Full-intelligent monitoring heat exchanger with pressure drop measuring function and system of full-intelligent monitoring heat exchanger

By using a fully intelligent monitoring heat exchanger with pressure drop measurement in the cooling circulating water system, the temperature and pressure drop are monitored in real time, solving the problem of inaccurate measurement of fouling thermal resistance. This enables timely detection of scaling and evaluation of the effectiveness of chemicals, ensuring equipment safety.

CN223882785UActive Publication Date: 2026-02-06GUODIAN NANJING ELECTRIC POWER TEST RES CO LTD
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Patent Information

Application Number
CN202520319866.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-02-26
Publication Date
2026-02-06
Estimated Expiration
2035-02-26

AI Technical Summary

Technical Problem

In existing cooling water circulation systems, the thermal resistance of fouling cannot be accurately measured, making it impossible to detect scaling in a timely manner, and thus impossible to effectively assess the effectiveness of corrosion inhibitors and scale inhibitors, which affects equipment safety.

Method used

A fully intelligent monitoring heat exchanger with pressure drop measurement is adopted, and a simulation test tube unit and an intelligent instrument unit are configured, including thermometers, temperature sensors, differential pressure gauges, etc., to monitor temperature and pressure drop in real time. Combined with the execution control unit, the operating status of the heat exchanger can be evaluated in real time.

Benefits of technology

It enables timely detection of scaling in heat exchangers, allows for more accurate assessment of reagent effectiveness, and ensures safe equipment operation.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model provides a full-intelligent monitoring heat exchanger with a pressure drop measuring function and a system of the full-intelligent monitoring heat exchanger with the pressure drop measuring function, and the full-intelligent monitoring heat exchanger with the pressure drop measuring function comprises a simulation experiment pipe unit and an intelligent instrument unit, two ends of the experiment pipe are respectively connected with a circulating water inlet pipeline and a circulating water outlet pipeline in a flow-adjustable manner, and the upper side and the lower side of the pipe wall are respectively connected with a steam pipeline and a condensation pipeline; and the intelligent instrument unit is provided with a thermodetector for respectively measuring the inlet water temperature, the outlet water temperature and the steam temperature of the experiment pipe and a differential pressure gauge for pressure drop between the inlet and the outlet at the two ends of the experiment pipe. According to the utility model, the heat exchange process and the scaling condition can be accurately mastered through multi-point temperature monitoring and pressure drop monitoring; flow adjustment is flexible, and steam adjustment is safe and efficient; a discharge port and a steam trap are arranged, so that the system is convenient to maintain; and the real-time monitoring and early warning function can discover abnormity in advance, so that the equipment failure downtime is reduced, and the accuracy of water treatment effect evaluation is improved.
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Description

TECHNICAL FIELD

[0001] The utility model relates to cooling circulating water treatment technical field, especially a kind of full intelligent monitoring heat exchanger and system with pressure drop determination. BACKGROUND

[0002] Water shortage is one of the problems faced by the world, and water conservation has become the consensus of mankind. Therefore, the promotion of circulating water cooling system in the industrial field has great significance for water conservation, and in the industrial circulating cooling water system, cooling water is continuously recycled,

[0003] The quality of water will deteriorate, causing corrosion and fouling of equipment, and in severe cases, it will damage the safety production of factory. Therefore, water quality must be monitored in time, and effective descaling and corrosion prevention treatment must be taken. The commonly used method for scale inhibition and corrosion prevention treatment is to use corrosion and scale inhibition composite agent, so the effect of the agent must be tracked in time.

[0004] At present, most of the cooling circulating water systems monitor the corrosion, fouling and deposition on the metal surface by monitoring the heat exchanger. Due to various reasons in the monitoring process, the fouling thermal resistance value is sometimes not accurate, which leads to the fact that the fouling of the experimental tube cannot be observed in time, and active measures cannot be taken effectively, and the final evaluation is also to take out the experimental tube stage, and the effect of water treatment is evaluated by weight loss method. UTILITY MODEL CONTENT

[0005] The utility model aims at overcoming the deficiencies in the prior art, and provides a full intelligent monitoring heat exchanger with pressure drop determination and system.

[0006] To achieve the above-mentioned purpose, the utility model is implemented by the following technical scheme:

[0007] In the first aspect, the utility model provides a full intelligent monitoring heat exchanger with pressure drop determination, which comprises a simulation experimental tube unit and an intelligent instrument unit, the simulation experimental tube unit is provided with a long strip experimental tube, the two ends of the experimental tube are connected with circulating water inlet pipe and circulating water outlet pipe with adjustable flow, and the upper and lower sides of the pipe wall are respectively connected with steam pipe and condenser pipe, the intelligent instrument unit is provided with temperature measuring instrument for measuring inlet water temperature, outlet water temperature and steam temperature of experimental tube respectively, and differential pressure instrument for measuring pressure drop between inlet and outlet of experimental tube.

[0008] Further, the temperature measuring instrument comprises a thermometer and a temperature sensor, and the thermometer and the temperature sensor are respectively arranged at the inlet and outlet of the experimental tube and the communication inlet of the steam pipe and the experimental tube.

[0009] Furthermore, a handle control valve is provided at the connection point between the two ends of the experimental tube and the circulating water inlet pipe and the circulating water outlet pipe, respectively, and a manual flow meter and an electric regulating valve are provided on the circulating water inlet pipe.

[0010] Furthermore, the steam pipeline is equipped with a filter, a pressure gauge, a self-regulating steam regulating valve, and an electric regulating valve connected in series.

[0011] Furthermore, the experimental tube is equipped with a 0.6 MPa pressure gauge.

[0012] Furthermore, the circulating water inlet pipe is equipped with an inlet and outlet.

[0013] Furthermore, a steam trap is installed on the condensate pipe.

[0014] Furthermore, the circulating water inlet pipe, circulating water outlet pipe, steam pipe, and condensate pipe are all equipped with external connection flanges.

[0015] Furthermore, it also includes an execution control unit, which is connected to the electric regulating valve via signal control.

[0016] Secondly, this utility model provides a monitoring system, comprising:

[0017] Fouling thermal resistance meter;

[0018] The fully intelligent monitoring heat exchanger with pressure drop measurement as described in any one of the first aspects;

[0019] The fouling thermal resistance meter is used to collect the inlet temperature, outlet temperature, steam temperature, inlet water flow rate, and pressure difference of the fully intelligent monitoring heat exchanger.

[0020] Compared with existing technologies, the beneficial effects achieved by this utility model are as follows: The fully intelligent monitoring heat exchanger and its system with pressure drop measurement of this utility model, by installing thermometers and temperature sensors at the inlet and outlet of the experimental tube and at the air inlet connecting the steam pipe and the experimental tube, can accurately measure the temperature at different locations, allowing for a comprehensive understanding of temperature changes during the heat exchange process; the differential pressure gauge measures the pressure drop between the inlet and outlet of the experimental tube, determining the scaling condition inside the heat exchanger, and real-time monitoring of the pressure drop can promptly detect early signs of scaling; real-time monitoring of parameters such as temperature and pressure drop by the intelligent instrument unit, combined with the control unit's control of components such as the electric regulating valve, enables real-time evaluation of the heat exchanger's operating status; real-time monitoring of parameters such as pressure drop and temperature can more promptly assist in evaluating the effectiveness of corrosion inhibitors and scale inhibitors during the specific application of the heat exchanger. Attached Figure Description

[0021] Figure 1The utility model provides a structure schematic diagram of full intelligent monitoring heat exchanger with pressure drop determination.

[0022] In the figure: Z1, Z2, Z3, Z4 and Z5 are external connection flanges;S6 and S13 are hanger pieces;S8 is a heat exchange cavity;S9 is an experimental tube;C1, C2 and C3 are thermometers;C4, C5 and C6 are temperature sensors;S7 and S10 are operating handles;S1~S5, S14, 15 are all ball valves;Q1 is a stop valve, Q6, Q8 are ball valves. DETAILED DESCRIPTION

[0023] The utility model will be further described below in connection with the drawings. The following examples are only used to more clearly illustrate the technical scheme of the utility model, and cannot limit the protection scope of the utility model.

[0024] In the description of the utility model, it is understood that the orientation or position relationship indicated by the terms "center", "longitudinal", "transverse", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer" and the like is based on the orientation or position relationship shown in the drawings, and is only for the convenience of describing the utility model and simplifying the description, and therefore cannot be understood as indicating or implying that the indicated device or element must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as limiting the utility model. In addition, the terms "first", "second" and the like are only for the purpose of description, and cannot be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Therefore, the features limited by "first", "second" and the like can explicitly or implicitly include one or more features. In the description of the utility model, unless otherwise specified, the meaning of "a plurality of" is two or more.

[0025] In the description of the utility model, it should be noted that, unless otherwise specified and limited, the terms "mounting", "connection", "connection" should be understood broadly, for example, it can be fixedly connected, or it can be detachably connected, or integrally connected;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, or it can be the communication between two elements. For ordinary skilled in the art, the specific meaning of the above terms in the utility model can be understood according to the specific circumstances.

[0026] As Figure 1As shown, the embodiment of the present application provides a full-intelligent monitoring heat exchanger with pressure drop measurement, which comprises a simulation experiment pipe unit and an intelligent instrument unit. The simulation experiment pipe unit is configured with a long strip-shaped experiment pipe, the two ends of the experiment pipe are connected with a circulating water inlet pipeline and a circulating water outlet pipeline with adjustable flow, and the upper and lower sides of the pipe wall are connected with a steam pipeline and a condensing pipeline, respectively. The intelligent instrument unit is configured with a temperature measuring instrument for measuring the inlet water temperature, outlet water temperature and steam temperature of the experiment pipe, respectively, and a pressure difference instrument for measuring the pressure drop between the inlet and outlet of the two ends of the experiment pipe.

[0027] In the embodiment, the temperature measuring instrument comprises a thermometer and a temperature sensor, which are respectively arranged at the inlet and outlet of the two ends of the experiment pipe and the communication inlet of the steam pipeline and the experiment pipe. By arranging the thermometer and the temperature sensor at the inlet, the outlet of the experiment pipe and the communication inlet of the steam pipeline and the experiment pipe, the temperature at different positions can be accurately measured, and the temperature change in the heat exchange process can be comprehensively mastered.

[0028] For example, in an industrial circulating cooling water system, accurate temperature data is crucial for judging the heat exchange effect. If the inlet water temperature of the experiment pipe is high and the outlet water temperature drops significantly, it indicates that the heat exchange effect is good. On the contrary, if the outlet water temperature does not drop significantly, it may indicate that there is a problem such as fouling in the heat exchanger, which affects heat transfer.

[0029] In the embodiment, the experiment pipe material can be ceramic or metal.

[0030] A handle control valve is arranged at the connection between the two ends of the experiment pipe and the circulating water inlet pipeline and the circulating water outlet pipeline. A manual flowmeter and an electric regulating valve are arranged on the circulating water inlet pipeline, so that the flow adjustment can be manually operated or automatically controlled through the electric regulating valve. During the experiment, the flow can be flexibly adjusted according to different monitoring requirements. For example, when testing the heat exchange efficiency, a certain flow stability needs to be maintained, and the automatic control function of the electric regulating valve can accurately maintain the set flow. When the system needs to be flushed or the flow needs to be adjusted, the manual valve and the manual flowmeter can be conveniently operated.

[0031] Specifically, the circulating water inlet pipeline is sequentially connected in series with a ball valve S1, a connecting flange Z1, a filter S17, a ball valve S2, a rotor flowmeter, a flowmeter X1, and a ball valve S3 and an electric valve S4 and a handle control valve S7 in parallel from the circulating water inlet. In addition, a flange Z2, a ball valve S5, a hanger S6 and a handle control valve S7 are sequentially connected in series from the water inlet discharge port, and the outlet of the electric valve S4 is sequentially connected with the ball valve S5, the flange Z2 and the water inlet discharge port.

[0032] In this embodiment, a 0.6 MPa pressure gauge Q7 is arranged on the experimental tube. The circulating water inlet pipeline is provided with a water inlet discharge port to facilitate the discharge of circulating water when necessary, for example, when the medicament is replaced or the system is cleaned.

[0033] The circulating water outlet pipeline is sequentially connected in series with a ball valve S14, a flange Z3, a ball valve S15 and a circulating water outlet from the handle control valve S10, and the ball valve S14 is connected in parallel with a ball valve S11, a hanger S13 and a ball valve S12.

[0034] The steam pipeline is provided with a stop valve Q1, a flange Z4, a filter Q2, a pressure gauge Q3, a self-operated steam regulating valve Q4 and an electric regulating valve Q5, and a ball valve Q6 connected in series. The filter can remove impurities in the steam to ensure the cleanliness of the steam and prevent impurities from entering the heat exchanger to affect the heat exchange effect and the service life of the equipment. The pressure gauge is used to monitor the steam pressure in real time, the self-operated steam regulating valve can automatically adjust the steam flow according to the change of the steam pressure, and the electric regulating valve can realize more accurate steam flow control. Under the premise of ensuring the safety of steam supply, the steam flow can be efficiently adjusted to meet the steam demand of the heat exchanger under different working conditions.

[0035] A trap Q9 and a flange Z5 are arranged on the condensing pipeline, wherein the trap Q9 is connected in parallel with a ball valve Q8, which can effectively remove condensate and prevent the condensate from accumulating in the pipeline to affect the flow of steam and the heat exchange efficiency.

[0036] The circulating water inlet pipeline, the circulating water outlet pipeline, the steam pipeline and the condensing pipeline are all provided with external connection flanges, which are convenient for connecting with other corresponding external equipment, and improve the universality and expandability of the equipment.

[0037] In this embodiment, the full-intelligent monitoring heat exchanger further comprises an execution control unit connected with the electric regulating valve signal control and connected with the temperature sensor and the like signals to obtain relevant parameter data in real time.

[0038] In this embodiment, the utility model provides a kind of monitoring system, comprising:

[0039] Fouling resistance instrument;

[0040] Full-intelligent monitoring heat exchanger with pressure drop determination as described in any of the above;

[0041] The fouling resistance instrument is used to collect the inlet temperature, outlet temperature, steam temperature, water flow and pressure difference of the full-intelligent monitoring heat exchanger, realize the calculation of the fouling resistance, complete the control of the water flow and the steam temperature, and provide reliable data for the dosing equipment.

[0042] Specifically, the dirt thermal resistance instrument mainly comprises a CPU, a ROM program memory, an E2PROM data recorder, a RAM instant data recorder, an A / D, a D / A conversion circuit, a communication module, a keyboard, a liquid crystal display and the like.

[0043] The technical features of the above-described embodiments can be combined in any manner, and to make the description concise, all possible combinations of the technical features in the above-described embodiments are not described, however, as long as the combinations of the technical features do not exist, they should be considered as the scope of the description.

[0044] The above-described embodiments only express several implementation manners of the utility model, the description is more specific and detailed, but it should not be understood as the limitation of the utility model patent scope. It should be pointed out that for ordinary skilled in the art, on the premise of not departing from the utility model concept, a number of modifications and improvements can be made, which belong to 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 fully intelligent monitored heat exchanger with pressure drop measurement, characterized by, It comprises a simulation experiment tube unit and an intelligent instrument unit, the simulation experiment tube unit is configured with a long strip-shaped experiment tube, the two ends of the experiment tube are respectively connected with a circulating water inlet pipeline and a circulating water outlet pipeline with adjustable flow, and the upper and lower sides of the tube wall are respectively connected with a steam pipeline and a condensing pipeline, the intelligent instrument unit is configured with a temperature measuring instrument for measuring the inlet water temperature, outlet water temperature and steam temperature of the experiment tube, and a pressure difference instrument for measuring the pressure drop between the inlet and outlet of the experiment tube.

2. The fully intelligent monitored heat exchanger with pressure drop measurement as claimed in claim 1 wherein, The temperature measuring instrument comprises a thermometer and a temperature sensor, and the thermometer and the temperature sensor are respectively arranged at the inlet and outlet of the two ends of the experiment tube and the communication inlet of the steam pipeline and the experiment tube.

3. The fully intelligent monitored heat exchanger with pressure drop measurement of claim 2, wherein, A handle control valve is arranged at the connection between the two ends of the experiment tube and the circulating water inlet pipeline and the circulating water outlet pipeline, and a manual flowmeter and an electric regulating valve are arranged on the circulating water inlet pipeline.

4. The fully intelligent monitored heat exchanger with pressure drop measurement of claim 3, wherein, The steam pipeline is provided with a filter, a pressure gauge, a self-operated steam regulating valve and an electric regulating valve connected in sequence.

5. The fully intelligent monitored heat exchanger with pressure drop measurement as claimed in claim 2 wherein, A 0.6MPa pressure gauge is arranged on the experiment tube.

6. The fully intelligent monitored heat exchanger with pressure drop measurement of claim 1, wherein, The circulating water inlet pipeline is provided with a water inlet and discharge port.

7. The fully intelligent monitored heat exchanger with pressure drop measurement of claim 1, wherein, A trap is arranged on the condensing pipeline.

8. The fully intelligent monitored heat exchanger with pressure drop measurement of claim 1, wherein, Flanges are arranged on the circulating water inlet pipeline, the circulating water outlet pipeline, the steam pipeline and the condensing pipeline.

9. The fully intelligent monitored heat exchanger with pressure drop measurement of claim 4, wherein, An execution control unit is further arranged and is signal-controlled with the electric regulating valve.

10. A heat exchanger system for monitoring, the system comprising: It comprises: a fouling resistance instrument; a full intelligent monitoring heat exchanger with pressure drop measurement according to any one of claims 1-9; the fouling resistance instrument is used to collect the inlet temperature, outlet temperature, steam temperature, water flow and pressure difference of the full intelligent monitoring heat exchanger.