Condensation structure
By using a dual-condenser structure and axial alignment design, the problem of poor cooling effect in traditional condensers is solved, achieving efficient heat energy utilization and cooling effect, especially improving the distillation efficiency of high-boiling-point fractions.
Patent Information
- Application Number
- CN202423318020.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-31
- Publication Date
- 2025-12-30
- Estimated Expiration
- 2034-12-31
AI Technical Summary
Traditional condensers have poor cooling performance and low thermal energy utilization during distillation, and there is room for improvement in cooling efficiency.
It adopts a dual condenser structure. The first condenser is used to preheat the solution to be distilled and precool the steam, while the second condenser is used for further cooling. The design, which combines inclined and vertical settings, utilizes gravity and heat exchange to improve the cooling effect.
It improves thermal energy utilization, enhances cooling effect and distillation efficiency, and reduces energy consumption, especially beneficial for the distillation of high-boiling-point fractions.
Smart Images
Figure CN223732138U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to condensing technical field especially relates to a condensing structure. BACKGROUND
[0002] In the distillation process, it is often necessary to use a condenser to convert gas or steam into liquid, so that the heat in the gas or steam is quickly removed.
[0003] At present, when the steam is cooled by means of the traditional condenser, the cooling effect still has room for improvement. CONTENT
[0004] The utility model provides a condensing structure to solve the problem of poor cooling effect.
[0005] The utility model provides a condensing structure, comprising:
[0006] The first condenser is formed with a heat medium inlet, a heat medium outlet and a condensate outlet on the shell, and a flow-through pipe is formed inside;
[0007] The second condenser is formed with a refrigerant inlet and a refrigerant outlet on the shell, and a reflux pipe is formed inside; one end of the reflux pipe is communicated with the heat medium outlet.
[0008] In some embodiments, the axis of the first condenser is inclined to make the condensate outlet lower than the heat medium inlet; the axis of the second condenser is vertically arranged.
[0009] In some embodiments, it further comprises:
[0010] The distillation column section is vertically arranged, the top end is communicated with the heat medium inlet, and the upper part is communicated with the condensate outlet.
[0011] In some embodiments, it further comprises:
[0012] The reflux proportion adjusting device is communicated with the condensate outlet; the reflux proportion adjusting device is communicated with the sampling outlet; the reflux proportion adjusting device is communicated with the upper part of the distillation column section.
[0013] In some embodiments, it further comprises:
[0014] The vacuum pump can be communicated with or disconnected from the other end of the reflux pipe.
[0015] In some embodiments, it further comprises:
[0016] The liquid supply pump is communicated with the flow-through pipe.
[0017] In some embodiments, the first condenser is more than one;
[0018] And / or, the second condenser is more than one.
[0019] In some embodiments, the reflux pipe is in communication with the heat medium outlet through a straight pipe or an elbow pipe.
[0020] The beneficial effects of the utility model are as follows: the condensing structure of the utility model is provided with a first condenser and a second condenser, steam generated by distillation flows into the first condenser from the heat medium inlet of the first condenser. At the same time, the to-be-distilled solution flows through the through pipe of the first condenser, the steam and the to-be-distilled solution exchange heat in the first condenser, the to-be-distilled solution is preheated, the steam is pre-cooled, the heat energy utilization rate is improved, the distillation efficiency is improved, and the cooling burden of the second condenser is reduced. Then, the pre-cooled steam that is not condensed flows through the heat medium outlet into the reflux pipe of the second condenser. Refrigerant such as freon, ammonia, water, carbon dioxide or various refrigerants flows into the second condenser from the refrigerant inlet. The refrigerant and the pre-cooled steam exchange heat in the second condenser, the steam is cooled again. In the first condenser, the liquid separated from the steam is discharged from the condensate outlet of the first condenser. In the second condenser, the liquid separated from the steam falls into the first condenser along the reflux pipe and is discharged from the condensate outlet of the first condenser. Overall, the heat energy utilization rate is effectively improved, the cooling effect and the cooling efficiency are improved. The axis of the second condenser is vertically arranged, the axis of the reflux pipe is vertically arranged, and the liquid separated from the steam falls into the first condenser along the reflux pipe. When the condensate falls in the reflux pipe of the second condenser by means of gravity, the continuously rising steam heats the falling condensate, so that the temperature of the liquid finally refluxing into the distillation column section is higher than the normal temperature, which is very beneficial to the distillation of high-boiling-point fractions and saves heating energy consumption. BRIEF DESCRIPTION OF DRAWINGS
[0021] Figure 1 The utility model relates to a kind of condensing structure some specific embodiments of structure schematic diagram.
[0022] In the drawing, 110, first condenser;111, heat medium inlet;112, heat medium outlet;113, condensate outlet;120, second condenser;121, refrigerant inlet;122, refrigerant outlet;130, distillation column section;140, reflux proportion adjusting device;150, vacuum pump;160, liquid supply pump;170, on-off valve. DETAILED DESCRIPTION
[0023] The technical solutions of the present application will be clearly and completely described below with reference to the embodiments. Obviously, the described embodiments are only some of the embodiments of the present application, but not all the embodiments. Based on the embodiments of the present application, all the other embodiments obtained by those skilled in the art without creative efforts fall within the scope of the present application.
[0024] As described in the background, in the distillation process, it is often necessary to convert gas or steam into liquid by means of a condenser, so that the heat in the gas or steam is quickly dissipated to the environment. At present, when the steam is cooled by means of a conventional condenser, the cooling effect is poor.
[0025] To solve the above problems, with reference to Figure 1 The present application provides a condensing structure, comprising a first condenser 110 and a second condenser 120. A heat medium inlet 111, a heat medium outlet 112 and a condensate outlet 113 are formed on the shell of the first condenser 110. A flow-through pipe is formed inside the first condenser 110. A coolant inlet 121 and a coolant outlet 122 are formed on the shell of the second condenser 120, and a reflux pipe is formed inside the second condenser 120. One end of the reflux pipe is in communication with the heat medium outlet 112.
[0026] The working process and principle of the condensing structure are as follows:
[0027] The steam generated by distillation flows into the first condenser 110 from the heat medium inlet 111 of the first condenser 110. At the same time, the solution to be distilled flows through the flow-through pipe of the first condenser 110. The steam and the solution to be distilled exchange heat in the first condenser 110, achieving the purpose of preheating the solution to be distilled and the purpose of precooling the steam. Both the heat energy utilization rate is improved, and the cooling burden of the second condenser 120 is reduced. Then, the pre-cooled steam flows through the heat medium outlet 112 into the reflux pipe of the second condenser 120. Refrigerants such as freon, ammonia, water, carbon dioxide, hydrocarbons or other refrigerants flow into the second condenser 120 from the coolant inlet 121. The refrigerant and the pre-cooled steam exchange heat in the second condenser 120, achieving the purpose of re-cooling the steam. In the first condenser 110, the liquid separated from the steam is discharged from the first condenser 110 through the condensate outlet 113. In the second condenser 120, the liquid separated from the steam falls into the first condenser 110 along the reflux pipe and is discharged from the first condenser 110 through the condensate outlet 113. Overall, the heat energy utilization rate is effectively improved, and the cooling effect and efficiency are improved.
[0028] Preferably, as Figure 1As shown, the axis of the first condenser 110 is arranged obliquely so that the condensate outlet 113 is lower than the heat medium inlet 111, while the axis of the second condenser 120 is arranged vertically. In this way, the axis of the reflux pipe is arranged vertically, which is more conducive to the liquid separated from the steam falling into the first condenser 110 along the reflux pipe. When the condensate falls in the reflux pipe of the second condenser 120 by gravity, the continuously rising steam heats the falling condensate, so that the liquid finally refluxing into the distillation column section 130 has a temperature higher than normal temperature, which is very conducive to the distillation of high-boiling-point fractions and saves heating energy consumption.
[0029] Specifically, in the exemplary embodiment, the condensing structure further comprises a distillation column section 130, a reflux ratio adjusting device 140, a vacuum pump 150, and a liquid supply pump 160. The axis of the distillation column section 130 is arranged vertically. The top end of the distillation column section 130 is in communication with the heat medium inlet 111, and the upper portion is in communication with the condensate outlet 113 of the first condenser 110. The distillation column section 130 is used as a steam rising channel and a condensate reflux channel. The reflux ratio adjusting device 140 is in communication with the condensate outlet 113, the sampling outlet, and the upper portion of the distillation column section 130, respectively, for adjusting the reflux flow. The vacuum pump 150 can be in communication with or disconnected from the other end of the reflux pipe. When the vacuum pump 150 is in communication with the reflux pipe, a negative pressure distillation form can be realized. When the vacuum pump 150 is disconnected from the reflux pipe, a normal pressure distillation form can be realized. The liquid supply pump 160 is in communication with the flow-through pipe of the first condenser 110, and can provide flow power for the liquid to be distilled, so that the solution to be distilled flows to the flow-through pipe of the first condenser 110.
[0030] In order to enable the vacuum pump 150 to be in communication with or disconnected from the reflux pipe, a switch valve 170 is arranged on the connecting pipeline of the vacuum pump 150 and the reflux pipe to control the opening and closing of the pipeline.
[0031] Preferably, the switch valve 170 can be an electromagnetic valve, which is conducive to improving the degree of automation. The switch valve 170 can also be a manual valve, which is convenient for manual operation.
[0032] It should be noted that the first condenser 110 is one, two, three, or more than four. And / or, the second condenser 120 is one, two, three, or more than four. More first condensers 110 and second condensers 120 can further improve the cooling effect.
[0033] In some embodiments, the reflux pipe is in communication with the heat medium outlet 112 through a straight pipe. In this way, the liquid in the reflux pipe can quickly reflux into the first condenser 110.
[0034] In other embodiments, the reflux pipe is in communication with the heat medium outlet 112 through a bent pipe. In this way, the path of the steam flowing into the second condenser 120 can be extended, and the cooling effect can be improved.
[0035] In the description of the utility model, it is understood that the orientation or positional relationship indicated by the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential" are based on the orientation or positional relationship shown in the drawings, and are only for the convenience of describing the utility model and simplifying the description, and therefore cannot be understood as indicating or implying that the devices or elements indicated must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as limiting the utility model.
[0036] In addition, the terms "first", "second" are only for the purpose of description, and cannot be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Therefore, the features defined with "first", "second" can explicitly or implicitly include at least one of the features. In the description of the utility model, the meaning of "multiple" is at least two, such as two, three, etc., unless otherwise specifically limited.
[0037] In the utility model, unless otherwise specifically defined and limited, the terms "mounting", "connection", "connection", "fixing" and other terms should be understood broadly, for example, it can be fixedly connected, or it can be detachably connected, or it can be integrated; it can be mechanically connected, or it can be electrically connected or in communication with each other; it can be directly connected, or it can be indirectly connected through an intermediate medium; it can be the internal communication of two elements or the interaction relationship between two elements, unless otherwise specifically limited. For ordinary skilled in the art, the specific meaning of the above terms in the utility model can be understood according to the specific circumstances.
[0038] In the utility model, the terms "one embodiment", "some embodiments", "example", "specific example" or "some examples" mean that the specific features, structures, materials or characteristics described in conjunction with the embodiment or example are included in at least one embodiment or example of the utility model. In the description, the illustrative description of the above terms does not necessarily refer to the same embodiment or example. Moreover, the specific features, structures, materials or characteristics described can be combined in any one or more embodiments or examples in a suitable manner. In addition, the skilled in the art can combine and combine the different embodiments or examples described in the specification and the features of different embodiments or examples without contradiction.
[0039] Although the embodiments of the utility model have been shown and described above, it can be understood that the above-mentioned embodiments are exemplary and cannot be understood as limiting the utility model, and the ordinary skilled in the art can change, modify, replace and transform the above-mentioned embodiments within the scope of the utility model.
Claims
1. A condensing structure, characterized by, Comprise: A first condenser, a heat medium inlet, a heat medium outlet and a condensate outlet are formed on the shell, and a flow-through pipe is formed inside; A second condenser, a refrigerant inlet and a refrigerant outlet are formed on the shell, and a reflux pipe is formed inside; one end of the reflux pipe is in communication with the heat medium outlet.
2. The condensing structure of claim 1, wherein The axis of the first condenser is inclined to make the condensate outlet lower than the heat medium inlet; the axis of the second condenser is vertical.
3. The condensing structure according to claim 1 or 2, characterized in that, Also comprising: A distillation column section, the axis is vertical, the top end is in communication with the heat medium inlet, and the upper part is in communication with the condensate outlet.
4. The condensing arrangement of claim 3, wherein, Also comprising: A reflux proportion adjusting device; the reflux proportion adjusting device is in communication with the condensate outlet; the reflux proportion adjusting device is in communication with the sampling outlet; the reflux proportion adjusting device is in communication with the upper part of the distillation column section.
5. The condensing structure according to claim 1 or 2, wherein Also comprising: A vacuum pump, which can be in communication or disconnected with the other end of the reflux pipe.
6. The condensing structure according to claim 1 or 2, wherein Also comprising: A liquid supply pump, which is in communication with the flow-through pipe.
7. The condensing structure according to claim 1 or 2, wherein The first condenser is more than one; And / or, the second condenser is more than one.
8. The condensing structure according to claim 1 or 2, wherein The reflux pipe is in communication with the heat medium outlet through a straight pipe or an elbow pipe.