Steam performance detection device

Abstract

The utility model relates to a steam performance detection device, which comprises a control module, a non-condensable gas detection unit, a superheat degree detection unit, a dryness detection unit, a steam inlet and a condensate water inlet, and is characterized in that the non-condensable gas detection unit is in communication connection with the control module; the superheat degree detection unit is in communication connection with the control module; the dryness detection unit is in communication connection with the control module; the steam inlet is communicated with the non-condensable gas detection unit and the superheat degree detection unit; the condensate water inlet is communicated with the non-condensable gas detection unit and the dryness detection unit; the control module can control the non-condensable gas detection unit to detect the content of non-condensable gas in steam entering the non-condensable gas detection unit from the steam inlet and store the detection result. The control module can control the superheat degree detection unit to detect and store the superheat degree of the steam; and the control module can also control the dryness detection unit to detect and store the dryness of the steam.

Description

TECHNICAL FIELD

[0001] The utility model relates to steam three performance detection equipment technical field, especially to a kind of steam performance detection device. BACKGROUND

[0002] With the development of society, medical health gradually is valued by people, with the improvement of regulations, the supervision of the state to the sterilization of enterprise and other related work is more strict.

[0003] Many enterprises currently use steam to sterilize equipment or utensils, tools, etc., so the indicators of steam need to be strictly controlled. Currently, the steam sterilization equipment is regulated in the standard EN285, which specifies the performance testing method for the three indicators of non-condensable gas content, dryness and superheat degree. The non-automatic equipment on the market is optimized and improved based on this method, and the market penetration rate is very high.

[0004] However, the existing technology for detecting the performance of the above three indicators is measured by manual measurement, resulting in large measurement error, time-consuming and unable to continuously measure. In addition, the detection results cannot be recorded and saved in real time. INVENTION CONTENTS

[0005] Therefore, it is necessary to provide a steam performance detection device to solve the technical problems of large measurement error, low efficiency and time-consuming in the related art.

[0006] A steam performance detection device, comprising:

[0007] a control module;

[0008] a non-condensable gas detection unit in communication with the control module;

[0009] a superheat degree detection unit in communication with the control module;

[0010] a dryness detection unit in communication with the control module;

[0011] a steam inlet in communication with the non-condensable gas detection unit and the superheat degree detection unit;

[0012] a condensate water inlet in communication with the non-condensable gas detection unit and the dryness detection unit;

[0013] The control module can control the non-condensable gas detection unit to detect the content of non-condensable gas in the steam entering the non-condensable gas detection unit from the steam inlet and store the detection result; the control module can control the superheat degree detection unit to detect the superheat degree of the steam and store; the control module can also control the dryness degree detection unit to detect the dryness degree of the steam and store.

[0014] In one embodiment, the non-condensable gas detection unit comprises:

[0015] A heat exchanger connected to the condensate water inlet, and the steam inlet is also connected to the heat exchanger;

[0016] A non-condensable gas collection tank connected to the condensate water outlet of the heat exchanger;

[0017] A condensate water collection tank connected to the overflow port of the non-condensable gas collection tank;

[0018] The control module can calculate the content of non-condensable gas in the steam according to the volume of condensate water in the non-condensable gas collection tank and the condensate water collection tank.

[0019] In one embodiment, the non-condensable gas detection unit comprises:

[0020] A first pressure detection member connected to the non-condensable gas collection tank, the first pressure detection member is used to detect the pressure in the non-condensable gas collection tank;

[0021] A second pressure detection member connected to the condensate water collection tank, the second pressure detection member is used to detect the pressure in the condensate water collection tank;

[0022] The overflow port of the non-condensable gas collection tank is consistent with the inlet pipe height of the condensate water collection tank.

[0023] In one embodiment, the non-condensable gas detection unit further comprises:

[0024] A first temperature detection member arranged between the heat exchanger and the non-condensable gas collection tank, the first temperature detection member is used to detect the temperature of the condensate water converted from the steam condensed by the heat exchanger.

[0025] In one embodiment, the non-condensable gas detection unit further comprises:

[0026] An adjusting valve arranged on the condensate water outlet pipe, the condensate water outlet pipe is connected to the heat exchanger;

[0027] The control module can control the adjusting valve according to the detection result of the first temperature detection member.

[0028] In one of the embodiments, the non-condensable gas collecting tank is provided with a gas outlet, the gas outlet is provided with a first electromagnetic valve, the first electromagnetic valve is in communication connection with the control module, and the gas outlet is in communication with an exhaust port.

[0029] In one of the embodiments, the superheat degree detection unit comprises:

[0030] A pressure relief hole plate is in communication with the steam inlet, and the pressure relief hole plate is in communication with the dryness degree detection unit;

[0031] A second temperature detection member is arranged between the pressure relief hole plate and the dryness degree detection unit;

[0032] The control module can calculate the superheat degree of the steam according to the detection result of the second temperature detection member.

[0033] In one of the embodiments, the superheat degree detection unit further comprises:

[0034] A trap valve is in communication with the steam inlet and in communication with a condensate outlet;

[0035] A third temperature detection member is arranged between the trap valve and the steam inlet.

[0036] In one of the embodiments, the dryness degree detection unit comprises:

[0037] A mixing tank is in communication with the pressure relief hole plate and the condensate inlet,

[0038] A fourth temperature detection member is connected to the mixing tank;

[0039] A third pressure detection member is connected to the outlet of the mixing tank, and the outlet of the mixing tank is in communication with the condensate outlet;

[0040] The control module can calculate the dryness degree of the steam according to the detection results of the third pressure detection member, the third temperature detection member and the fourth temperature detection member.

[0041] In one of the embodiments, the dryness degree detection unit further comprises:

[0042] A stirring member is connected to the mixing tank, and the stirring member is used for stirring the steam and water in the mixing tank.

[0043] The utility model discloses the beneficial effects of:

[0044] The utility model provides a kind of steam performance detection device, by not condensable gas detection unit, superheat degree detection unit and dryness degree detection unit communication connection, and steam import is connected with not condensable gas detection unit and superheat degree detection unit intercommunication, to pass through control module and not condensable gas detection unit synergic detection the content of not condensable gas in steam, and detection result is stored to control module;Pass through superheat degree detection unit and control module synergic detection the superheat degree of steam, and superheat degree detection sees over storage to control module.By condensate import and not condensable gas detection unit and dryness degree detection unit intercommunication, to make condensate by condensate import into not condensable gas detection unit and dryness degree detection unit, condense steam, to separate moisture in steam and not condensable gas, to facilitate the detection of not condensable gas content and dryness degree.Control module and dryness degree detection unit synergic detection and store the dryness degree of steam.By the above structure, when detecting the not condensable gas content, dryness degree and superheat degree of steam, no manual detection is needed, and the above structure can realize the detection and storage of three performances directly;And the above structure can continuously detect the three performances of steam, so as to improve the efficiency and accuracy of steam three performance detection, and the detection results can be stored and recorded. BRIEF DESCRIPTION OF DRAWINGS

[0045] Figure 1 The utility model provides a kind of steam performance detection device's schematic diagram for embodiment of the utility model.

[0046] Reference signs:

[0047] Not condensable gas detection unit 100;Heat exchanger 110;Not condensable gas collection tank 120;Gas outlet 121;First electromagnetic valve 122;Condensate collection tank 130;First pressure detection piece 140;Second pressure detection piece 150;First temperature detection piece 160;Regulating valve 170;Superheat degree detection unit 200;Pressure relief hole plate 210;Second temperature detection piece 220;Drain valve 230;Third temperature detection piece 240;Dryness degree detection unit 300;Mixing tank 310;Fourth temperature detection piece 320;Third pressure detection piece 330;Stirring piece 340;Steam import 400;Condensate import 500;Exhaust port 600;Condensate outlet 700;Condensate outlet 800. DETAILED DESCRIPTION

[0048] In order to make the above object, characteristics and advantages of the present application more apparent, concrete embodiments of the present application will be described in detail with reference to the drawings. In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present application. However, the present application can be practiced in a number of different manners without departing from the spirit of the present application. Those skilled in the art will appreciate the scope of the present application and can make similar modifications without departing from the spirit of the present application. Therefore, the present application is not limited by the embodiments disclosed below.

[0049] In the description of the present application, it should be understood that the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential" and the like indicate the orientation or positional relationship based on the orientation or positional relationship shown in the drawings, and are only for the convenience of describing the present application and simplifying the description, and do not indicate or imply 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.

[0050] In addition, the terms "first", "second" are only for descriptive purposes and cannot be understood as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Therefore, the features defined with "first", "second" can explicitly or implicitly include at least one of the features. In the description of the present application, the meaning of "a plurality of" is at least two, such as two, three, etc., unless otherwise specifically limited.

[0051] In the present application, unless otherwise specifically defined and limited, the terms "mounting", "connection", "connection", "fixing" and the like 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; 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 those skilled in the art, the specific meaning of the above terms in the present application can be understood according to the specific circumstances.

[0052] In the present application, unless otherwise explicitly specified and limited, the first feature is "on" or "under" the second feature, which can be direct contact between the first and second features, or indirect contact through an intermediate medium. Moreover, the first feature "above", "above" and "above" the second feature can be directly above or obliquely above the first feature, or only indicate 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 directly below or obliquely below the first feature, or only indicate that the horizontal height of the first feature is less than that of the second feature.

[0053] It should be noted that when an element is referred to as "fixed to" or "disposed on" another element, it can be directly on another element or there can be a middle element. When an element is considered to be "connected" to another element, it can be directly connected to another element or there can be a middle element. The terms "vertical", "horizontal", "up", "down", "left", "right" and similar expressions used herein are for illustrative purposes only and are not the only embodiment.

[0054] Referring to Figure 1 The utility model discloses an embodiment provides a kind of steam performance detection device, steam performance detection device includes control module, non-condensable gas detection unit 100, superheat degree detection unit 200, dryness detection unit 300, steam import 400 and condensate import 500, non-condensable gas detection unit 100 is connected with control module communication;Superheat degree detection unit 200 is connected with control module communication;Dryness detection unit 300 is connected with control module communication;Steam import 400 is communicated with non-condensable gas detection unit 100 and superheat degree detection unit 200;Condensate import 500 is communicated with non-condensable gas detection unit 100 and dryness detection unit 300;Wherein, control module can control non-condensable gas detection unit 100 detects the content of non-condensable gas in the steam that enters non-condensable gas detection unit 100 from steam import 400 and stores detection result;Control module can control superheat degree detection unit 200 detects the superheat degree of steam and stores;Control module can also control dryness detection unit 300 detects the dryness of steam and stores.

[0055] The technical scheme provides a steam performance detection device, which is characterized in that: the non-condensable gas detection unit 100, the superheat degree detection unit 200 and the dryness degree detection unit 300 are communicatively connected, the steam inlet 400 is connected in communication with the non-condensable gas detection unit 100 and the superheat degree detection unit 200, the content of non-condensable gas in the steam is detected by the control module and the non-condensable gas detection unit 100 in cooperation, and the detection result is stored in the control module; the superheat degree of the steam is detected by the superheat degree detection unit 200 and the control module in cooperation, and the superheat degree detection result is stored in the control module. The condensate water inlet 500 is connected in communication with the non-condensable gas detection unit 100 and the dryness degree detection unit 300, so that the condensate water enters the non-condensable gas detection unit 100 and the dryness degree detection unit 300 through the condensate water inlet 500, the steam is condensed, the water and the non-condensable gas in the steam are separated, and the content of the non-condensable gas and the dryness degree are detected. The dryness degree of the steam is detected by the control module and the dryness degree detection unit 300 in cooperation and stored. Through the above structure, when the content of the non-condensable gas, the dryness degree and the superheat degree of the steam are detected, manual detection is not required, and the detection of the three performances and storage can be realized directly through the above structure. Moreover, the above structure can continuously detect the three performances of the steam, thereby improving the efficiency and accuracy of the detection of the three performances of the steam, and the detection result can be stored and recorded.

[0056] It can be understood that, in addition to gaseous water molecules, non-condensable gases such as carbon dioxide in the air exist in the steam, and therefore it is necessary to detect the content of the non-condensable gas in the steam.

[0057] As shown in the drawings, Figure 1 In one embodiment, the non-condensable gas detection unit 100 includes a heat exchanger 110, a non-condensable gas collection tank 120 and a condensate water collection tank 130. The heat exchanger 110 is connected in communication with the condensate water inlet 500, and the steam inlet 400 is also connected in communication with the heat exchanger 110. The non-condensable gas collection tank 120 is connected in communication with the condensate water outlet 800 of the heat exchanger 110. The condensate water collection tank 130 is connected in communication with the overflow port of the non-condensable gas collection tank 120. The control module can calculate the content of the non-condensable gas in the steam according to the volume of the condensate water in the non-condensable gas collection tank 120 and the condensate water collection tank 130.

[0058] The heat exchanger 110 is connected with the condensed water inlet 500, and the steam inlet 400 is connected with the heat exchanger 110, so that the condensed water flows into the heat exchanger 110 from the condensed water inlet 500, and the temperature of the surface of the heat exchanger 110 approaches the temperature of the condensed water; and the steam flows into the heat exchanger 110 from the steam inlet 400, and the gaseous water in the steam is condensed into liquid water after heat exchange between the steam and the heat exchanger 110. The condensed water outlet 800 of the heat exchanger 110 is connected with the non-condensable gas collecting tank 120, so that the condensed water formed after being condensed by the heat exchanger 110 flows into the non-condensable gas collecting tank 120, and the non-condensable gas also flows into the non-condensable gas collecting tank 120. Since the overflow port of the non-condensable gas collecting tank 120 is connected with the condensed water collecting tank 130, the condensed water can flow from the non-condensable gas collecting tank into the condensed water collecting tank 130. The control module calculates the content of the non-condensable gas in the steam according to the volume of the condensed water in the non-condensable gas collecting tank and the condensed water collecting tank 130.

[0059] In the embodiment, the condensed water and the non-condensable gas enter the non-condensable gas collecting tank 120 from the upper part of the non-condensable gas collecting tank 120, so that water-gas separation can be better achieved without affecting the entry of the condensed water.

[0060] As shown in Figure 1 , specifically, the non-condensable gas detection unit 100 includes a first pressure detection member 140 and a second pressure detection member 150. The first pressure detection member 140 is connected to the non-condensable gas collecting tank 120 and is used to detect the pressure in the non-condensable gas collecting tank 120. The second pressure detection member 150 is connected to the condensed water collecting tank 130 and is used to detect the pressure in the condensed water collecting tank 130. The overflow port of the non-condensable gas collecting tank 120 is at the same height as the inlet pipe of the condensed water collecting tank 130. An air outlet 121 is arranged on the non-condensable gas collecting tank 120, and a first electromagnetic valve 122 is arranged at the air outlet 121. The first electromagnetic valve 122 is in communication connection with the control module, and the air outlet 121 is connected with the exhaust port 600.

[0061] As shown in Figure 1 , specifically, the first pressure detection member 140 and the second pressure detection member 150 are both pressure sensors. By arranging pressure sensors on the non-condensable gas collecting tank and the condensed water collecting tank 130, the pressures in the non-condensable gas collecting tank 120 and the condensed water collecting tank 130 can be detected, so that the volumes of the condensed water in the non-condensable gas collecting tank 120 and the condensed water collecting tank 130 can be obtained, and the content of the non-condensable gas in the steam can be calculated through the volume difference of the condensed water in the two tanks. By connecting the overflow port of the non-condensable gas collecting tank 120 with the condensed water collecting tank 130, the condensed water can flow from the non-condensable gas collecting tank into the condensed water collecting tank 130.

[0062] By setting an outlet 121 on the non-condensable gas collection tank 120 and connecting the outlet 121 to the exhaust port 600 of the entire steam performance testing device, non-condensable gas is discharged through the outlet 121. By setting a first solenoid valve 122 at the outlet 121 and communicating with the control module, the opening and closing of the first solenoid valve 122 is controlled by the control module, thereby realizing the connection or disconnection between the outlet 121 and the exhaust port 600.

[0063] like Figure 1 As shown, specifically, when detecting the content of non-condensable gases in steam, the first solenoid valve 122 is first opened via the control module to connect the outlet 121 with the exhaust port 600. This allows condensate and non-condensable gases formed from the condensed steam to flow from the heat exchanger 110 into the non-condensable gas collection tank 120. The non-condensable gases are discharged from the outlet 121 through the exhaust port 600. When the condensate level in the non-condensable gas collection tank 120 reaches the overflow port height, the condensate flows from the overflow port into the condensate collection tank 130. When the liquid levels in the condensate collection tank 130 and the non-condensable gas collection tank 120 are equal, that is, when they reach the overflow port height, the pressure values ​​of the first pressure sensor 140 and the second pressure sensor 150 are equal. The first solenoid valve 122 can be closed via the control module, at which point the non-condensable gases in the non-condensable gas collection tank 120 are not discharged from the non-condensable gas collection tank 120. Condensate in the non-condensable gas collection tank 120 flows into the condensate collection tank 130 under the pressure of the non-condensable gas. At this time, the pressure value of the first pressure sensor 140 and the pressure value detected by the second pressure sensor 150 are the liquid level height of the condensate in the corresponding collection tank; the difference between the pressure value of the second pressure sensor 150 and its initial pressure value is the sum of the increase in non-condensable gas and the decrease in condensate in the non-condensable gas collection tank 120, which is the total volume of steam; the difference between the pressure value of the first pressure sensor 140 and its initial pressure value is the volume of non-condensable gas in the steam. The content of non-condensable gas in the steam can be calculated from the total volume of steam and the volume of non-condensable gas. After detecting the content of non-condensable gas, the outlet 121 can be connected to the exhaust port 600 to discharge the non-condensable gas.

[0064] like Figure 1As shown, in one embodiment, the non-condensable gas detection unit 100 further comprises a first temperature detection member 160, which is arranged between the heat exchanger 110 and the non-condensable gas collection tank 120, and is configured to detect the temperature of the condensed water, which is converted from the steam condensed by the heat exchanger 110. The non-condensable gas detection unit 100 further comprises an adjusting valve 170, which is arranged on a condensed water outlet pipe, and is in communication with the heat exchanger 110 and the condensed water outlet 700. The control module is configured to control the adjusting valve 170 according to the detection result of the first temperature detection member 160.

[0065] Specifically, the first temperature detection member 160 is a temperature sensor. The temperature sensor is arranged between the heat exchanger 110 and the non-condensable gas collection tank 120, and is configured to detect the temperature of the condensed water condensed by the heat exchanger 110. If the temperature of the condensed water is within a preset range, it indicates that the flow rate of the cooling water in the heat exchanger 110 is appropriate. If the temperature of the condensed water exceeds the preset range, the control unit controls the adjusting valve 170 to adjust the flow rate of the condensed water, so as to adjust the temperature of the heat exchanger 110, and thus make the condensation effect of the steam close to the ideal state.

[0066] As shown, Figure 1 In one embodiment, the superheat detection unit 200 comprises a pressure relief hole plate 210 and a second temperature detection member 220. The pressure relief hole plate 210 is in communication with the steam inlet 400 and the dryness detection unit 300. The second temperature detection member 220 is arranged between the pressure relief hole plate 210 and the dryness detection unit 300. The control module is configured to calculate the superheat of the steam according to the detection result of the second temperature detection member 220.

[0067] The pressure relief hole plate 210 is arranged to relieve the pressure of the steam. The second temperature detection member 220, i.e., the temperature sensor, is arranged between the pressure relief hole plate 210 and the dryness detection unit 300, and is configured to detect the temperature of the steam at the pressure relief hole plate 210, so as to calculate the superheat of the steam.

[0068] As shown, Figure 1As shown in the drawings, in one embodiment, the superheat degree detection unit 200 further comprises a drain valve 230 and a third temperature detection member 240, the drain valve 230 is connected with the steam inlet 400 and connected with the condensate water outlet 800; the third temperature detection member 240 is arranged between the drain valve 230 and the steam inlet 400. By arranging the drain valve 230 between the steam inlet 400 and the condensate water outlet 800, the steam is prevented from splashing outside the equipment to cause harm to people, in addition, the drain valve 230 is arranged to prevent continuous discharge of the steam source, and the temperature sensor is arranged between the drain valve 230 and the steam inlet 400 to monitor the temperature of the steam, thereby ensuring the stability of the steam.

[0069] As shown in the drawings, Figure 1 As shown in the drawings, in one embodiment, the dryness degree detection unit 300 comprises a mixing tank 310, a fourth temperature detection member 320 and a third pressure detection member 330, the mixing tank 310 is connected with the pressure relief hole plate 210 and the condensate water inlet 500, the fourth temperature detection member 320 is connected to the mixing tank 310; the third pressure detection member 330 is connected to the outlet of the mixing tank 310, and the outlet of the mixing tank 310 is connected with the condensate water outlet 800; wherein the control module can calculate the dryness degree of the steam according to the detection results of the third pressure detection member 330, the third temperature detection member 240 and the fourth temperature detection member 320. The dryness degree detection unit 300 further comprises a stirring member 340, the stirring member 340 is connected to the mixing tank 310, and the stirring member 340 is used to stir the steam and water in the mixing tank 310.

[0070] The mixing tank 310 is connected with the condensate water inlet 500, so that the condensate water flows into the mixing tank 310 from the condensate water inlet 500; the pressure relief hole plate 210 is connected with the mixing tank 310, so that the steam flowing out of the pressure relief hole plate 210 enters the mixing tank 310; after the condensate water and the steam are mixed in the mixing tank 310, the moisture in the steam is condensed, and the non-condensable gas is separated from the moisture. By arranging the stirring member 340 in the mixing tank 310, the steam and water in the mixing tank 310 are stirred by the stirring member 340, so that the water in the mixing tank 310 is more uniform. The outlet of the mixing tank 310 is connected with the condensate water outlet, so that the water in the mixing tank 310 is discharged from the condensate water outlet 800.

[0071] Specifically, the condensed water is introduced into the mixing tank 310 from the condensed water inlet 500, and the third pressure detecting member 330 can detect the height of the liquid level in the mixing tank 310, and the water inlet is stopped when the liquid level in the mixing tank 310 reaches the preset position. At this time, the amount and temperature of the water in the mixing tank 310 can be detected according to the third pressure detecting member 330 and the fourth temperature detecting member 320. The steam is introduced into the mixing tank 310 from the steam inlet 400, and after passing through the pressure relief hole plate 210, it is introduced into the mixing tank 310, and when the preset temperature is reached, the steam introduction into the mixing tank 310 is stopped, and then the steam is stirred uniformly by the stirring member 340, and then the amount and temperature of the heated water are detected according to the third pressure detecting member 330 and the fourth temperature detecting member 320, and the dryness of the steam can be calculated according to the temperature of the steam. It should be noted that in the embodiment, the mixing tank 310 adopts vacuum insulation technology, which can effectively prevent heat loss. In addition, in the utility model, the dryness detecting unit 300 and the non-condensable gas detecting unit 100 are arranged as two independent units, and they do not affect each other, so as to ensure the accuracy of the detection.

[0072] The technical features of the above-described embodiments can be combined in any manner. To make the description concise, all possible combinations of the technical features in the above-described embodiments are not described, but as long as the combinations of the technical features do not contradict, they should be considered within the scope of the present disclosure.

[0073] The above-described embodiments only express several implementation manners of the utility model, and the description is more specific and detailed, but it should not be understood as a limitation on the scope of the utility model patent. It should be noted that for ordinary skilled persons in the art, without departing from the concept of the utility model, some modifications and improvements can be made, which are within the protection scope of the utility model. Therefore, the protection scope of the utility model patent should be subject to the appended claims.

Claims

1. A steam performance detection device, characterized by, The steam performance detection device comprises: a control module; a non-condensable gas detection unit, which is in communication connection with the control module; a superheat degree detection unit, which is in communication connection with the control module; a dryness degree detection unit, which is in communication connection with the control module; a steam inlet, which is in communication with the non-condensable gas detection unit and the superheat degree detection unit; a condensate water inlet, which is in communication with the non-condensable gas detection unit and the dryness degree detection unit; wherein the control module can control the non-condensable gas detection unit to detect the content of non-condensable gas in the steam entering the non-condensable gas detection unit from the steam inlet and store the detection result; the control module can control the superheat degree detection unit to detect the superheat degree of the steam and store; and the control module can also control the dryness degree detection unit to detect the dryness degree of the steam and store.

2. The steam performance detection device of claim 1, wherein, The non-condensable gas detection unit comprises: a heat exchanger, which is in communication with the condensate water inlet and the steam inlet; a non-condensable gas collection tank, which is in communication with the condensate water outlet of the heat exchanger; a condensate water collection tank, which is in communication with the overflow port of the non-condensable gas collection tank; wherein the control module can calculate the content of non-condensable gas in the steam according to the volume of condensate water in the non-condensable gas collection tank and the condensate water collection tank.

3. The steam performance detection device of claim 2, wherein, The non-condensable gas detection unit comprises: a first pressure detection member, which is connected to the non-condensable gas collection tank and is used to detect the pressure in the non-condensable gas collection tank; a second pressure detection member, which is connected to the condensate water collection tank and is used to detect the pressure in the condensate water collection tank; wherein the overflow port of the non-condensable gas collection tank is consistent in height with the inlet pipe of the condensate water collection tank.

4. The steam performance detection device of claim 2, wherein, The non-condensable gas detection unit further comprises: a first temperature detection member, which is arranged between the heat exchanger and the non-condensable gas collection tank and is used to detect the temperature of the condensate water converted from the steam condensed by the heat exchanger.

5. The steam performance detection device of claim 4, wherein, The non-condensable gas detection unit further comprises: a regulating valve, which is arranged on a condensate water outlet pipe in communication with the heat exchanger; wherein the control module can control the regulating valve according to the detection result of the first temperature detection member.

6. The steam performance detection apparatus of claim 2, wherein, An air outlet is arranged on the non-condensable gas collection tank, and a first electromagnetic valve is arranged at the air outlet, which is in communication connection with the control module.

7. The steam performance detection apparatus of claim 1, wherein, The superheat degree detection unit comprises: a pressure relief hole plate, which is in communication with the steam inlet and the dryness degree detection unit; a second temperature detection member, which is arranged between the pressure relief hole plate and the dryness degree detection unit; wherein the control module can calculate the superheat degree of the steam according to the detection result of the second temperature detection member.

8. The steam performance detection apparatus of claim 7, wherein, The superheat degree detection unit further comprises: a trap valve, which is in communication with the steam inlet and the condensate water outlet; a third temperature detection member, which is arranged between the trap valve and the steam inlet.

9. The steam performance detection apparatus of claim 8, wherein, The dryness degree detection unit comprises: a mixing tank, which is in communication with the pressure relief orifice plate and the condensed water inlet, a fourth temperature detecting member connected to the mixing tank; a third pressure detecting member connected to an outlet of the mixing tank, which is in communication with a condensed water outlet; wherein the control module is capable of calculating the dryness of the steam according to the detection results of the third pressure detecting member, the third temperature detecting member and the fourth temperature detecting member.

10. The steam performance detection device of claim 9, wherein, The dryness detecting unit further comprises: a stirring member connected to the mixing tank, which is used for stirring the steam and water in the mixing tank.

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