Forced circulation evaporation equipment for heat loss control

Abstract

The utility model relates to the technical field of heat loss circulation evaporation, in particular to forced circulation evaporation equipment for heat loss control, which comprises a circulation evaporation component, the circulation evaporation component comprises a preheating tank, the preheating tank comprises a heating barrel, and the outer surface of the heating barrel is fixedly connected with a first heat preservation shell. A first heat preservation cavity is formed between the first heat preservation shell and the heating barrel and filled with heat preservation materials, the upper surface of the heating barrel is fixedly connected with a liquid conveying pipe, the other end of the liquid conveying pipe is fixedly connected with an evaporation tank, the evaporation tank is used for evaporating liquid, the surface of the evaporation tank is fixedly connected with a second heat preservation shell, and a second heat preservation cavity is formed between the second heat preservation shell and the evaporation tank. According to the forced circulation evaporation equipment for heat loss control, advanced heat preservation materials and a heat insulation technology are adopted, critical components such as the evaporator and the pipeline are subjected to elaborate heat preservation treatment, conduction and radiation of heat to the surrounding environment through the surface of the equipment are effectively reduced, and the energy utilization efficiency is greatly improved.

Description

Technical Field

[0001] This utility model relates to the field of heat loss circulating evaporation technology, and more specifically, to a forced circulating evaporation device for heat loss control. Background Technology

[0002] In many industrial production fields, such as chemical, pharmaceutical, and food processing, evaporation equipment is one of the important unit operation devices. However, traditional evaporation equipment suffers from serious heat loss problems. On the one hand, the insulation performance of the evaporator is insufficient, and heat is easily lost to the surrounding environment through the walls of the equipment. For example, some old-fashioned evaporators are only wrapped with simple insulation materials. Over time and with the operation of the equipment, the insulation materials may age or break down, leading to an increase in thermal conductivity and exacerbating heat loss. On the other hand, during the evaporation process, secondary steam carries a large amount of latent heat and is directly discharged into the atmosphere without being effectively recovered and utilized. This heat loss accounts for a large proportion of the energy consumption of the entire evaporation system.

[0003] Therefore, there is an urgent need for a forced circulation evaporation device for heat loss control to improve the shortcomings of existing technologies. Utility Model Content

[0004] The purpose of this invention is to provide a forced circulation evaporation device for heat loss control, so as to solve the problems mentioned in the background art.

[0005] To achieve the above objectives, this utility model provides a forced circulation evaporation device for heat loss control, comprising a support assembly, the support assembly including a platform, the platform being fixedly connected to a circulation evaporation assembly, the circulation evaporation assembly including a preheating tank, the heating tank including a heating barrel, the outer surface of the heating barrel being fixedly connected to an insulating shell, an insulating cavity being provided between the insulating shell and the heating barrel, the insulating cavity being filled with insulating material, a liquid delivery pipe being fixedly connected to the upper surface of the heating barrel, the other end of the liquid delivery pipe being fixedly connected to an evaporation tank, the evaporation tank being used for liquid evaporation, a second insulating shell being fixedly connected to the surface of the evaporation tank, an insulating cavity being provided between the second insulating shell and the evaporation tank, insulating cotton being fixedly connected to the outer surface of the second insulating shell, a compensation port being fixedly connected to the surface of the second insulating shell, the compensation port being connected to the insulating cavity, a steam pipe being fixedly connected to the upper surface of the evaporation tank, the other end of the steam pipe being fixedly connected to a condenser, a circulation pipe being fixedly connected to the surface of the evaporation tank, the other end of the circulation pipe being fixedly connected to a heat exchange tank.

[0006] As a further improvement to this technical solution, the platform is fixedly connected to the lower surface with a support leg, the heating barrel is fixedly connected to the lower surface with an inlet pipe, one end of the inlet pipe is fixedly connected to a feed pump, one end of the feed pump is fixedly connected to a feed pipe, a heating rod is fixedly connected inside the heating barrel, a heat source pipe is fixedly connected to the surface of the heating barrel, and the other end of the heat source pipe is fixedly connected to a condenser.

[0007] As a further improvement to this technical solution, a fixing frame is fixedly connected to the surface of the evaporator, and the fixing frame is fixedly connected to the upper surface of the platform. A bracket is fixedly connected inside the second heat-insulating shell, and the bracket is fixedly connected to the outer surface of the evaporator. A discharge pipe is fixedly connected to the surface of the evaporator, and the discharge pipe is used to connect to subsequent processing equipment.

[0008] As a further improvement to this technical solution, a hot liquid pipe is fixedly connected to the upper surface of the heat exchange tank, and the other end of the hot liquid pipe is fixedly connected to the evaporator. A forced circulation pump is fixedly connected to one end of the circulation pipe, and the forced circulation pump pumps the liquid in the evaporator into the heat exchange tank. A condensate tank is fixedly connected to the lower surface of the condenser.

[0009] Compared with the prior art, the beneficial effects of this utility model are as follows:

[0010] This forced circulation evaporation equipment for heat loss control employs advanced insulation materials and technology. Key components such as the evaporator and piping are meticulously insulated, utilizing a multi-layered composite insulation structure including high-efficiency insulation materials and a well-sealed protective layer. This effectively reduces heat conduction and radiation from the equipment surface to the surrounding environment, significantly improving energy efficiency and lowering energy costs. The equipped secondary steam latent heat recovery system efficiently recovers the latent heat from the secondary steam generated by the evaporator. The steam is condensed into liquid by the condenser, and the recovered heat is reused to preheat the feed solution or other processes requiring heating, further reducing overall system heat loss and enabling more efficient energy utilization. This offers significant economic benefits for industrial production processes where energy costs are a high percentage of total energy consumption. Attached Figure Description

[0011] Figure 1 This is a schematic diagram of the overall structure of the embodiment;

[0012] Figure 2 This is a schematic diagram of the support component structure for an embodiment;

[0013] Figure 3 This is a schematic diagram of the circulating evaporation component structure in an embodiment;

[0014] Figure 4 This is a schematic diagram of the preheating tank structure in an embodiment;

[0015] Figure 5 This is a schematic diagram of the evaporator structure in an embodiment.

[0016] The meanings of the labels in the diagram are as follows:

[0017] 1. Support components; 10. Platform; 11. Support legs;

[0018] 2. Circulating evaporation assembly; 20. Preheating tank; 200. Feed pipe; 201. Feed pump; 202. Inlet pipe; 203. Insulation shell one; 204. Heating tank; 205. Insulation cavity one; 206. Heating rod; 207. Heat source pipe; 208. Liquid delivery pipe; 21. Evaporator; 210. Insulation cavity two; 211. Insulation shell two; 212. Insulation cotton; 213. Support; 214. Compensation port; 215. Fixing frame; 216. Discharge pipe; 22. Heat exchange tank; 220. Hot liquid pipe; 221. Circulation pipe; 222. Forced circulation pump; 23. Condensate tank; 230. Condensate tank; 231. Steam pipe. Detailed Implementation

[0019] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0020] Please see Figures 1-5 As shown, this embodiment provides a forced circulation evaporation device for heat loss control, including a support assembly 1. The support assembly 1 includes a platform 10, and a circulation evaporation assembly 2 is fixedly connected to the platform 10. The circulation evaporation assembly 2 includes a preheating tank 20, and the preheating tank includes a heating barrel 204. An insulation shell 203 is fixedly connected to the outer surface of the heating barrel 204. An insulation cavity 205 is provided between the insulation shell 203 and the heating barrel 204, and the insulation cavity 205 is filled with insulation material. A liquid delivery pipe 208 is fixedly connected to the upper surface of the heating barrel 204, and the other end of the liquid delivery pipe 208 is fixedly connected to an evaporation device. Evaporator 21 is used for the evaporation of liquid. An insulating outer shell 211 is fixedly connected to the surface of evaporator 21. An insulating cavity 210 is provided between the insulating outer shell 211 and evaporator 21. Insulating cotton 212 is fixedly connected to the outer surface of the insulating outer shell. An expansion joint 214 is fixedly connected to the surface of the outer shell 214, which is connected to the insulating cavity. A steam pipe 231 is fixedly connected to the upper surface of evaporator 21. A condenser 23 is fixedly connected to the other end of the steam pipe 231. A circulation pipe 221 is fixedly connected to the surface of evaporator 21. A heat exchanger 22 is fixedly connected to the other end of the circulation pipe 221.

[0021] The above working principle is as follows: First, the raw material liquid enters the heating tank 204 of the preheating tank 20 through an external pipe. The insulation shell 203 outside the heating tank 204 and the insulation material filled inside effectively reduce heat loss and preheat the liquid. Then, the preheated liquid flows into the evaporator 21 through the liquid delivery pipe 208. The insulation shell 211 on the surface of the evaporator 21, the insulation cotton 212, the insulation cavity 210, and the compensation port 214 further enhance the insulation effect and reduce heat loss. In the evaporator 21, the liquid evaporates due to heat, and the generated steam enters the condenser 23 through the steam pipe 231 for condensation and recovery. Meanwhile, the unevaporated liquid in the evaporator 21 enters the heat exchange tank 22 through the circulation pipe 221. After exchanging heat with other media, the temperature changes, and the liquid is then circulated back into the evaporator 21 to continue participating in the evaporation process. This cycle repeats continuously. By using efficient heat preservation measures to reduce heat loss and utilizing the circulation mechanism to continuously evaporate and concentrate the liquid, heat loss can be effectively controlled and the evaporation operation can be carried out continuously and stably, thereby improving energy utilization efficiency and meeting the evaporation needs in the production process.

[0022] To preheat the feed material, in this embodiment, a support leg 11 is fixedly connected to the lower surface of the platform 10, and an inlet pipe 202 is fixedly connected to the lower surface of the heating tank 204. A feed pump 201 is fixedly connected to one end of the inlet pipe 202, and a feed pipe 200 is fixedly connected to the other end of the feed pump 201. A heating rod 206 is fixedly connected inside the heating tank 204, and a heat source pipe 207 is fixedly connected to the surface of the heating tank 204. The other end of the heat source pipe 207 is fixedly connected to the condenser tank 23. When the equipment is started, the feed pump 201 begins to work, drawing in the raw material through the feed pipe 200. The raw material then enters the heating tank 204 through the inlet pipe 202. The heating rod 206 inside the heating tank 204 generates heat when energized, directly heating the raw material inside the tank. Simultaneously, a heat source with a certain amount of heat from the condenser tank 23 is introduced around the heating tank 204 through the heat source pipe 207, working together with the heating rod 206 to preheat the raw material to a certain temperature before it enters the evaporator tank 21. This preheating method not only utilizes the waste heat generated by the equipment itself, improving energy efficiency, but also enables the raw materials to reach the required evaporation temperature more quickly after entering the evaporator 21, accelerating the evaporation process and reducing the energy consumed by relying solely on external heating in the evaporator 21. Thus, the rational distribution and efficient utilization of heat are achieved at the beginning of the entire evaporation process, laying the foundation for subsequent stable evaporation operations.

[0023] To minimize heat loss, in this embodiment, a fixing frame 215 is fixedly connected to the surface of the evaporator 21, and the fixing frame 215 is fixedly connected to the upper surface of the platform 10. A support 213 is fixedly connected inside the insulation shell 211, and the support 213 is fixedly connected to the outer surface of the evaporator 21. A discharge pipe 216 is fixedly connected to the surface of the evaporator 21, and the discharge pipe 216 is used to connect to subsequent processing equipment. The support 213 inside the insulation shell 211 further strengthens the support and fixation of the evaporator 21, while also reducing the direct contact area between the evaporator 21 and the external environment. The insulation shell 211 and its internal insulation material form an effective heat insulation barrier, greatly reducing the conduction of heat from the inside of the evaporator 21 to the external environment. When the liquid in the evaporator 21 evaporates, the generated heat is retained within the tank as much as possible, reducing energy waste caused by heat loss. When the discharge pipe 216 of the evaporator 21 is connected to the subsequent processing equipment, corresponding heat preservation measures are also taken to ensure that heat is not lost in large quantities during the discharge process, thereby ensuring the thermal efficiency of the entire evaporation process. This allows the equipment to maintain efficient evaporation operation with low energy consumption during operation, reducing production costs and improving economic benefits.

[0024] To fully utilize heat, in this embodiment, a hot liquid pipe 220 is fixedly connected to the upper surface of the heat exchange tank 22, and the other end of the hot liquid pipe 220 is fixedly connected to the evaporator 21. A forced circulation pump 222 is fixedly connected to one end of the circulation pipe 221, which pumps the liquid in the evaporator 21 into the heat exchange tank 22. A condensate tank 230 is fixedly connected to the lower surface of the condenser 23. The hot liquid pipe 220 in the heat exchange tank 22 transports the heated liquid in the tank back to the evaporator 21 after heat exchange, providing additional heat to the liquid in the evaporator 21 to replenish the heat lost during evaporation, ensuring that the liquid in the evaporator 21 can be continuously maintained in a temperature range conducive to evaporation, further improving evaporation efficiency. The forced circulation pump 222 at one end of the circulation pipe 221 powerfully drives the unevaporated liquid in the evaporator 21 into the heat exchange tank 22. In the heat exchange tank 22, the liquid undergoes sufficient heat exchange with other media at suitable temperatures, absorbing heat before circulating back to the evaporator 21 to continue evaporation. The condensate tank 230 below the condensate tank 23 collects the condensate generated during the condensation process, preventing the condensate from being discharged indiscriminately and causing heat waste.

[0025] In this embodiment, a forced circulation evaporation device for heat loss control is used in the following way: First, after the device is started, the feed pump 201 begins operation, drawing in the raw material through the feed pipe 200. The raw material then enters the heating tank 204 through the inlet pipe 202. The heating rod 206 inside the heating tank 204 generates heat after being energized, directly heating the raw material inside the tank. Simultaneously, a heat source with a certain amount of heat in the condenser 23 is introduced around the heating tank 204 through the heat source pipe 207, working together with the heating rod 206 to preheat the raw material to a certain temperature before it enters the evaporator 21. The insulation shell 203 outside the heating tank 204 and the insulation material inside effectively reduce heat loss, providing initial preheating of the liquid. Afterward, the preheated liquid flows into the evaporator 21 through the liquid delivery pipe 208. The support 213 inside the insulation shell 211 further strengthens the support and fixation of the evaporator 21, while also reducing the direct contact area between the evaporator 21 and the external environment. The insulating outer shell 211 and its internal insulation material form an effective heat insulation barrier, greatly reducing the conduction of heat from the inside of the evaporator 21 to the external environment. When the liquid in the evaporator 21 evaporates, the generated heat is retained in the tank as much as possible, reducing energy waste caused by heat loss. When the discharge pipe 216 of the evaporator 21 is connected to the subsequent processing equipment, corresponding insulation measures are also taken to ensure that heat is not lost in large quantities during the discharge process, thereby ensuring the thermal efficiency of the entire evaporation process. This allows the equipment to maintain efficient evaporation operation with low energy consumption during operation, reducing production costs and improving economic benefits. The unevaporated liquid in the evaporator 21 enters the heat exchange tank 22 through the circulation pipe 221. After exchanging heat with other media, the temperature changes, and it is then circulated back to the evaporator 21 to continue participating in the evaporation process. The forced circulation pump 222 at one end of the circulation pipe 221 strongly drives the unevaporated liquid in the evaporator 21 into the heat exchange tank 22. In the heat exchange tank 22, the liquid undergoes sufficient heat exchange with other media with suitable temperatures, absorbs heat, and is then circulated back to the evaporator 21 to continue evaporation. The condensate tank 230 below the condenser 23 collects the condensate generated during the condensation process, preventing the condensate from being discharged indiscriminately and causing heat waste. This cycle repeats continuously, reducing heat loss through efficient insulation measures and using the circulation mechanism to continuously evaporate and concentrate the liquid, thereby achieving effective control of heat loss and continuous and stable evaporation operation, improving energy efficiency and meeting the evaporation needs in the production process.

[0026] The foregoing has shown and described the basic principles, main features, and advantages of this utility model. Those skilled in the art should understand that this utility model is not limited to the above embodiments. The embodiments and descriptions in the specification are merely preferred examples and are not intended to limit the utility model. Various changes and modifications can be made to this utility model without departing from its spirit and scope, and all such changes and modifications fall within the scope of the claimed utility model. The scope of protection of this utility model is defined by the appended claims and their equivalents.

Claims

1. A forced circulation evaporation apparatus for heat loss control comprising a support assembly (1) characterized by: The support assembly (1) includes a platform (10), to which a circulating evaporation assembly (2) is fixedly connected. The circulating evaporation assembly (2) includes a preheating tank (20), which includes a heating barrel (204). An insulating outer shell (203) is fixedly connected to the outer surface of the heating barrel (204). An insulating cavity (205) is provided between the insulating outer shell (203) and the heating barrel (204). The insulating cavity (205) is filled with insulating material. An infusion pipe (208) is fixedly connected to the upper surface of the heating barrel (204). An evaporation tank (21) is fixedly connected to the other end of the infusion pipe (208). The evaporation tank (21) is used for liquid... Evaporation, the surface of the evaporator (21) is fixedly connected to the heat insulation shell II (211), the heat insulation shell II (211) and the evaporator (21) are provided with the heat insulation cavity II (210), the outer surface of the heat insulation shell is fixedly connected to the heat insulation cotton (212), the surface of the heat insulation shell II is fixedly connected to the compensation port (214), the compensation port (214) is connected to the heat insulation cavity, the upper surface of the evaporator (21) is fixedly connected to the steam pipe (231), the other end of the steam pipe (231) is fixedly connected to the condenser (23), the surface of the evaporator (21) is fixedly connected to the circulation pipe (221), the other end of the circulation pipe (221) is fixedly connected to the heat exchange tank (22).

2. The forced circulation evaporation apparatus for thermal damage control according to claim 1, characterized by: The platform (10) is fixedly connected to the lower surface of the support leg (11), the heating barrel (204) is fixedly connected to the lower surface of the inlet pipe (202), one end of the inlet pipe (202) is fixedly connected to the feed pump (201), one end of the feed pump (201) is fixedly connected to the feed pipe (200), the heating barrel (204) is fixedly connected to the inside of the heating barrel (204), the heating barrel (204) is fixedly connected to the surface of the heating barrel (204) and the other end of the heat source pipe (207) is fixedly connected to the condenser (23).

3. The forced circulation evaporation apparatus for thermal damage control of claim 1, wherein: A fixing frame (215) is fixedly connected to the surface of the evaporator (21), and the fixing frame (215) is fixedly connected to the upper surface of the platform (10). A bracket (213) is fixedly connected inside the second heat-insulating shell (211), and the bracket (213) is fixedly connected to the outer surface of the evaporator (21). A discharge pipe (216) is fixedly connected to the surface of the evaporator (21), and the discharge pipe (216) is used to connect to subsequent processing equipment.

4. The forced circulation evaporation apparatus for thermal damage control of claim 1, wherein: A hot liquid pipe (220) is fixedly connected to the upper surface of the heat exchange tank (22), and the other end of the hot liquid pipe (220) is fixedly connected to the evaporator (21). A forced circulation pump (222) is fixedly connected to one end of the circulation pipe (221), and the forced circulation pump (222) pumps the liquid in the evaporator (21) into the heat exchange tank (22). A condensate tank (230) is fixedly connected to the lower surface of the condenser (23).

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