Horizontal hot-pressing distilled water device

Abstract

The utility model relates to the technical field of injection water treatment, in particular to a horizontal hot-pressing distilled water device. The horizontal hot-pressing distilled water device comprises a raw water pipeline, a preheating module, a horizontal evaporator, a liquid outlet pipe section, an industrial steam conveying pipeline, an industrial steam condensing pipeline and a storage container, the industrial steam conveying pipeline is used for conveying industrial steam to supply heat to raw water in the evaporation chamber, and the industrial steam condensing pipeline is used for discharging industrial steam condensed water after the industrial steam is condensed; the industrial steam conveying pipeline and the raw water pipeline are subjected to heat exchange through the first heat exchanger so as to preheat raw water; the industrial steam condensation pipeline and the raw water pipeline are subjected to heat exchange through the second heat exchanger so as to preheat the raw water. In the working process, raw water can be preheated through industrial steam condensate water in the second heat exchanger and the industrial steam condensation pipeline, heat energy is fully utilized, the energy consumption needed for preheating the raw water is reduced, and the energy consumption needed for treating the raw water is reduced.

Description

TECHNICAL FIELD

[0001] The utility model relates to the technical field of water for injection processing, especially to a horizontal hot pressure distilled water device. BACKGROUND

[0002] Water for injection is a special type of water, mainly used in the pharmaceutical and medical fields, especially when preparing injections and sterile drugs.

[0003] The quality of water for injection is directly related to the safety and effectiveness of drugs, and water for injection is generally obtained by processing raw water.

[0004] The existing water for injection production device needs to preheat the raw water first, then evaporate the raw water into pure steam, and finally condense the pure steam into distilled water, which consumes a lot of energy in the whole process. UTILITY MODEL CONTENTS

[0005] The utility model aims at providing a horizontal hot pressure distilled water device to reduce the energy consumption required for processing raw water.

[0006] To solve the above technical problems, the utility model provides a horizontal hot pressure distilled water device.

[0007] The horizontal hot pressure distilled water device of the utility model, including raw water pipeline, preheating module, horizontal evaporator, liquid outlet pipe section, industrial steam conveying pipeline, industrial steam condensing pipeline and storage container;

[0008] The raw water pipeline is connected with the horizontal evaporator to supply raw water to the horizontal evaporator;

[0009] The horizontal evaporator includes a shell and an atomizing nozzle assembly, the shell is provided with an evaporation chamber and a condensation chamber, the evaporation chamber is provided with an evaporation tube bundle, the outer wall surface of the evaporation tube bundle forms an evaporation surface, and the atomizing nozzle assembly is used for atomizing the raw water in the evaporation tube bundle and spraying it to the evaporation surface;

[0010] The evaporation chamber is used for containing raw water, the inner cavity of the evaporation tube bundle forms the condensation chamber, and the condensation chamber is used for introducing pure steam to condense the pure steam into distilled water while heating the raw water;

[0011] The industrial steam conveying pipeline is used for conveying industrial steam to heat the raw water in the evaporation chamber, and the industrial steam condensing pipeline is used for discharging industrial steam condensate after the industrial steam is condensed;

[0012] The preheating module includes a first heat exchanger and a second heat exchanger. The industrial steam delivery pipeline and the raw water pipeline perform heat exchange through the first heat exchanger to preheat the raw water. The industrial steam condensation pipeline and the raw water pipeline perform heat exchange through the second heat exchanger to preheat the raw water.

[0013] The liquid outlet pipe section is used to guide the distilled water into the storage container.

[0014] Furthermore, the industrial steam transmission pipeline includes a first industrial steam branch and a second industrial steam branch. The first industrial steam branch and the raw water pipeline perform heat exchange with the first heat exchanger to preheat the raw water. The second industrial steam branch is used to transport industrial steam to supply heat to the raw water in the evaporation chamber.

[0015] Furthermore, the industrial steam condensation pipeline includes a first industrial steam condensation branch and a second industrial steam condensation branch, the first industrial steam condensation branch is connected to the first industrial steam branch, and the second industrial steam condensation branch is connected to the second industrial steam condensation branch.

[0016] Furthermore, a demister is provided in the evaporation chamber, and the demister is used to demist the pure steam.

[0017] Furthermore, it also includes a concentrated water discharge pipeline, which is connected to the bottom of the evaporation chamber to regularly discharge the concentrated raw water in the evaporation chamber.

[0018] Furthermore, the preheating module further includes a third heat exchanger, and the concentrated water discharge pipeline and the raw water pipeline perform heat exchange through the second heat exchanger to preheat the raw water.

[0019] Furthermore, it also includes a non-condensable gas removal device, the liquid outlet pipe section flows through the non-condensable gas removal device, and the non-condensable gas removal device is used to remove non-condensable gases in distilled water.

[0020] Furthermore, the liquid outlet pipe section includes a first liquid outlet pipe section, a second liquid outlet pipe section and a third liquid outlet pipe section, the first liquid outlet pipe section is used to introduce the distilled water in the condensation chamber into the non-condensable gas removal device, the second liquid outlet pipe section introduces the degassed distilled water in the non-condensable gas removal device into the storage container, the third liquid outlet pipe section is used to connect the first liquid outlet pipe section and the non-condensable gas removal device, and a control valve is provided on the third liquid outlet pipe section.

[0021] Further, a vapor compression pipeline and a compressor are also included, the compressor is arranged on the vapor compression pipeline, the vapor compression pipeline has an air inlet end and an air outlet end, the air inlet end is communicated with the evaporation chamber, the air outlet end is communicated with the condensation chamber, the vapor compression pipeline is used for introducing pure steam in the evaporation chamber into the condensation chamber, and the compressor is used for compressing the pure steam in the vapor compression pipeline.

[0022] Compared with the prior art, the utility model has at least the following beneficial effects:

[0023] When the horizontal heat pressure distillation water device is used to produce distilled water, raw water is supplied to the horizontal evaporator through the raw water pipeline, in this process, the industrial steam conveying pipeline preheats the raw water in the raw water pipeline through the first heat exchanger, the industrial steam in the industrial steam conveying pipeline is condensed into industrial steam condensate after releasing heat, the industrial steam condensate enters the industrial steam condensing pipeline, because the industrial steam condensate has a certain temperature, therefore, the industrial steam condensate in the industrial steam condensing pipeline can also preheat the raw water through the second heat exchanger, so that the heat energy is fully utilized, the energy consumption required for preheating the raw water is reduced, and the energy consumption required for treating the raw water is reduced as a whole. BRIEF DESCRIPTION OF DRAWINGS

[0024] Figure 1 It is a structure schematic view of one embodiment of the horizontal heat pressure distillation water device.

[0025] Reference signs:

[0026] 11, first raw water pipeline section; 12, second raw water pipeline section; 13, third raw water pipeline section;

[0027] 21, first heat exchanger; 22, second heat exchanger; 23, third heat exchanger; 24, fourth heat exchanger; 25, fifth heat exchanger;

[0028] 30, horizontal evaporator; 31, water spraying pipe; 32, atomizing nozzle; 33, raw water collecting tank; 34, heat supplementing tank; 35, demister;

[0029] 41, first liquid outlet pipe section; 42, second liquid outlet pipe section; 43, third liquid outlet pipe section;

[0030] 51, industrial steam conveying main line; 52, first industrial steam branch line; 53, second industrial steam branch line;

[0031] 61, industrial steam condensing main line; 62, first industrial steam condensing branch line; 63, second industrial steam condensing branch line;

[0032] 70, concentrated water discharge pipeline;

[0033] 81, vapor compression circuit; 82, compressor;

[0034] 90, non-condensable gas removal device; 91, vent line; 92, exhaust line. DETAILED DESCRIPTION

[0035] The horizontal hot-press distillation water device of the present application will be described below in conjunction with the accompanying drawings, wherein the preferred embodiments of the present application are shown, it should be understood that the present application described herein can be modified by those skilled in the art, while still achieving the advantageous effects of the present application. Therefore, the following description should be understood as a broad knowledge for those skilled in the art, rather than as a limitation of the present application.

[0036] The serial numbers of components in this paper, such as "first", "second", etc., are only used to distinguish the described objects, and do not have any order or technical meaning. The "connection" and "coupling" in this application include direct and indirect connection (coupling) unless otherwise specified. In the description of the present application, it should be understood that the orientation or position relationship indicated by the terms "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise" and the like are based on the orientation or position relationship shown in the drawings, and are only for the convenience of describing the present application and simplifying the description, and therefore cannot be understood as indicating or implying that the devices or elements referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as limiting the present application.

[0037] In the present application, unless otherwise explicitly specified and limited, the first feature "on" or "under" the second feature can be that the first and second features are in direct contact, or the first and second features are in indirect contact through an intermediate medium. Moreover, the first feature "above", "above" and "above" the second feature can be that the first feature is directly above or obliquely above the second feature, or only indicates that the horizontal height of the first feature is higher than that of the second feature. The first feature "below", "below" and "below" the second feature can be that the first feature is directly below or obliquely below the second feature, or only indicates that the horizontal height of the first feature is less than that of the second feature.

[0038] The present application will be described in more detail in the following paragraphs with reference to the accompanying drawings. The advantages and features of the present application will be more apparent according to the following description and claims. It should be noted that the drawings are very simplified and use non-precise proportions, only for the purpose of facilitating and clarifying the purpose of assisting the description of the embodiments of the present application.

[0039] The horizontal hot-press distillation water device of the present application will be described below in conjunction with the accompanying drawings, wherein the preferred embodiments of the present application are shown, it should be understood that the present application described herein can be modified by those skilled in the art, while still achieving the advantageous effects of the present application. Therefore, the following description should be understood as a broad knowledge for those skilled in the art, rather than as a limitation of the present application. Figure 1 The horizontal hot-press distillation water device of the present application will be described below in conjunction with the accompanying drawings, wherein the preferred embodiments of the present application are shown, it should be understood that the present application described herein can be modified by those skilled in the art, while still achieving the advantageous effects of the present application. Therefore, the following description should be understood as a broad knowledge for those skilled in the art, rather than as a limitation of the present application.

[0040] like Figure 1 As shown, the horizontal hot-pressed distilled water device of this embodiment includes a raw water pipeline, a preheating module, a horizontal evaporator 30, a liquid outlet pipe section, an industrial steam delivery pipeline, an industrial steam condensation pipeline and a storage container.

[0041] The raw water pipeline is connected to the horizontal evaporator 30 to supply raw water to the horizontal evaporator 30 .

[0042] The horizontal evaporator 30 comprises a housing and an atomizing nozzle assembly 32. The housing houses an evaporation chamber and a condensation chamber. The evaporation chamber houses an evaporation tube bundle, the outer wall of which forms an evaporation surface. The atomizing nozzle assembly 32 is used to atomize raw water in the evaporation tube bundle and spray it onto the evaporation surface. The atomizing nozzle assembly 32 includes a water spray pipe 31 and multiple atomizing nozzles 32 connected to the water spray pipe 31. The number and position of the atomizing nozzles 32 can be appropriately adjusted based on the size of the steam chamber.

[0043] The evaporation chamber is used to accommodate raw water. The inner cavity of the evaporation tube bundle forms the condensation chamber. The condensation chamber is used to allow pure steam to pass through so as to heat the raw water and condense the pure steam into distilled water.

[0044] The industrial steam delivery pipeline is used to deliver industrial steam to supply heat to the raw water in the evaporation chamber, and the industrial steam condensation pipeline is used to discharge industrial steam condensate after the industrial steam is condensed.

[0045] The preheating module includes a first heat exchanger 21 and a second heat exchanger 22. The industrial steam delivery pipeline and the raw water pipeline perform heat exchange through the first heat exchanger 21 to preheat the raw water; the industrial steam condensation pipeline and the raw water pipeline perform heat exchange through the second heat exchanger 22 to preheat the raw water.

[0046] The liquid outlet pipe section is used to guide the distilled water into the storage container.

[0047] When using the horizontal hot-pressed distilled water device of the present invention to produce distilled water, the raw water pipeline is first used to supply raw water to the horizontal evaporator 30. In this project, the industrial steam delivery pipeline preheats the raw water in the raw water pipeline through the first heat exchanger 21. The industrial steam in the industrial steam delivery pipeline condenses into industrial steam condensate after releasing heat, and the industrial steam condensate enters the industrial steam condensate pipeline. Since the industrial steam condensate itself still has a certain temperature, the industrial steam condensate in the industrial steam condensate pipeline can also preheat the raw water using the second heat exchanger 22, thereby making full use of thermal energy and reducing the energy consumption required for preheating the raw water, thereby reducing the energy consumption required for treating the raw water as a whole.

[0048] In one embodiment, in order to accelerate the evaporation of raw water in the evaporation chamber, the industrial steam transportation pipeline includes an industrial steam transportation main line 51 and a first industrial steam branch 52 and a second industrial steam branch 53. The industrial steam in the industrial steam transportation main line 51 is diverted into the first industrial steam branch 52 and the second industrial steam branch 53 respectively. The first industrial steam branch 52 and the raw water pipeline perform heat exchange through the first heat exchanger 21 to preheat the raw water. The second industrial steam branch 53 is used to transport industrial steam to supply heat to the raw water in the evaporation chamber.

[0049] Since industrial steam will cool into condensed water after releasing heat, in order to transport industrial steam condensed water, the industrial steam condensation pipeline includes an industrial steam condensation main line 61, a first industrial steam condensation branch 62 and a second industrial steam condensation branch 63. The first industrial steam condensation branch 62 is connected to the first industrial steam branch 52, and the second industrial steam condensation branch 63 is connected to the second industrial steam condensation branch 63. The condensed water of the two branches converges into the industrial steam condensation main line 61 and is finally discharged.

[0050] The industrial steam transmission main line 51 and the raw water pipeline perform heat exchange with each other through the first heat exchanger 21 to preheat the raw water; the industrial steam condensation main line 61 and the raw water pipeline perform heat exchange with each other through the second heat exchanger 22 to preheat the raw water.

[0051] To improve the purity of the pure steam and remove any water droplets or mist droplets that may be present in the pure steam, the pure steam is defogged before entering the condensation chamber. In one embodiment, a demister 35 is provided in the evaporation chamber to defog the pure steam. The demister 35 is positioned near the exit of the evaporation chamber. The pure steam passes through the demister 35 before leaving the evaporation chamber. During this process, any water droplets or mist droplets, as well as endotoxins, that may be present in the pure steam are removed by the demister 35, ensuring that the purity of the pure steam meets the required standards.

[0052] In one embodiment, the horizontal hot-pressed water distillation device further includes a concentrated water discharge pipeline 70, which is connected to the evaporation chamber to periodically discharge concentrated raw water from the evaporation chamber. Specifically, the raw water pipeline includes a first raw water pipeline section 11, a second raw water pipeline section 12, and a third raw water pipeline section 13. The first raw water pipeline section 11 introduces raw water into the evaporation chamber. A raw water collection tank 33 and a supplemental heat tank 34 are provided at the bottom of the evaporation chamber, both of which are connected to the evaporation chamber. The raw water collection tank 33 and the supplemental heat tank 34 are connected via the second raw water pipeline section 12. The raw water collection tank 33 and the water spray pipe 31 are connected via the third raw water pipeline section 13. A water pump is provided on the third raw water pipeline section 13, and the third raw water pipeline can use the water pump to introduce raw water from the raw water collection tank 33 into the water spray pipe 31. The second industrial steam branch 53 is connected to the supplementary heat tank 34 . After the raw water in the evaporation chamber enters the supplementary heat tank 34 , the second industrial steam branch 53 can exchange heat with the raw water in the supplementary heat tank 34 .

[0053] As the raw water in the evaporation chamber continues to evaporate, the concentration of impurities in the raw water will continue to increase. Therefore, in order to avoid the raw water being contaminated by the impurities in the raw water due to excessive concentration, a concentrated water discharge pipeline 70 is provided to regularly discharge the concentrated raw water in the raw water collection tank 33. The discharge cycle can be set according to factors such as the water quality index of the concentrated water and specific needs.

[0054] Furthermore, since the concentrated water has a relatively high temperature and high thermal energy, in order to fully utilize the thermal energy in the concentrated water, the preheating module also includes a third heat exchanger 23. The concentrated water discharge pipeline 70 and the raw water pipeline perform heat exchange through the third heat exchanger 23 to preheat the raw water.

[0055] Specifically, the concentrated water discharge pipeline 70 is in communication with the third raw water pipeline to discharge concentrated water. The concentrated water discharge pipeline 70 and the third raw water pipeline perform heat exchange with each other through the third heat exchanger 23 to preheat the raw water.

[0056] During the condensation process of pure steam into distilled water, gases that cannot condense into water may be mixed in. These gases are called non-condensable gases. Non-condensable gases include air, inert gases, or other impurity gases. These non-condensable gases may affect the acidity or alkalinity of the water or carry microorganisms, resulting in substandard water for injection. Therefore, it is necessary to remove the non-condensable gases to ensure the purity of the distilled water. In one embodiment, the horizontal hot-pressed water distillation device also includes a non-condensable gas removal device 90, through which the liquid outlet pipe section flows. The non-condensable gas removal device 90 is used to remove non-condensable gases from the distilled water.

[0057] Specifically, the liquid outlet pipe includes a first liquid outlet pipe section 41 and a second liquid outlet pipe section 42. The first liquid outlet pipe section 41 is used to introduce the distilled water in the condensation chamber into the non-condensable gas removal device 90, and the second liquid outlet pipe section 42 introduces the degassed distilled water in the non-condensable gas removal device 90 into the storage container. Preferably, the first liquid outlet pipe section 41 is a U-shaped pipe, and a third liquid outlet pipe section 43 is connected between the U-shaped pipe and the non-condensable gas removal device 90. A control valve is provided on the third liquid outlet pipe section 43. During continuous operation, the third liquid outlet pipe section 43 is closed. When the operation is completed, the third liquid outlet pipe section 43 is opened to introduce the distilled water remaining in the first liquid outlet pipe section 41 into the non-condensable gas removal device 90 to avoid liquid residue.

[0058] In order to discharge the non-condensable gas and balance the pressure in the non-condensable gas device, a ventilation pipeline 91 and an exhaust pipeline 92 are provided between the evaporator and the non-condensable gas removal device 90 .

[0059] Specifically, in order to discharge non-condensable gases, the injection water production device further includes a non-condensable gas discharge pipeline, and the evaporator is connected to the non-condensable gas discharge pipeline to discharge the non-condensable gases.

[0060] In one embodiment, to cool the condensed distilled water and fully utilize the thermal energy of the distilled water, the preheating module further includes a fourth heat exchanger 24. The liquid outlet pipe section and the raw water pipeline perform heat exchange through the fourth heat exchanger 24 to preheat the raw water. Specifically, the second liquid outlet pipe section 42 and the raw water pipeline perform heat exchange through the fourth heat exchanger 24 to preheat the raw water.

[0061] In addition, a fifth heat exchanger 25 is provided in the horizontal evaporator 30 , and the fifth heat exchanger uses non-condensable gas to preheat the raw water.

[0062] During the entire processing process of this embodiment, according to the flow route of the raw water, the second heat exchanger 22 first performs the primary preheating of the raw water using industrial steam condensate, and then the third heat exchanger 23 performs the secondary preheating of the raw water using concentrated water. Then, the fourth heat exchanger 24 performs the tertiary preheating of the raw water using distilled water. Subsequently, the first heat exchanger 21 performs the quaternary heating of the raw water using industrial steam to heat the raw water to no less than 90°C. The raw water continues to flow into the horizontal evaporator 30, and the fifth heat exchanger 25 performs the quintuple preheating of the raw water using non-condensable gas. The raw water enters the supplementary heat tank 34 and is heated six times by industrial steam.

[0063] In other embodiments, the preheating or heating sequence of different heat exchangers may be flexibly adjusted according to the specific arrangement of the pipelines.

[0064] Through the above-mentioned multi-stage preheating and heating process, not only can the energy utilization rate be improved, but the raw water can also be preheated to a higher temperature before entering the heat exchanger, so that it can evaporate into pure steam more quickly after entering the heat exchanger, thereby improving the pure steam generation efficiency.

[0065] In order to reduce energy consumption and improve energy utilization, in one embodiment, the injection water production device also includes a steam compression pipeline 81 and a compressor 82. The compressor 82 is arranged on the steam compression pipeline 81. The steam compression pipeline 81 has an air inlet end and an air outlet end. The air inlet end is connected to the evaporation chamber, and the air outlet end is connected to the condensation chamber. The steam compression pipeline 81 is used to introduce pure steam in the evaporation chamber into the condensation chamber, and the compressor 82 is used to compress the pure steam in the steam compression pipeline 81.

[0066] Compressing pure steam increases its internal energy. This allows the pure steam to transfer more heat to the raw water when it exchanges heat with the raw water through the evaporation surface, improving evaporation efficiency. This also reduces the demand for industrial steam. Compared to the energy utilization of generating industrial steam, compressor 82 has a higher energy utilization rate, which helps reduce energy consumption and facilitates the condensation of pure steam into distilled water.

[0067] Obviously, those skilled in the art may make various modifications and variations to the present invention without departing from the spirit and scope of the present invention. Thus, if such modifications and variations fall within the scope of the claims of the present invention and their equivalents, the present invention is intended to include such modifications and variations.

Claims

1. A horizontal hot-pressed distilled water device, characterized in that: It includes raw water pipeline, preheating module, horizontal evaporator, liquid outlet pipe section, industrial steam transmission pipeline, industrial steam condensation pipeline and storage container; The raw water pipeline is connected to the horizontal evaporator to supply raw water to the horizontal evaporator; The horizontal evaporator includes a shell and an atomizing nozzle assembly. The shell is provided with an evaporation chamber and a condensation chamber. The evaporation chamber is provided with an evaporation tube bundle. The outer wall surface of the evaporation tube bundle forms an evaporation surface. The atomizing nozzle assembly is used to atomize the raw water in the evaporation tube bundle and spray it onto the evaporation surface. The evaporation chamber is used to contain raw water, the inner cavity of the evaporation tube bundle forms the condensation chamber, and the condensation chamber is used to pass pure steam to heat the raw water and condense the pure steam into distilled water. The industrial steam delivery pipeline is used to deliver industrial steam to provide heat to the raw water in the evaporation chamber, and the industrial steam condensation pipeline is used to discharge industrial steam condensate after the industrial steam is condensed; The preheating module includes a first heat exchanger and a second heat exchanger. The industrial steam delivery pipeline and the raw water pipeline perform heat exchange through the first heat exchanger to preheat the raw water. The industrial steam condensation pipeline and the raw water pipeline perform heat exchange through the second heat exchanger to preheat the raw water. The liquid outlet pipe section is used to guide the distilled water into the storage container.

2. The horizontal hot-pressed distilled water device according to claim 1, characterized in that: The industrial steam transmission pipeline includes a first industrial steam branch and a second industrial steam branch. The first industrial steam branch and the raw water pipeline perform heat exchange with each other through the first heat exchanger to preheat the raw water. The second industrial steam branch is used to transport industrial steam to supply heat to the raw water in the evaporation chamber.

3. The horizontal hot-pressed distilled water device according to claim 2, characterized in that: The industrial steam condensation pipeline includes a first industrial steam condensation branch and a second industrial steam condensation branch, the first industrial steam condensation branch is connected to the first industrial steam branch, and the second industrial steam condensation branch is connected to the second industrial steam condensation branch.

4. The horizontal hot-pressed distilled water device according to claim 1, characterized in that: A demister is provided in the evaporation chamber, and the demister is used to demist the pure steam.

5. The horizontal hot-pressed distilled water device according to claim 1, characterized in that: The device further comprises a concentrated water discharge pipeline, which is communicated with the bottom of the evaporation chamber to regularly discharge the concentrated raw water in the evaporation chamber.

6. The horizontal hot-pressed distilled water device according to claim 5, characterized in that: The preheating module further includes a third heat exchanger, and the concentrated water discharge pipeline and the raw water pipeline perform heat exchange through the second heat exchanger to preheat the raw water.

7. The horizontal hot-pressed distilled water device according to claim 1, characterized in that: The preheating module further includes a fourth heat exchanger, and the liquid outlet pipe section and the raw water pipeline perform heat exchange through the fourth heat exchanger to preheat the raw water.

8. The horizontal hot-pressed distilled water device according to claim 1, characterized in that: It also includes a non-condensable gas removal device, through which the liquid outlet pipe section flows, and the non-condensable gas removal device is used to remove non-condensable gases in distilled water.

9. The horizontal hot-pressed distilled water device according to claim 8, characterized in that: The liquid outlet pipe section includes a first liquid outlet pipe section, a second liquid outlet pipe section and a third liquid outlet pipe section. The first liquid outlet pipe section is used to introduce the distilled water in the condensation chamber into the non-condensable gas removal device. The second liquid outlet pipe section introduces the degassed distilled water in the non-condensable gas removal device into a storage container. The third liquid outlet pipe section is used to connect the first liquid outlet pipe section and the non-condensable gas removal device. A control valve is provided on the third liquid outlet pipe section.

10. The horizontal hot-pressed distilled water device according to claim 1, characterized in that: It also includes a steam compression pipeline and a compressor, the compressor is arranged on the steam compression pipeline, the steam compression pipeline has an air inlet end and an air outlet end, the air inlet end is connected to the evaporation chamber, and the air outlet end is connected to the condensation chamber, the steam compression pipeline is used to introduce pure steam in the evaporation chamber into the condensation chamber, and the compressor is used to compress the pure steam in the steam compression pipeline.

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