Co-processing purification system for flue gas from coal-fired power units with condensation function
By implementing the linkage control of flue gas desulfurization and dust removal devices and the treatment of dust agglomeration in the flue gas co-purification system of coal-fired units, the problems of ineffective energy consumption and high manual operation intensity in independent operation are solved, thereby improving dust removal efficiency and reducing energy consumption.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- XINJIANG WESTERN TIANFU HESHENG THERMAL POWER CO LTD
- Filing Date
- 2025-08-01
- Publication Date
- 2026-06-30
AI Technical Summary
In the current coal-fired power generation process, the flue gas desulfurization and dust removal devices operate independently, resulting in high ineffective energy consumption and unstable parameter adjustment lag, and high reliance on manual operation.
A coal-fired unit flue gas co-purification system with condensation function is adopted, including a core processing module, a flue gas monitoring module, a co-control module and a dynamic execution module. It realizes the linkage control between the external desulfurization device and the bag filter dust collector. The processing parameters are automatically adjusted through the dynamic optimization unit, and the dust is converted into liquid substances by the condensation unit to increase the contact area.
It reduced the workload of staff, improved the efficiency of bag filter dust collection, reduced ineffective energy consumption, and achieved efficient purification of flue gas.
Smart Images
Figure CN224422370U_ABST
Abstract
Description
Technical Field
[0006]
[0001] The utility model relates to the technical field of coal-fired unit power generation, and particularly relates to a flue gas collaborative purification system for coal-fired units with a coagulation function. Background Art
[0002] During the power generation process of coal-fired units, flue gas desulfurization treatment and dust removal operations have long been in an independent operating state. The desulfurization device and the bag filter dust collector operate as two independent devices respectively, and the problem of ineffective energy consumption is relatively prominent.
[0003] The current main technical path to achieve device linkage control still relies on staff with more operation experience to manually calibrate and adjust the processing parameters of the two devices regularly. This regulation method relying on manual experience has the following problems: on the one hand, frequent manual intervention greatly increases the operation intensity of the staff; on the other hand, the lag of parameter adjustment makes it difficult to stably present the linkage effect between the two devices. Content of the Utility Model
[0004] To solve the defects of the prior art, the flue gas collaborative purification system for coal-fired units with a coagulation function provided by the utility model mainly includes a core processing module, a flue gas monitoring module, a collaborative control module and a dynamic execution module. When in use, under the action of the dynamic optimization unit in the collaborative control module, the operating state of the dynamic execution module can be adjusted, that is, the utility model can automatically adjust the corresponding processing parameters in the external desulfurization device and the external bag filter dust collector. Such a design enables the flue gas to meet the emission standards after being treated by the external desulfurization device and the external bag filter dust collector; in addition, the coagulation unit in the dynamic execution module can reduce the temperature of the flue gas entering the external bag filter dust collector to near the dew point, coagulate the dust in the flue gas and convert it into a liquid substance. Such a design can increase the contact area between the bag and the flue gas dust. Compared with the prior art, the utility model realizes the linkage control of the external desulfurization device and the external bag filter dust collector, reduces the operation intensity of the staff, improves the dust removal efficiency of the external bag filter dust collector to a certain extent; at the same time, it also reduces the degree of ineffective energy consumption. Therefore, it has high practicability.
[0005] To achieve the above object, the utility model provides the following technical solutions:
[0006] A flue gas collaborative purification system for coal-fired units with a coagulation function, comprising:
[0007] A core processing module;
[0008] A flue gas monitoring module for detecting the parameter conditions of the flue gas when entering and leaving the flue gas collaborative purification system of the coal-fired unit, and the output end of the flue gas monitoring module is directly or indirectly connected to the core processing module;
[0009] The collaborative control module is used to select the optimal processing parameters from the external cloud storage database based on the parameters. The collaborative control module is equipped with a dynamic optimization unit, which is connected to the core processing module.
[0010] A dynamic execution module is used to assist the external desulfurization device and the external bag filter device in processing the incoming flue gas according to the optimal processing parameters. The dynamic execution module is connected to the core processing module.
[0011] in,
[0012] The dynamic execution module is equipped with a condensation unit, which can condense the dust in the flue gas entering the external bag filter and convert it into a liquid substance.
[0013] Furthermore, the dynamic execution module includes:
[0014] Atomizing unit;
[0015] The atomizing unit is used to increase the contact area between the desulfurization substance and the flue gas. The atomizing unit is connected to the data communication terminal of the core processing module, that is, the external desulfurization device can perform desulfurization treatment on the flue gas under the action of the atomizing unit.
[0016] Furthermore, the coal-fired unit flue gas co-purification system with condensation function also includes:
[0017] ADC conversion module;
[0018] The ADC conversion module is used to convert analog signals into digital signals. The receiving end of the ADC conversion module is connected to the output end of the flue gas monitoring module, and the output end of the ADC conversion module is connected to the data communication end of the core processing module.
[0019] Furthermore, the collaborative control module includes:
[0020] Parameter adjustment unit;
[0021] The parameter adjustment unit is used to fine-tune the optimal processing parameters. The receiving end of the parameter adjustment unit is connected to the output end of the dynamic optimization unit, and the output end of the parameter adjustment unit is connected to the data communication end of the core processing module.
[0022] Furthermore, the coal-fired unit flue gas co-purification system with condensation function also includes:
[0023] The host computer is connected to the data communication terminal of the core processing module.
[0024] Furthermore, the coal-fired unit flue gas co-purification system with condensation function also includes:
[0025] The mobile communication device is wirelessly connected to the data communication terminal of the host computer.
[0026] Furthermore, the mobile communication device is a smartphone.
[0027] Furthermore, the coal-fired unit flue gas co-purification system with condensation function also includes:
[0028] The LED display's receiving end is connected to the data communication end of the host computer.
[0029] Furthermore, the coal-fired unit flue gas co-purification system with condensation function also includes:
[0030] The alarm's receiver is connected to the data communication terminal of the core processing module.
[0031] Furthermore, the alarm is an audible and visual alarm.
[0032] The beneficial effects of this utility model are:
[0033] 1. The flue gas co-purification system with condensation function provided by this utility model is equipped with a flue gas monitoring module, which can detect the parameters of the flue gas when it enters and leaves this utility model; then, the flue gas monitoring module transmits the parameters to the core processing module. This design can provide the utility model with the corresponding basic information and reduce the consumption of ineffective energy to a certain extent.
[0034] 2. The coal-fired unit flue gas co-processing purification system with condensation function is equipped with a co-processing control module. The dynamic optimization unit in this co-processing control module can receive data on the current flue gas parameters sent by the core processing module and select the optimal processing parameters from the external cloud storage database. Then, the dynamic optimization unit sends the optimal processing parameters to the core processing module, which automatically converts the received data into corresponding control commands and sends them to the dynamic execution module. Then, according to the control commands, the dynamic execution module can automatically assist the external desulfurization device in desulfurization treatment and automatically assist the external bag filter in dust removal treatment. This design can achieve the purpose of purifying flue gas. At the same time, it also realizes the linkage control of the external desulfurization device and the external bag filter, thereby reducing the operational intensity of the staff.
[0035] 3. The coal-fired unit flue gas co-purification system with condensation function is equipped with a condensation unit, which can reduce the temperature of the flue gas entering the external bag filter to near the dew point, condense the dust in the flue gas and convert it into liquid substances. This design can increase the contact area between the filter bag and the flue gas dust, thereby improving the dust removal efficiency of the external bag filter. Attached Figure Description
[0036] Figure 1 This is a general principle block diagram of the present invention;
[0037] Figure 2 This is a schematic diagram of the principle of this utility model in a specific application scenario;
[0038] Figure 3 This is a schematic diagram of the collaborative control module of this utility model.
[0039] Figure 4 This is a schematic diagram of the dynamic execution module of this utility model.
[0040] Figure label:
[0041] 1. Core processing module;
[0042] 2. Flue gas monitoring module;
[0043] 3. ADC conversion module;
[0044] 4. Cooperative control module; 41. Dynamic optimization unit; 42. Parameter adjustment unit;
[0045] 5. Dynamic execution module; 51. Atomization unit; 52. Coagulation unit;
[0046] 6. External processing module;
[0047] 7. Host computer; 71. Mobile communication equipment; 72. LED display;
[0048] 8. Alarm device. Detailed Implementation
[0049] To make the objectives, technical solutions, and advantages of this utility model clearer, the present utility model will be further described in detail below with reference to the embodiments and accompanying drawings. Here, the illustrative embodiments and descriptions of this utility model are used to explain the present utility model, but are not intended to limit the present utility model.
[0050] As attached Figure 1-4As shown, this embodiment discloses a coal-fired unit flue gas co-purification system with condensation function, designed to reduce the operational intensity of workers. It mainly includes a core processing module 1, a flue gas monitoring module 2, a co-control module 4, and a dynamic execution module 5. In use, experienced operators first create various desulfurization and dust removal operation plans based on different flue gas parameters. These plans include the concentration of sulfur dioxide in the flue gas, the concentration of dust in the flue gas, the duration of desulfurization treatment, the number of corresponding desulfurization components to be activated, the duration of dust removal treatment, and the number of corresponding dust removal components to be activated. By adopting the corresponding processing parameters in these operation plans, the flue gas leaving this invention can meet emission standards, thereby achieving the purpose of flue gas purification. These operation plans are constructed into an external cloud storage database (not shown in the figure), which is prior art; the relevant content can be found in publication number C. The existing patent N113050559A; then, the flue gas generated by the coal-fired unit is passed into an external cooling device (not shown in the figure) to cool the flue gas. This design can extend the service life of this embodiment. This external cooling device is prior art, and can be generally referred to as the evaporative cooling component in the existing patent with publication number CN117925286A; next, the flue gas monitoring module 2 can detect the parameters of the flue gas when it enters and leaves this embodiment; among them, the flue gas monitoring module 2 can use laser spectroscopy to detect the concentration of sulfur dioxide in the flue gas in real time and use β-ray method to detect the concentration of dust in the flue gas in real time. This is currently... The relevant technology is available, but the details will not be elaborated here. Then, the flue gas monitoring module 2 transmits the parameter information to the core processing module 1. This design provides the necessary basic information for this embodiment, reducing the waste of ineffective energy to some extent. Next, the core processing module 1 forwards the received data to the collaborative control module 4. Then, the dynamic optimization unit 41 in the collaborative control module 4 receives the data on the current flue gas parameters sent by the core processing module 1 and selects the optimal processing parameters from the external cloud storage database. Finally, the dynamic optimization unit 41 transmits the optimal processing parameters to the core processing module 1. The core processing module 1 automatically converts the received data into corresponding control commands and sends them to the dynamic execution module 5. Then, according to the control commands, the dynamic execution module 5 can automatically assist the external desulfurization device (shown in the figure) in desulfurization treatment and automatically assist the external bag filter device (not shown in the figure) in dust removal treatment. This design allows the flue gas to meet the emission standards after being treated by the external desulfurization device and the external bag filter device, and to a certain extent realizes the linkage control between the external desulfurization device and the external bag filter device. At the same time, this embodiment can also achieve the purpose of purifying flue gas, thereby playing a role in protecting the natural environment.
[0051] In addition, the dynamic execution module 5 includes a condensation unit 52 that assists the external bag filter dust collector. This condensation unit 52 is located on one side of the filter bag (not shown in the figure) and can reduce the temperature of the flue gas entering the external bag filter dust collector to near the dew point, condense the dust in the flue gas and convert it into liquid substances. This design can increase the contact area between the filter bag and the flue gas dust, thereby improving the dust removal efficiency of the external bag filter dust collector. The external bag filter dust collector can be existing technology, and the relevant content can be generally referred to the existing patent with publication number CN220779405U.
[0052] The specific architecture of the coal-fired unit flue gas co-purification system with condensation function is as follows: It includes a core processing module 1, which is used to monitor the operation of other components in this embodiment and the transmission of corresponding data; the data communication terminal of the core processing module 1 is equipped with a flue gas monitoring module 2, which is used to detect the parameters of the flue gas when entering and leaving this embodiment in real time; the co-control module 4 is equipped with a dynamic optimization unit 41, which is connected to the data communication terminal of the core processing module 1, and is used to select the optimal processing parameters from the external cloud storage database according to the parameters detected by the current flue gas monitoring module 2; the data communication terminal of the core processing module 1 is equipped with a dynamic execution module 5, which is used to assist the external desulfurization device and the external bag filter device in processing the flue gas entering this embodiment according to the optimal processing parameters; and the dynamic execution module 5 is equipped with a condensation unit 52, which can condense the dust in the flue gas entering the external bag filter device and convert it into liquid substances. Compared with the prior art, this utility model realizes the linkage control between the external desulfurization device and the external bag filter, which reduces the operating intensity of the staff and improves the dust removal efficiency of the external bag filter to a certain extent; at the same time, it also reduces the consumption of ineffective energy, thus having high practicality.
[0053] In a specific application scenario, as shown in the appendix Figure 1 and appendix Figure 4 As shown, the dynamic execution module 5 is also equipped with an atomization unit 51; wherein, the atomization unit 51 is connected to the data communication terminal of the core processing module 1, that is, under the action of the atomization unit 51, the external desulfurization device can perform desulfurization treatment on the flue gas, and the desulfurized flue gas can move to the external bag filter for corresponding dust removal operation.
[0054] In actual use, the cooled flue gas first enters the external desulfurization device; then, the atomizing unit 51 installed in the external desulfurization device can desulfurize the flue gas according to the aforementioned optimal processing parameters. In this process, the atomizing unit 51 can increase the contact area between the desulfurizing substance and the flue gas. This design can assist the external desulfurization device in desulfurization, thereby improving the desulfurization effect of this embodiment. The atomizing unit 51 can be several dual-fluid nozzles, and the desulfurizing substance is usually lime slurry. Specifically, the dual-fluid nozzles are supplied with compressed air by an external air compressor (not shown in the figure). Under the action of the compressed air, the lime slurry in the dual-fluid nozzles is atomized. This design allows the lime slurry to be dispersed in the desulfurization device in an atomized form, thereby improving the atomization effect of this embodiment and achieving the purpose of semi-dry desulfurization. In addition, the optimal processing parameters usually include indicators of the number and duration of operation of the dual-fluid nozzles in the atomizing unit 51, thereby adapting to the flue gas entering the external desulfurization device and reducing the consumption of ineffective energy to a certain extent.
[0055] In a specific application scenario, the aforementioned condensation unit 52 can be several condensing heat exchangers. Typically, the outlet of the external desulfurization device is connected to the inlet of the external bag filter, meaning that after desulfurization, the flue gas can move to the external bag filter via the external desulfurization device. Then, the condensing heat exchangers can cool the flue gas entering the external bag filter. During this process, the condensing heat exchangers can release water vapor, which condenses into droplets. These droplets can combine with dust in the flue gas to form liquid substances, thereby increasing the contact area between the dust in the flue gas and the filter bags. Of course, a waterproof layer can be installed on the outer surface of the filter bags; this design can prevent the circuitry inside the filter bags from being affected. Furthermore, the optimal processing parameters typically include indicators for the number and duration of operation of the condensing heat exchangers in the condensation unit 52, adapting to the current flue gas conditions entering the external bag filter and reducing the consumption of ineffective energy to some extent.
[0056] In a specific application scenario, as shown in the appendix Figure 2 As shown, the output end of the aforementioned flue gas monitoring module 2 is equipped with an ADC conversion module 3, and the output end of the ADC conversion module 3 is connected to the data communication end of the core processing module 1.
[0057] In practical use, the flue gas monitoring module 2 can transmit the detected data to the ADC conversion module 3. Normally, the data transmitted by the flue gas monitoring module 2 is an analog signal, which is generally difficult for the core processing module 1 to identify. However, the ADC conversion module 3 can convert the analog signal data into a digital signal. Then, the ADC conversion module 3 transmits the converted data to the core processing module 1. This design facilitates the core processing module 1 in analyzing the corresponding data in this embodiment and ensures the normal operation of this embodiment to a certain extent.
[0058] In a specific application scenario, as shown in the appendix Figure 2 and appendix Figure 3 As shown, the collaborative control module 4 is provided with a parameter adjustment unit 42; wherein, the receiving end of the parameter adjustment unit 42 is connected to the output end of the dynamic optimization unit 41, and the output end of the parameter adjustment unit 42 is connected to the data communication end of the core processing module 1.
[0059] In actual use, the dynamic execution module 5 has already performed corresponding desulfurization and dust removal treatment on the flue gas currently entering this embodiment; however, the flue gas monitoring module 2 detects that the flue gas leaving this embodiment still does not meet the emission standards and needs to undergo a second desulfurization and dust removal treatment; typically, the data communication terminal of the core processing module 1 is also equipped with an external processing module 6; specifically, a three-way pipe (not shown in the figure) is set at the outlet end of the external bag filter dust collector, and the three-way pipe has a first outlet end and a second outlet end, and a first valve is set near the first outlet end of the three-way pipe, and a second valve is set near the second outlet end of the three-way pipe, and the first valve... Both the receiving ends of the first and second valves are connected to the data communication end of the core processing module 1, and the first outlet end of the three-way pipe is connected to the inlet end of the external processing module 6. When the flue gas entering this embodiment needs to undergo secondary desulfurization and dust removal treatment, the core processing module 1 sends an opening command to the external processing module 6 and the first valve, and sends a closing command to the second valve. That is, the non-compliant flue gas can enter the external processing module 6 through the first outlet end of the three-way pipe for secondary desulfurization and dust removal treatment. This design can prevent the non-compliant flue gas from being discharged into nature through the second outlet end of the three-way pipe, thereby achieving the effect of protecting the natural environment.
[0060] Meanwhile, the flue gas monitoring module 2 transmits the relevant parameters of the flue gas subsequently entering this embodiment to the dynamic optimization unit 41 via the ADC conversion module 3 and the core processing module 1. Then, the dynamic optimization unit 41 transmits the received data and the current optimal processing parameters to the parameter adjustment unit 42. Next, the parameter adjustment unit 42 fine-tunes the current optimal processing parameters based on the data sent by the dynamic optimization unit 41. Then, the parameter adjustment unit 42 transmits the adjusted processing parameters to the core processing module 1, which then sends the corresponding control commands to the dynamic execution module 5, that is, to make the corresponding number of dual-fluid nozzles work continuously. The corresponding number of condensing heat exchangers are operated for the corresponding time and for the corresponding duration until the flue gas in this embodiment can be discharged from the second outlet of the three-way pipe. That is, the flue gas in this embodiment does not need to undergo a second desulfurization and dust removal treatment. The core processing module 1 sends an opening command to the second valve and a closing command to the external processing module 6 and the first valve. In actual use, the desulfurization device and the bag filter dust collector in the background technology can be used together as the external processing module 6 to achieve a second desulfurization and dust removal treatment. Under normal circumstances, the flue gas in this embodiment can meet the emission standards after two desulfurization and dust removal treatments. In addition, the parameter adjustment unit 42 can send the last adjusted processing parameters to an external cloud storage database to correct the processing parameters of the corresponding operation plan. If the same situation is encountered again, when the collaborative control module 4 retrieves the optimal processing parameters from the external cloud storage database, the corrected processing parameters can be used as the optimal processing parameters for the current flue gas situation. This design avoids multiple adjustment operations and improves the working efficiency of this embodiment to a certain extent. At the same time, it also reduces the degree of waste energy consumption in this embodiment. Because during the second desulfurization and dust removal treatment, the desulfurization device and the bag filter dust collector operate as two independent devices, the problem of waste energy consumption is more prominent. On the other hand, the dynamic optimization unit 41 and the parameter adjustment unit 42 work together to jointly adjust the operating status of the corresponding components in the dynamic execution module 5.
[0061] This embodiment takes into account a situation, as shown in the attached figure. Figure 2-4As shown, the specific solution is as follows: A host computer 7 is set up at the data communication terminal of the core processing module 1. Experienced operators can quickly input data to the core processing module 1 to correct the processing parameters in the corresponding operation plan through the host computer 7. Then, the core processing module 1 transmits the corrected information to the parameter adjustment unit 42 via the dynamic optimization unit 41, causing the parameter adjustment unit 42 to stop its own fine-tuning and instead retrieve the latest corrected processing parameters from the external cloud storage database. This processing parameter is then used as the current optimal processing parameter and transmitted to the dynamic execution module 5 via the core processing module 1. The dynamic execution module 5 then assists the external desulfurization device and the external bag filter. The dust removal device performs desulfurization and dust removal treatment on the flue gas entering this embodiment. This design reduces the working time of the external processing module 6, thereby reducing the consumption of ineffective energy. Typically, the core processing module 1 can directly transmit the corresponding data to an external cloud storage database, replacing the original processing parameters. This design enables the correction of processing parameters for the corresponding operation plan. Simultaneously, the core processing module 1 can feed back the data it receives to the host computer 7, allowing staff to access the data generated during the operation of this embodiment via the host computer 7, thus providing convenience for data analysis. A mobile communication device 71, which can be a smartphone, is wirelessly installed at the data communication terminal of the host computer 7. Experienced staff can remotely send data to the core processing module 1 via the host computer 7 to correct the processing parameters of the corresponding operation plan, thereby achieving remote control and improving work efficiency to a certain extent. An LED display 72 is installed at the data communication terminal of the host computer 7. This LED display 72 can display the data received by the host computer 7 from the core processing module 1. This design makes it easier for staff to find the relevant data more quickly and accurately, and then analyze and process the data to obtain the basis and evidence for correcting the processing parameters of the corresponding operation plan. An alarm 8 is installed at the data communication terminal of the core processing module 1. This alarm 8 can be an audible and visual alarm. If the core processing module 1 finds that the optimal processing parameters have been adjusted multiple times and the flue gas leaving this embodiment needs to undergo secondary desulfurization and dust removal treatment, the core processing module 1 will issue a start-up command to the audible and visual alarm, alerting nearby staff with more operating experience to manually correct the current processing parameters, thereby avoiding the external processing module 6 from working for a long time and reducing the consumption of ineffective energy to a certain extent.Furthermore, if several dual-flow nozzles and condenser heat exchangers in the dynamic execution module 5 malfunction, the dynamic execution module 5 feeds back the corresponding information to the core processing module 1. The core processing module 1 can also send a start-up command to the audible and visual alarm, alerting experienced personnel nearby to inspect this embodiment. If the personnel find that the flue gas desulfurization and dust removal are normal, meaning the flue gas leaving this embodiment has not undergone secondary desulfurization and dust removal, then the personnel will check the damage to the dual-flow nozzles and condenser heat exchangers to replace them. This design maintains the normal operation of this embodiment to a certain extent. Before replacing components, the personnel should stop the operation of this embodiment to prevent flue gas from entering, thereby ensuring the personnel's safety. Of course, considering temperature factors, the personnel can use high-temperature resistant materials to manufacture the corresponding components in this embodiment, thereby extending the service life of this embodiment. The circuit structures described above all fall within the scope of existing technology. The innovation of this utility model lies only in the optimization design of the overall system architecture and does not involve improvements to specific circuit structures.
[0062] The above description is merely an optional embodiment of this utility model and is not intended to limit the utility model. For those skilled in the art, various modifications and variations can be made to the embodiments of this utility model. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of this utility model should be included within the protection scope of this utility model.
Claims
1. A coal-fired power unit flue gas co-purification system with condensation function, characterized in that, include: The system comprises: a core processing module (1); a flue gas monitoring module (2) for detecting the parameters of flue gas entering and leaving the coal-fired unit's flue gas co-purification system; the output of the flue gas monitoring module (2) is directly or indirectly connected to the core processing module (1); a co-control module (4) for selecting the optimal processing parameters from an external cloud storage database based on the parameters; a dynamic optimization unit (41) is provided in the co-control module (4) and is connected to the core processing module (1); a dynamic execution module (5) for assisting the external desulfurization device and the external bag filter device in processing the incoming flue gas based on the optimal processing parameters; the dynamic execution module (5) is connected to the core processing module (1); and a condensation unit (52) is provided in the dynamic execution module (5), which can condense the dust in the flue gas entering the external bag filter device and convert it into liquid substances.
2. The coal-fired unit flue gas co-purification system with condensation function according to claim 1, characterized in that, The dynamic execution module (5) includes: an atomizing unit (51); the atomizing unit (51) is used to increase the contact area between the desulfurization substance and the flue gas. The atomizing unit (51) is connected to the data communication terminal of the core processing module (1). That is, the external desulfurization device can perform desulfurization treatment on the flue gas under the action of the atomizing unit (51).
3. The coal-fired unit flue gas co-purification system with condensation function according to claim 1, characterized in that, Also includes: ADC conversion module (3); The ADC conversion module (3) is used to convert analog signals into digital signals. The receiving end of the ADC conversion module (3) is connected to the output end of the flue gas monitoring module (2), and the output end of the ADC conversion module (3) is connected to the data communication end of the core processing module (1).
4. The coal-fired unit flue gas co-purification system with condensation function according to any one of claims 1-3, characterized in that, The collaborative control module (4) includes: a parameter adjustment unit (42); the parameter adjustment unit (42) is used to fine-tune the optimal processing parameters, the receiving end of the parameter adjustment unit (42) is connected to the output end of the dynamic optimization unit (41), and the output end of the parameter adjustment unit (42) is connected to the data communication end of the core processing module (1).
5. The coal-fired unit flue gas co-purification system with condensation function according to claim 4, characterized in that, Also includes: The host computer (7) is connected to the data communication terminal of the core processing module (1).
6. The coal-fired unit flue gas co-purification system with condensation function according to claim 5, characterized in that, Also includes: The mobile communication device (71) is wirelessly connected to the data communication terminal of the host computer (7).
7. The coal-fired unit flue gas co-purification system with condensation function according to claim 6, characterized in that, The mobile communication device (71) is a smartphone.
8. The coal-fired unit flue gas co-purification system with condensation function according to claim 6 or claim 7, characterized in that, Also includes: The LED display (72) has its receiving end connected to the data communication end of the host computer (7).
9. The coal-fired unit flue gas co-purification system with condensation function according to any one of claims 5-7, characterized in that, Also includes: The alarm (8) is connected to the data communication terminal of the core processing module (1).
10. The flue gas co-purification system for coal-fired power units with condensation function according to claim 9, characterized in that, The alarm (8) is an audible and visual alarm.