An online calculation system and method for characterizing CO2 consumption during operation of dry electrostatic precipitator
By introducing a data monitoring and processing unit into the dry electrostatic precipitator, online calculation and optimization of CO2 consumption are achieved, solving the problem that traditional equipment cannot monitor CO2 emissions and improving the energy-saving and carbon-reduction capabilities of the equipment.
Patent Information
- Application Number
- CN202111133036.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2021-09-27
- Publication Date
- 2025-09-26
- Estimated Expiration
- 2041-09-27
AI Technical Summary
Traditional dry electrostatic precipitators are unable to monitor CO2 emissions, resulting in an inability to effectively reduce energy consumption and carbon emissions.
An online accounting system for CO2 consumption during the operation of a dry electrostatic precipitator is designed. The system includes data monitoring, transmission and processing units. The system monitors and displays CO2 consumption through conversion functions and can adjust operating parameters to optimize CO2 consumption.
It realizes real-time monitoring and optimization of CO2 emissions, reduces energy consumption and carbon emissions, and improves the energy-saving and carbon-reduction efficiency of equipment.
Smart Images

Figure CN113941446B_ABST
Abstract
Description
Technical field
[0001] The present invention relates to the technical field of dust removal equipment, and in particular to an online accounting system and method for characterizing CO2 consumption during operation of a dry-type electrostatic precipitator. [Background Technology]
[0002] At present, the mainstream equipment for treating flue gas particulate matter in coal-fired power plants at home and abroad is dry electrostatic precipitator. Dry electrostatic precipitator is a dust collector that removes ash from flue gas and discharges it in dry state. It releases a high-intensity electric field through electrodes. Under the action of the electric field force, the charged dust is collected by the cathode and anode devices. The anode plate adopts parallel suspended metal plates, while the cathode can be top-mounted or side-mounted according to the actual situation of the project.
[0003] Traditional dry electrostatic precipitators can only monitor pollutant emissions and operating parameters, but cannot monitor and characterize CO2 emissions, which is not conducive to energy conservation and carbon reduction of pollution reduction equipment. This paper proposes an online accounting system and method for characterizing CO2 consumption during operation of dry electrostatic precipitators. [Summary of the invention]
[0004] The purpose of the present invention is to solve the problems in the prior art and to propose an online accounting system and method for characterizing CO2 consumption during operation of a dry electrostatic precipitator, which can monitor and characterize CO2 emissions.
[0005] To achieve the above-mentioned objectives, the present invention proposes an online accounting system for characterizing the CO2 consumption during the operation of a dry electrostatic precipitator, comprising a dry electrostatic precipitator, a data monitoring unit, a data transmission unit, and a data processing and display unit. The data monitoring unit is used to monitor the energy consumption data of the dry electrostatic precipitator during operation. The data monitoring unit is communicatively connected to the data processing and display unit through the data transmission unit. The data processing and display unit includes a processor and a display communicatively connected to the processor. The processor is used to receive the data monitored by the data monitoring unit and convert it into CO2 consumption data. The display is used to display the CO2 consumption data converted by the processor.
[0006] Preferably, the processor is preset with control logic and calculation functions for converting the data monitored by the data monitoring unit into CO2 consumption data.
[0007] Preferably, the data processing and display unit also includes a controller and an operation input device communicatively connected to the processor, the controller is used to adjust the operating mode and parameters of the dry electrostatic precipitator to change the CO2 consumption, and the operation input device is used to manually input the operating mode and parameters of the dry electrostatic precipitator.
[0008] Preferably, the dry electrostatic precipitator includes a cathode system, an anode system, a high-voltage power supply device, a low-voltage power supply device, a vibration system, an ash conveying system, and an ash hopper insulation system.
[0009] Preferably, the data monitoring unit includes an electric energy meter for monitoring the power consumption of the high-voltage power supply device, a pressure gauge for monitoring the resistance of the dry electrostatic precipitator, and an electric energy meter for monitoring the power consumption of the low-voltage power supply device.
[0010] Preferably, the data transmission unit includes a transmission wire and a wireless network. The processor is communicatively connected to the data monitoring unit and the display through the transmission wire. The transmission wire is used to transmit the data monitored by the data monitoring unit to the processor, and to transmit the data converted by the processor to the display. The wireless network is used to transmit the data converted by the processor to the mobile terminal in real time.
[0011] The present invention also proposes an online calculation method for characterizing CO2 consumption during operation of a dry electrostatic precipitator. The method uses the following conversion function to calculate CO2 consumption:
[0012] F=eTP e (E h +E l +E p ) / P c
[0013] Among them, F is the CO2 consumption of the dry electrostatic precipitator during operation, e is the coal consumption conversion coefficient; T is the operating time; Pe and Pc are the electricity price and coal price respectively; E h 、E l 、E p They are high voltage power consumption, low voltage power consumption and resistance power consumption respectively.
[0014] As a preferred option, the resistance power consumption E p The calculation formula is as follows:
[0015]
[0016] Among them, Q is the flue gas volume at the inlet of the dry electrostatic precipitator, and P is the resistance of the dry electrostatic precipitator.
[0017] The present invention provides the following beneficial effects: The data monitoring unit monitors the energy consumption of the dry electrostatic precipitator during operation, converts it into CO2 consumption using control logic and calculation functions pre-set in the data processing and display unit, and ultimately displays it on a display. Furthermore, the controller can adjust relevant parameters to vary CO2 consumption, achieving the lowest CO2 consumption while ensuring pollutant emissions meet standards.
[0018] The features and advantages of the present invention will be described in detail through embodiments with reference to the accompanying drawings.
Brief Description of the Drawings
[0019] Figure 1This is a block diagram of an online calculation system for CO2 consumption during operation of a dry electrostatic precipitator according to the present invention;
[0020] Figure 2 It is a coal consumption conversion coefficient corresponding to different types of coal in the online calculation method of CO2 consumption in the operation of a dry electrostatic precipitator of the present invention, wherein the value corresponding to the standard coal carbon dioxide emission coefficient is the coal consumption conversion coefficient e of different types of coal. [Specific implementation method]
[0021] See Figure 1 The present invention provides an online accounting system for characterizing the CO2 consumption during the operation of a dry electrostatic precipitator, comprising a dry electrostatic precipitator 1, a data monitoring unit 2, a data transmission unit 3, and a data processing and display unit 4. The data monitoring unit 2 is used to monitor the energy consumption data consumed during the operation of the dry electrostatic precipitator 1. The data monitoring unit 2 is communicatively connected to the data processing and display unit 4 through the data transmission unit 3. The data processing and display unit 4 includes a processor and a display communicatively connected to the processor. The processor is preset with control logic and calculation functions. The processor is used to receive the data monitored by the data monitoring unit 2 and convert it into CO2 consumption data. The display is used to display the CO2 consumption data converted by the processor.
[0022] Furthermore, the data processing and display unit 4 also includes a controller and an operation input device that are communicatively connected to the processor. The controller is used to adjust the operating mode and parameters of the dry electrostatic precipitator 1 to change the CO2 consumption. The controller has multiple operating modes, including maximum output mode, general operating mode, energy-saving and carbon reduction mode, etc. Different modes correspond to different CO2 consumption. The operator can set the mode to automatic operation or switch to manual control. The operation input device is used to manually input the operating mode and parameters of the dry electrostatic precipitator 1, and the manual input method has a specific account and identity recognition function. For junior operators, there will be an automatic interface prompt function when entering various parameters or modes.
[0023] Furthermore, the dry electrostatic precipitator 1 includes inlet and outlet heads, a cathode system, an anode system, a high-voltage power supply device, a low-voltage power supply device, a vibration system, an ash conveying system, and an ash hopper insulation system, wherein the high-voltage power supply device supplies power to the cathode system and the anode system, and the low-voltage power supply device supplies power to the vibration system, the ash conveying system, and the ash hopper insulation system.
[0024] Furthermore, the data monitoring unit 2 includes an electric energy meter for monitoring the power consumption of the high-voltage power supply device, a pressure gauge for monitoring the resistance of the dry electrostatic precipitator 1, and an electric energy meter for monitoring the power consumption of low-voltage power supply devices such as the rapping motor of the rapping system, the ash conveying pump of the ash conveying system, and the electric heating of the ash hopper insulation system.
[0025] Furthermore, the data transmission unit 3 includes a transmission wire and a wireless network. The processor is respectively connected to the data monitoring unit 2 and the display through the transmission wire. The transmission wire is used to transmit the data monitored by the data monitoring unit 2 to the processor, and to transmit the data converted by the processor to the display. The wireless network is used to transmit the data converted by the processor to the mobile terminal in real time.
[0026] The system of the present invention uses the following conversion function to calculate CO2 consumption:
[0027] F=eTP e (E h +E l +E p ) / P c
[0028] Among them, F is the CO2 consumption during the operation of the dry electrostatic precipitator, e is the coal consumption conversion coefficient, and the coal consumption conversion coefficient e of different coal types is as follows: Figure 2 As shown; T is the operating time; Pe and Pc are electricity price and coal price respectively; E h 、E l 、E p They are high voltage power consumption, low voltage power consumption and resistance power consumption, among which high voltage power consumption and low voltage power consumption are measured by electric energy meter; resistance power consumption E p The calculation formula is as follows:
[0029]
[0030] Among them, Q is the flue gas volume at the inlet of the dry electrostatic precipitator, and P is the resistance of the dry electrostatic precipitator.
[0031] The above embodiments are intended to illustrate the present invention, not to limit the present invention. Any solution that is a simple transformation of the present invention falls within the protection scope of the present invention.
Claims
1. A method for calculating CO2 consumption in an online calculation system for a dry electrostatic precipitator, characterized by: An online accounting system for characterizing CO2 consumption during operation of a dry-type electrostatic precipitator is used. The online accounting system comprises a dry-type electrostatic precipitator (1), a data monitoring unit (2), a data transmission unit (3), and a data processing and display unit (4). The data monitoring unit (2) is used to monitor energy consumption data during operation of the dry-type electrostatic precipitator (1). The data monitoring unit (2) is communicatively connected to the data processing and display unit (4) via the data transmission unit (3). The data processing and display unit (4) comprises a processor and a display communicatively connected to the processor. The processor is used to receive data monitored by the data monitoring unit (2) and convert it into CO2 consumption data. The display is used to display the CO2 consumption data converted by the processor. The processor is pre-set with control logic and calculation functions for converting the data monitored by the data monitoring unit (2) into CO2 consumption data; The data processing and display unit (4) further comprises a controller and an operation input device in communication with the processor, wherein the controller is used to adjust the operation mode and parameters of the dry electrostatic precipitator (1) to change the CO2 consumption, and the operation input device is used to manually input the operation mode and parameters of the dry electrostatic precipitator (1); The controller has multiple operating modes, including maximum output mode, normal operation mode, and energy-saving and carbon-reduction mode. Different modes correspond to different CO2 consumption. Operators can set the mode to automatic operation or switch to manual control. The manual input method has a specific account and identity recognition function, and for junior operators, there will be an automatic interface prompt function when entering various parameters or modes. The dry electrostatic precipitator (1) comprises a cathode system, an anode system, a high-voltage power supply device, a low-voltage power supply device, a vibration system, an ash conveying system, and an ash hopper insulation system; The data monitoring unit (2) includes an electric energy meter for monitoring the power consumption of the high-voltage power supply device, a pressure gauge for monitoring the resistance of the dry electrostatic precipitator (1), and an electric energy meter for monitoring the power consumption of the low-voltage power supply device; the data transmission unit (3) includes a transmission wire and a wireless network, and the processor is respectively connected to the data monitoring unit (2) and the display through the transmission wire. The transmission wire is used to transmit the data monitored by the data monitoring unit (2) to the processor and to transmit the data converted by the processor to the display. The wireless network is used to transmit the data converted by the processor to the mobile terminal in real time; The calculation method uses the following conversion function to calculate CO2 consumption: F=eTP e (TO h +E l +E p ) / P c Among them, F is the CO2 consumption of the dry electrostatic precipitator during operation, e is the coal consumption conversion coefficient; T is the operating time; Pe and Pc are the electricity price and coal price respectively; E h 、E l 、E p They are high voltage power consumption, low voltage power consumption and resistance power consumption respectively; Resistance power consumption E p The calculation formula is as follows: Among them, Q is the flue gas volume at the inlet of the dry electrostatic precipitator, and P is the resistance of the dry electrostatic precipitator.
Citation Information
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