in the art are intended to be included within the scope of this claim.
Claims (4)
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Address after: 312369 Hangzhou Bay Shangyu economic and Technological Development Zone, Shaoxing, Zhejiang, Shangyu Patentee after: SHAOXING BSM CHEMICAL CO.,LTD. Address before: 312369 Hangzhou Bay Fine Chemical Industry Park, Shaoxing, Zhejiang Province, No. eleven, No. 2, Shangyu Patentee before: BSM CHEMICAL Co.,Ltd. |
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