阅读说明：本技术 空冷岛热态冲洗时的蒸汽流量计算方法、装置及终端设备 (Steam flow calculation method and device during hot flushing of air cooling island and terminal equipment ) 是由 杜威 王志强 李路江 李晖 唐广通 杨海生 于 2021-06-07 设计创作，主要内容包括：本发明适用于空冷岛技术领域,提供了一种空冷岛热态冲洗时的蒸汽流量计算方法、装置及终端设备,该方法包括：获取空冷岛在校核工况下的试验数据,并根据校核工况下的试验数据计算所述空冷岛的污垢热阻；获取空冷岛在热态冲洗时目标凝汽器列的监测数据,目标凝汽器列为所述空冷岛内的任一凝汽器列；根据污垢热阻和所述监测数据,计算目标凝汽器列的换热系数；根据换热系数计算所述目标凝汽器列的换热量。本发明提供的方法可以根据空冷岛的污垢热阻准确计算空冷岛热态冲洗时中各个凝汽器列中的蒸汽流量,为空冷岛热态冲洗过程的控制与调整提供依据,从而缩短空冷岛热态清洗的时间,节省蒸汽的消耗,改善清洗效果,提高清洗效率。(The invention is suitable for the technical field of air cooling islands, and provides a method, a device and terminal equipment for calculating steam flow during hot flushing of an air cooling island, wherein the method comprises the following steps: acquiring test data of the air cooling island under a checking condition, and calculating fouling thermal resistance of the air cooling island according to the test data under the checking condition; acquiring monitoring data of a target condenser row when the air cooling island is flushed in a hot state, wherein the target condenser row is any one condenser row in the air cooling island; calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data; and calculating the heat exchange quantity of the target condenser array according to the heat exchange coefficient. The method provided by the invention can accurately calculate the steam flow in each condenser row during the hot washing of the air cooling island according to the dirt thermal resistance of the air cooling island, and provides a basis for controlling and adjusting the hot washing process of the air cooling island, thereby shortening the hot washing time of the air cooling island, saving the consumption of steam, improving the washing effect and improving the washing efficiency.)

1. A steam flow calculation method during hot flushing of an air cooling island is characterized in that the air cooling island comprises at least one group of condenser rows; the method comprises the following steps:

acquiring test data of the air cooling island under a checking working condition, and calculating fouling thermal resistance of the air cooling island according to the test data under the checking working condition;

acquiring monitoring data of a target condenser row when the air cooling island is flushed in a hot state; the target condenser column is any condenser column in the air cooling island;

calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data;

calculating the heat exchange quantity of the target condenser array according to the heat exchange coefficient;

and calculating the steam flow of the target condenser column according to the heat exchange amount.

2. The method for calculating the steam flow during the hot flushing of the air cooling island according to claim 1, wherein the calculating the fouling resistance of the air cooling island according to the test data comprises the following steps:

calculating the number of heat transfer units of the air cooling island according to the test data and a heat transfer unit number calculation formula;

calculating the heat exchange coefficient of the air cooling island under the checking working condition according to the number of the heat transfer units and a first heat exchange coefficient calculation formula;

calculating the fouling thermal resistance of the air cooling island according to a calculation formula of the heat exchange coefficient and the fouling thermal resistance of the air cooling island under the checking working condition;

the heat transfer unit number calculation formula is as follows:

wherein NTU is the number of heat transfer units, Q_pIs the heat released by the steam, t_s1To check the temperature of the condensate in the operating mode, t_a1To check the inlet cold air temperature under operating conditions, D_a1For checking the inlet air quantity under operating conditions, C_pa1The specific heat capacity of the cold air under the checking working condition is constant pressure, and rho is the density of the cold air under the checking working condition;

the first heat exchange coefficient calculation formula is as follows:

k is the heat exchange coefficient of the air cooling island under the checking working condition, and A is the heat exchange area of the air cooling island;

the fouling thermal resistance calculation formula is as follows:

wherein R is_fThermal resistance to fouling, K₀And designing the heat exchange coefficient for the air cooling island.

3. The method for calculating the steam flow during the hot flushing of the air cooling island according to claim 1, wherein the target condenser row comprises a stopped condenser row, and the monitoring data comprises an on-face wind speed; the monitoring data who obtains target condenser row includes:

the method comprises the following steps: initializing the head-on wind speed, and taking the initialized head-on wind speed as the current head-on wind speed;

step two: calculating a judgment difference corresponding to the current head-on wind speed according to the current head-on wind speed and a judgment difference calculation formula;

step three: comparing the judgment difference value corresponding to the current head-on wind speed with the judgment threshold value, if the judgment difference value corresponding to the current head-on wind speed is larger than or equal to the judgment threshold value, increasing the current head-on wind speed according to a preset step length, and updating the current head-on wind speed in the second step by adopting the increased head-on wind speed; repeatedly executing the second step to the third step until the judgment difference value is smaller than the judgment threshold value;

step four: if the judgment difference value corresponding to the current head-on wind speed is smaller than the judgment threshold value, taking the current head-on wind speed as the head-on wind speed of the condenser row which stops running;

the judgment difference value calculation formula is as follows:

wherein, Delta is a judgment difference value, Q_pIs the heat released by the steam, t_s1tTemperature of condensate for stopping condenser train operation, t_a1tInlet cold air temperature for the condenser row to be stopped, A_yTo stop the frontal area of the condenser row, v_tHead-on wind speed for stopping condenser train operation, C_pa1tFor stopping the cold air of the condenser row at a constant pressure and specific heat capacity, rho_tIn order to stop the cold air density of the condenser row, A is the heat exchange area of the air cooling island; alpha is alpha_iIs the steam side heat exchange coefficient under the reference working condition, A_iIs the steam side heat exchange area, delta is the tube wall thickness, A_mFor measuring heat transfer area, alpha, of the tube wall_oIs the air side heat exchange coefficient eta under the reference working condition_oFor fin heat exchange efficiency, v_tHead-on wind speed, v, for stopping operation of the condenser bank_oThe head-on wind speed of the air cooling condenser row under the reference working condition.

4. The method for calculating the steam flow during the hot flushing of the air cooling island according to any one of claims 1 to 3, wherein the monitoring data comprises: the heat exchange area of the air cooling island, the heat exchange area of the steam side, the heat exchange area of the pipe wall, the heat exchange area of the air side, the heat exchange efficiency of fins of the air cooling island, the thermal resistance of dirt, the heat exchange coefficient of the air side under a reference working condition, the head-on wind speed under the reference working condition, the heat exchange coefficient of the steam side under the current working condition, the heat conductivity coefficient of the pipe wall under the current working condition and the heat exchange coefficient of the air side under the current working condition;

calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data, wherein the calculation comprises the following steps:

substituting the monitoring data into a second heat exchange coefficient calculation formula, and calculating the heat exchange coefficient of the target condenser row;

the second heat exchange coefficient calculation formula is as follows:

wherein K' is the heat exchange coefficient of the target condenser row, A is the heat exchange area of the air cooling island, and alpha_i' is the steam side heat transfer coefficient under the current working condition, A_iIs the heat exchange area of the steam side, lambda' is the heat conductivity coefficient of the pipe wall under the current working condition, A_mIs the heat exchange area of the pipe wall, delta is the pipe wall thickness of the air cooling island, alpha_o' is the air side heat transfer coefficient under the current working condition, A_oIs the air side heat exchange area, eta_oFor air cooling island fin heat exchange efficiency, R_fIs fouling resistance; alpha is alpha_oIs the air side heat exchange coefficient v under the reference working condition_o' is the head-on wind speed under the current working condition, v_oIs the head-on wind speed under the reference working condition.

5. The method for calculating the steam flow during the hot flushing of the air cooling island according to claim 1, wherein the calculating the heat exchange amount of the target condenser row according to the heat exchange coefficient includes:

calculating the heat exchange quantity of the target condenser array according to a heat exchange quantity calculation formula and the heat exchange coefficient;

the heat exchange quantity calculation formula is as follows:

wherein Q is_p' is the heat exchange quantity of the target condenser row under the current working condition, t_s1' is the temperature of the condensate water under the current operating conditions, t_a1' is the inlet cold air temperature under the current operating condition, D_a1' is the inlet air quantity under the current working condition, C_pa1The specific heat capacity of cold air at constant pressure under the current working condition is ' shown, rho ' is the density of the cold air under the current working condition, K ' is the heat exchange coefficient of the target condenser row, and A is the heat exchange area of the air cooling island.

6. The method for calculating the steam flow during the hot flushing of the air cooling island according to claim 1, wherein the calculating the steam flow of the target condenser row according to the heat exchange amount comprises:

calculating the steam flow of the target condenser row according to a steam flow calculation formula and the heat exchange amount;

the steam flow calculation formula is as follows:

wherein D is_p' is the steam flow of the target condenser row under the current working condition, Q_p' is the heat exchange quantity of the target condenser row under the current working condition, h_p' is the inlet enthalpy under the current working condition, h_s1' is the enthalpy of the condensed water under the current operating conditions.

7. A steam flow calculation device for hot flushing of an air cooling island is characterized by comprising:

the fouling thermal resistance acquisition module is used for acquiring test data of the air cooling island under a checking working condition and calculating fouling thermal resistance of the air cooling island according to the test data under the checking working condition;

the monitoring data acquisition module is used for acquiring monitoring data of a target condenser column when the air cooling island is flushed in a hot state; the target condenser column is any condenser column of the air cooling island;

the heat exchange coefficient calculation module is used for calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data;

the heat exchange quantity calculation module is used for calculating the heat exchange quantity of the target condenser array according to the heat exchange coefficient;

and the steam flow calculation module is used for calculating the steam flow of the target condenser column according to the heat exchange amount.

8. The apparatus for calculating vapor flow during hot flushing of an air cooling island according to claim 7, wherein the fouling thermal resistance obtaining module comprises:

the heat transfer unit number calculation unit is used for calculating the heat transfer unit number of the air cooling island according to the test data and a heat transfer unit number calculation formula;

the checking working condition heat exchange coefficient calculation unit is used for calculating the heat exchange coefficient of the air cooling island under the checking working condition according to the number of the heat transfer units and a first heat exchange coefficient calculation formula;

the fouling thermal resistance calculation unit is used for calculating the fouling thermal resistance of the air cooling island according to the heat exchange coefficient and the fouling thermal resistance calculation formula of the air cooling island under the checking working condition;

the heat transfer unit number calculation formula is as follows:

wherein NTU is the number of heat transfer units, Q_pIs the heat released by the steam, t_s1To check the temperature of the condensate in the operating mode, t_a1To check the inlet cold air temperature under operating conditions, D_a1For checking the inlet air quantity under operating conditions, C_pa1The specific heat capacity of the cold air under the checking working condition is constant pressure, and rho is the density of the cold air under the checking working condition;

the first heat exchange coefficient calculation formula is as follows:

k is the heat exchange coefficient of the air cooling island under the checking working condition, and A is the heat exchange area of the air cooling island;

the fouling thermal resistance calculation formula is as follows:

wherein R is_fThermal resistance to fouling, K₀And designing the heat exchange coefficient for the air cooling island.

9. A terminal device comprising a memory, a processor and a computer program stored in the memory and executable on the processor, characterized in that the processor implements the steps of the method according to any of claims 1 to 6 when executing the computer program.

10. A computer-readable storage medium, in which a computer program is stored which, when being executed by a processor, carries out the steps of the method according to any one of claims 1 to 6.

Technical Field

The invention belongs to the technical field of air cooling islands, and particularly relates to a method and a device for calculating steam flow during hot flushing of an air cooling island and terminal equipment.

Background

The direct air cooling unit needs to be cooled through an air cooling island, the air cooling island comprises a main steam exhaust pipeline, a steam distribution pipe, a condensed water collecting system, a lifting type steel platform, an auxiliary system and a plurality of air cooling condenser rows, and each air cooling condenser consists of a plurality of cooling units with finned tube heat exchangers. The inner surfaces of the pipeline of the air cooling island and the heat exchanger can have impurities such as rust, welding slag, dust and dirt, and the like, so that the pipeline and the heat exchanger are flushed in a hot state through steam before the direct air cooling unit is started integrally to remove the impurities in the system in order to avoid the impurities from entering a condensed water system. Usually, each air-cooled condenser row needs to be washed intermittently for 2 to 4 times so as to enable the washed condensed water to meet the standard.

Due to the structural limitation of the air cooling island, in the hot washing process, a plurality of rows of air cooling condensers are simultaneously connected, the steam flow in each condenser row can only be calculated and adjusted according to experience, the steam distribution is unreasonable, the pertinence of the washing process is poor, long-time low-flow washing is easy to occur, the waste of hot steam is caused, a large amount of time is occupied, and the efficiency is low.

Disclosure of Invention

In view of this, embodiments of the present invention provide a method and an apparatus for calculating a steam flow during hot flushing of an air cooling island, and a terminal device, so as to solve the problem in the prior art that the steam flow calculation accuracy in each air cooling condenser row is poor.

The first aspect of the embodiment of the invention provides a method for calculating steam flow during hot flushing of an air cooling island, which comprises the following steps:

acquiring test data of the air cooling island under a checking working condition, and calculating fouling thermal resistance of the air cooling island according to the test data under the checking working condition;

acquiring monitoring data of a target condenser row when the air cooling island is flushed in a hot state; the target condenser column is any condenser column in the air cooling island;

calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data;

calculating the heat exchange quantity of the target condenser array according to the heat exchange coefficient;

and calculating the steam flow of the target condenser column according to the heat exchange amount.

A second aspect of the embodiments of the present invention provides a steam flow calculation device during hot flushing of an air cooling island, including:

the fouling thermal resistance acquisition module is used for acquiring test data of the air cooling island under a checking working condition and calculating fouling thermal resistance of the air cooling island according to the test data under the checking working condition;

the monitoring data acquisition module is used for acquiring monitoring data of a target condenser column when the air cooling island is flushed in a hot state; the target condenser column is any condenser column of the air cooling island;

the heat exchange coefficient calculation module is used for calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data;

the heat exchange quantity calculation module is used for calculating the heat exchange quantity of the target condenser array according to the heat exchange coefficient;

and the steam flow calculation module is used for calculating the steam flow of the target condenser column according to the heat exchange amount.

A third aspect of an embodiment of the present invention provides a terminal device, including:

comprising a memory, a processor and a computer program stored in said memory and executable on said processor, said processor implementing the steps of the method as described above when executing said computer program.

A fourth aspect of embodiments of the present invention provides a computer-readable storage medium having stored thereon a computer program which, when executed by a processor, performs the steps of the method as described above.

Compared with the prior art, the embodiment of the invention has the following beneficial effects: the embodiment of the invention provides a steam flow calculation method during hot flushing of an air cooling island, which comprises the following steps: acquiring test data of the air cooling island under a checking condition, and calculating fouling thermal resistance of the air cooling island according to the test data under the checking condition; acquiring monitoring data of a target condenser row when the air cooling island is flushed in a hot state, wherein the target condenser row is any one condenser row in the air cooling island; calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data; and calculating the heat exchange quantity of the target condenser array according to the heat exchange coefficient. The steam flow calculation method during the hot washing of the air cooling island can accurately calculate the steam flow in each condenser row during the hot washing of the air cooling island according to the dirt thermal resistance of the air cooling island, and provides a basis for controlling and adjusting the hot washing process of the air cooling island, so that the hot washing time of the air cooling island is shortened, the steam consumption is saved, the washing effect is improved, and the washing efficiency is improved.

Drawings

In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the embodiments or the prior art descriptions will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings based on these drawings without inventive exercise.

Fig. 1 is a schematic structural diagram of an air cooling island provided in an embodiment of the present invention;

fig. 2 is a schematic flow chart illustrating an implementation of a steam flow calculation method during hot flushing of an air cooling island according to an embodiment of the present invention;

FIG. 3 is a schematic diagram of performance curves of an air cooling island provided by an embodiment of the invention;

fig. 4 is a schematic structural diagram of a steam flow calculation device during hot flushing of an air cooling island according to an embodiment of the present invention;

fig. 5 is a schematic diagram of a terminal device according to an embodiment of the present invention.

Detailed Description

In the following description, for purposes of explanation and not limitation, specific details are set forth, such as particular system structures, techniques, etc. in order to provide a thorough understanding of the embodiments of the invention. It will be apparent, however, to one skilled in the art that the present invention may be practiced in other embodiments that depart from these specific details. In other instances, detailed descriptions of well-known systems, devices, circuits, and methods are omitted so as not to obscure the description of the present invention with unnecessary detail.

In order to explain the technical means of the present invention, the following description will be given by way of specific examples.

The embodiment of the invention provides an air cooling island which comprises a main steam exhaust pipeline, a steam distribution pipe, a plurality of air cooling condenser rows and a condensed water collection system. Each air-cooled condenser column comprises a plurality of cooling units with finned tube heat exchangers, and each cooling unit is provided with a shaft exhaust fan for ventilation, a reduction gearbox and an electric appliance driving device. The air cooling island further comprises an elevating steel platform and an auxiliary system, wherein the auxiliary system comprises a windproof net, a wind-break wall, a high-pressure water cleaning system and the like.

Before the air cooling island is put into use, impurities such as rust, welding slag, dust and the like exist on the inner surfaces of the pipeline and the heat exchanger of the air cooling island. In order to avoid impurities entering a condensed water system, the air cooling island system needs to be flushed in a hot state through hot steam before starting.

The process of the hot state flushing of the air cooling island comprises the following steps: the boiler of the unit provides steam for flushing, the steam enters the air cooling island after being subjected to temperature reduction and pressure reduction through the steam turbine bypass, the steam scours dirt in the air cooling island and is condensed into water, and the condensed water is discharged outside through the pipeline of the temporary system and does not enter the condensed water system. And when the iron content and the turbidity of the condensed water corresponding to each condenser row are qualified, stopping the unit, breaking the vacuum of the steam turbine, recovering the air cooling system and removing the temporary pipeline.

Fig. 1 shows a structure of an air cooling island, wherein 101 in fig. 1 is an inlet steam pressure measuring point, 102 is an inlet steam temperature measuring point, 103 is a steam isolating valve, 104 is a condensate temperature measuring point, 105 is a condensate tank, and 1-8 columns are condenser columns. In the hot washing process, in order to improve the washing pertinence, the condenser rows are washed one by one, and the operation parameters of the condenser rows which are being washed are adjusted. However, the individual condenser rows of the air cooling island are not completely isolated, for example, 3 rows, 4 rows, 5 rows and 6 rows in fig. 1 are always in operation, i.e., a simultaneous hot flushing is required. Under the condition, the staff is difficult to accurately calculate the steam flow of each condenser row, and can only adjust the pressure and the temperature of the hot steam according to experience, so that the control process is extensive.

Referring to fig. 2, an embodiment of the present invention provides a method for calculating a steam flow during hot flushing of an air cooling island, including:

s101: acquiring test data of the air cooling island under a checking working condition, and calculating fouling thermal resistance of the air cooling island according to the test data under the checking working condition;

in this embodiment, the test data of the air cooling island can be directly obtained according to the measuring point when the air cooling island operates, and a sensor does not need to be added or a hardware system of the air cooling island is not required to be improved, so that certain convenience is provided.

In this embodiment, before S101, the method further includes:

acquiring the model of an air cooling island and the distribution condition of measuring points of an air cooling island unit; confirming that the main and auxiliary machines and the temporary system related to the hot state flushing have commissioning conditions; and cleaning the inner part and the outer part of the air cooling island.

And starting the boiler, the water supply system and the vacuum system, gradually increasing the pressure of the steam of the boiler, adjusting the pressure and the temperature of the main steam to target values through a high-low pressure bypass system of the steam turbine, and discharging the condensed water.

Controlling an isolation valve to enable steam to enter each condenser row of the air cooling island for testing, and adjusting the operation of an air cooling fan to enable the air cooling island to be in a checking working condition, namely controlling the pressure of the air cooling island within a target range; and (4) keeping the rotating speed of the air cooling fan, the steam pressure and the steam temperature of the low side outlet and the evaporation capacity of the boiler in a stable state, operating for 30-60 minutes, and acquiring measuring point data as test data.

In one embodiment of the present invention, S101 includes:

calculating the number of heat transfer units of the air cooling island according to the test data and a heat transfer unit number calculation formula;

calculating the heat exchange coefficient of the air cooling island under the checking working condition according to the number of the heat transfer units and a first heat exchange coefficient calculation formula;

calculating the fouling thermal resistance of the air cooling island according to a calculation formula of the heat exchange coefficient and the fouling thermal resistance of the air cooling island under the checking working condition;

the heat transfer unit number calculation formula is as follows:

in the formula (1), NTU is the number of heat transfer units, Q_pIs the heat released by the steam, t_s1To check the temperature of the condensate in the operating mode, t_a1To check the inlet cold air temperature under operating conditions, D_a1For checking the inlet air quantity under operating conditions, C_pa1The specific heat capacity of the cold air under the checking working condition is constant pressure, and rho is the density of the cold air under the checking working condition;

in this embodiment, the calculation formula of the inlet air volume under the checking condition is as follows:

in the formula (2), n_a1For checking the speed, n, of the air-cooled fan under operating conditions_aRated speed of the air-cooling fan, D_aThe inlet air quantity is the inlet air quantity of the air cooling fan at the rated rotating speed.

In the present embodiment, the calculation formula of the steam heat release amount is:

Q_p＝D_t·(h_t-h_s1) (3)

in the formula (3), D_tIs the steam flow rate, h_tTo check the steam enthalpy, h, under operating conditions_s1The enthalpy of the condensed water under the working condition is checked.

Alternatively, the steam flow is calculated by the condensate flow, the steam enthalpy is calculated by the steam pressure and the temperature, and the condensate enthalpy is calculated by the condensate temperature.

The first heat exchange coefficient is calculated by the formula

In the formula (4), K is the heat exchange coefficient of the air cooling island under the checking working condition, and A is the heat exchange area of the air cooling island; the fouling thermal resistance calculation formula is as follows:

in the formula (5), R_fThermal resistance to fouling, K₀And designing the heat exchange coefficient for the air cooling island.

In this embodiment, due to the existence of the fouling resistance, the real heat exchange coefficient of the air cooling island is often smaller than the designed heat exchange coefficient, and according to the fouling resistance calculated by the embodiment of the invention, the heat exchange coefficient of the target condenser row can be accurately calculated, so that a basis is provided for accurately calculating the steam flow.

S102: acquiring monitoring data of a target condenser row when the air cooling island is flushed in a hot state; the target condenser column is any condenser column in the air cooling island;

in this embodiment, the monitoring data of the air cooling island can be directly obtained according to the measuring point during the operation of the air cooling island, and a sensor does not need to be added or a hardware system of the air cooling island is not required to be improved.

In this embodiment, before S102, the method further includes:

and adjusting an isolation valve, the rotating speed of an air cooling fan, the evaporation capacity of a boiler and a high-low bypass, and enabling the air cooling island system to operate stably.

Specifically, the exhaust pressure is maintained at 35 kPa, and the exhaust stability is maintained at 120 ℃.

In this embodiment, the condenser column with the closed isolation valve can completely isolate steam, and the heat exchange amount of this type of condenser column is zero, so that the calculation of the steam flow is not needed.

In this embodiment, the target condenser bank is in the variable-operating-condition operating state without closing the isolation valve. The target condenser rows are divided into an out-of-service condenser row and an in-service condenser row according to the operating condition of the fan, wherein the in-service condenser row is a condenser row mainly flushed at the current time, and the out-of-service condenser row can shunt a part of hot steam. Specifically, the fans of the air cooling units in the condenser row which is stopped from operating are in a closed state, but air still passes through the air cooling fin radiator due to natural ventilation.

The natural ventilation in this embodiment is formed by air in the air cooling island under the distribution effect of its own temperature field, and does not refer to natural wind in the atmospheric environment.

In this embodiment, the flow resistance and the heat exchange characteristic of the air flowing through the finned tube bundle are mainly affected by the head-on wind speed, and fig. 3 shows a performance curve diagram of the air cooling island provided by the embodiment of the present invention, that is, a corresponding relationship among the back pressure, the temperature and the heat load rate of the stop operation condenser row.

In this embodiment, the target condenser row includes a condenser row which stops operating, and the monitoring data includes an oncoming wind speed; s102 includes:

the method comprises the following steps: initializing the head-on wind speed, and taking the initialized head-on wind speed as the current head-on wind speed;

step two: calculating a judgment difference corresponding to the current head-on wind speed according to the current head-on wind speed and a judgment difference calculation formula;

step three: comparing the judgment difference value corresponding to the current head-on wind speed with the judgment threshold value, if the judgment difference value corresponding to the current head-on wind speed is larger than or equal to the judgment threshold value, increasing the current head-on wind speed according to a preset step length, and updating the current head-on wind speed in the second step by adopting the increased head-on wind speed; repeatedly executing the second step to the third step until the judgment difference value is smaller than the judgment threshold value;

step four: if the judgment difference value corresponding to the current head-on wind speed is smaller than the judgment threshold value, taking the current head-on wind speed as the head-on wind speed of the condenser row which stops running;

the judgment difference value calculation formula is as follows:

in the formula (6), Δ is a judgment difference value, Q_pIs the heat released by the steam, t_s1tTemperature of condensate for stopping condenser train operation, t_a1tInlet cold air temperature for the condenser row to be stopped, A_yTo stop the frontal area of the condenser row, v_tHead-on wind speed for stopping condenser train operation, C_pa1tFor stopping the cold air of the condenser row at a constant pressure and specific heat capacity, rho_tIn order to stop the cold air density of the condenser row, A is the heat exchange area of the air cooling island; alpha is alpha_iIs the steam side heat exchange coefficient under the reference working condition, A_iIs the steam side heat exchange area, delta is the tube wall thickness, A_mFor measuring heat transfer area, alpha, of the tube wall_oIs the air side heat exchange coefficient eta under the reference working condition_oFor fin heat exchange efficiency, v_tHead-on wind speed, v, for stopping operation of the condenser bank_oThe head-on wind speed of the air cooling condenser row under the reference working condition.

In this embodiment, the judgment difference calculation formula is derived from the second heat exchange coefficient calculation formula and the heat exchange amount calculation formula, optionally, the initialized head-on wind speed is 0.01m/s, the preset step length is 0.001m/s, and the judgment threshold is 0.005.

S103: calculating the heat exchange coefficient of the target condenser array according to the fouling thermal resistance and the monitoring data;

in one embodiment of the invention, the monitoring data comprises: the heat exchange area of the air cooling island, the heat exchange area of the steam side, the heat exchange area of the pipe wall, the heat exchange area of the air side, the heat exchange efficiency of fins of the air cooling island, the thermal resistance of dirt, the heat exchange coefficient of the air side under a reference working condition, the head-on wind speed under the reference working condition, the heat exchange coefficient of the steam side under the current working condition, the heat conductivity coefficient of the pipe wall under the current working condition and the heat exchange coefficient of the air side under the current working condition;

s103 includes:

substituting the monitoring data into a second heat exchange coefficient calculation formula, and calculating the heat exchange coefficient of the target condenser row;

the second heat exchange coefficient calculation formula is as follows:

in the formula (7), K' is the heat exchange coefficient of the target condenser row, A is the heat exchange area of the air cooling island, and alpha_i' is the steam side heat transfer coefficient under the current working condition, A_iIs the heat exchange area of the steam side, lambda' is the heat conductivity coefficient of the pipe wall under the current working condition, A_mIs the heat exchange area of the pipe wall, delta is the pipe wall thickness of the air cooling island, alpha_o' is the air side heat transfer coefficient under the current working condition, A_oIs the air side heat exchange area, eta_oFor air cooling island fin heat exchange efficiency, R_fIs fouling resistance; alpha is alpha_oIs the air side heat exchange coefficient v under the reference working condition_o' is the head-on wind speed under the current working condition, v_oIs the head-on wind speed under the reference working condition.

In this embodiment, the condenser uses the single row of oval finned tube, and pipe wall side heat transfer coefficient and steam side heat transfer coefficient's value is less, and the change under different operating modes is less, can regard as the definite value.

In this embodiment, calculating the heat transfer coefficient can carry out simple and easy evaluation to the heat transfer performance of air cooling condenser.

S104: calculating the heat exchange quantity of the target condenser array according to the heat exchange coefficient;

in one embodiment of the present invention, S104 includes:

calculating the heat exchange quantity of the target condenser array according to a heat exchange quantity calculation formula and the heat exchange coefficient;

the heat exchange quantity calculation formula is as follows:

in the formula (8), Q_p' is the heat exchange quantity of the target condenser row under the current working condition, t_s1' is the temperature of the condensate water under the current operating conditions, t_a1' is the inlet cold air temperature under the current operating condition, D_a1' is the inlet air quantity under the current working condition, C_pa1The specific heat capacity of cold air at constant pressure under the current working condition is ' shown, rho ' is the density of the cold air under the current working condition, K ' is the heat exchange coefficient of the target condenser row, and A is the heat exchange area of the air cooling island.

S105: and calculating the steam flow of the target condenser column according to the heat exchange amount.

In one embodiment of the present invention, S105 includes:

calculating the steam flow of the target condenser row according to a steam flow calculation formula and the heat exchange amount;

the steam flow calculation formula is as follows:

in the formula (9), D_p' is the steam flow of the target condenser row under the current working condition, Q_p' is the heat exchange quantity of the target condenser row under the current working condition, h_p' is the inlet enthalpy under the current working condition, h_s1' is the enthalpy of the condensed water under the current operating conditions.

In an embodiment of the invention, after calculating the steam flow of the target condenser bank, the method further comprises:

comparing the steam flow of the condenser row in operation with the corresponding steam flow design value; if the steam flow of the condenser row in operation is larger than the corresponding steam flow design value, keeping the current state for flushing;

if the target condenser row which does not reach the steam flow design value exists, calculating the difference value between the target condenser row which does not reach the steam flow design value and the corresponding steam flow design value;

the flushing process is adjusted according to the magnitude of the difference, the number of columns currently being flushed, and the amount of the demineralized water remaining.

Optionally, if the demineralized water storage is greater than the storage threshold and the steam flow difference of the current target condenser row is smaller than the difference threshold, the steam flow of the current target condenser row may be increased by increasing the boiler evaporation capacity or increasing the rotation speed of the fan of the current target condenser row. If the desalted water storage is smaller than the storage threshold and/or the steam flow difference value of the current target condenser row is larger than the difference threshold, the fan of the current target condenser row can be closed, steam is preferentially supplied to other target condenser rows, the washing pertinence is improved, and the target condenser rows are prevented from being in a low-efficiency washing state with low flow for a long time.

The steam flow calculation method provided by the embodiment fully considers the influence of fouling thermal resistance, and the calculation accuracy is high by analyzing based on the actual performance of the air cooling island; the condenser columns are classified according to isolation conditions and operation states, and calculation pertinence is good. In addition, the method provided by the embodiment can directly use the running measuring point of the unit without an additional instrument, and the calculation process is simple. In addition, the result of this embodiment calculation still can provide the basis for the operating personnel control washing process, makes the state that the high parameter of high flow is maintained to the target condenser row, avoids each condenser row all to carry out invalid low flow and washes repeatedly to improve the effect that the hot is washed, shorten the time of washing, and then reduce the consumption of steam promptly demineralized water, prevent the washing interrupt condition that the demineralized water is not enough to appear.

Taking a specific application scenario as an example, the air cooling island is applied to two 660MW supercritical direct air cooling units, and the turbo generator units in the units are arranged in a full high position. Referring to fig. 1, the air cooling island provided in this embodiment obtains steam exhausted by the steam turbine through the diversion tee and the main steam exhaust pipeline. And steam enters the top of the air-cooled condenser row through the eight steam exhaust branch pipes after passing through the horizontal straight pipe. In the condenser row, steam is subjected to surface heat exchange with air and then cooled to form condensate water after passing through an upper header, and the condensate water is collected by a condensate pipe and then discharged to a condensate water tank or a temporary drainage system. Specifically, the air cooling island that this embodiment provided includes eight condenser rows, and every condenser row includes 8 fans eight air cooling condenser units promptly, and every air cooling condenser all has cocurrent flow tube bank and countercurrent tube bank two parts to constitute.

Table 1 lists the main design parameters of the air cooling island provided by the present embodiment.

TABLE 1

Referring to fig. 1, in the air cooling island provided by the present embodiment, the 1-row, 2-row, 7-row and 8-row condenser rows can be isolated by the isolation valve 103, that is, when the isolation valve 103 is closed, the steam flow in each of the condenser rows does not need to be calculated. And 3-6 condenser rows can not be isolated.

The method for calculating the steam flow calculates the fouling thermal resistance of the air cooling island, evaluates the heat exchange performance of the air cooling island, and finally calculates the steam flow in each condenser row, and comprises the following specific steps:

step 1, adjusting an air cooling island to a checking working condition and operating;

step 1.1 test preparation

1) And carrying out test preparation work, and formulating a test scheme according to the distribution of the isolation valves of the condenser row.

Specifically, 3, 4, 5 and 6 condenser columns which cannot be isolated are taken as test objects; closing isolation valves 103 corresponding to 1, 2, 7 and 8 isolatable condenser rows, wherein each row is provided with a condensate temperature measuring point 104, and the respective operation conditions can be respectively determined; the air cooling island steam inlet pipeline is respectively provided with a plurality of pressure measuring points 101 and temperature measuring points 102, so that the parameters of steam entering the air cooling island can be accurately measured;

2) confirming that the main and auxiliary machines related to the hot state flushing have operation conditions; confirming that the temporary system for hot state flushing is installed completely and has commissioning conditions; confirming that the inside and the outside of the air cooling island are both preliminarily cleaned;

step 1.2, starting a machine set:

1) ignition of a boiler, and operation of related equipment and systems such as condensation system water, a water supply system, a steam turbine vacuum system and the like; discharging condensed water;

2) the pressure of the boiler steam is gradually increased by the boiler, and the steam pressure and the temperature are adjusted to target values (70kPa/120 ℃) by main steam through a high-pressure bypass system and a low-pressure bypass system of a steam turbine;

step 1.3, the air cooling island is adjusted to a test state:

1) controlling an isolation valve of a steam distribution pipe of an air cooling island to enable steam to enter a condenser row for testing, adjusting the running rotating speed of an air cooling fan, and simultaneously maintaining the steam pressure temperature at a target value, wherein the specific steam pressure target value is 70kPa, and the steam temperature target value is 120 ℃;

2) maintaining stable parameters such as the rotating speed of an air cooling fan, the steam pressure and the temperature of a low side outlet, the evaporation capacity of the boiler and the like of the test train, and operating for 60 minutes; and (4) carrying out water sample assay and recording, wherein the test working condition can be used as primary cleaning of 3, 4, 5 and 6 columns.

And 2, acquiring test data under the checking working condition, wherein the acquisition frequency of the test data is 10 seconds/time.

Table 2 lists the experimental data collected through the stations in this example.

TABLE 2

Step 3, calculating the fouling thermal resistance and heat exchange performance

Step 3.1, calculating the number of heat transfer units according to the formula (1), the formula (2), the formula (3) and the test data, wherein the result is as follows: NTU 1.812;

step 3.2, calculating the heat exchange coefficient of the air cooling island under the checking working condition according to the formula (4) and the number of the heat transfer units, wherein the result is as follows: K34.551W/(° c. m)²)；

Step 3.3, calculating fouling thermal resistance according to the formula (5) and the heat exchange coefficient under the checking working condition, wherein the result is as follows:

R_f＝0.00204(℃·m²)/W。

step 4, carrying out hot state washing and acquiring monitoring data

And 4.1, opening isolation valves of the 1 row and the 8 rows of condenser rows, adjusting the rotating speed of the fans, and reducing the rotating speed of the fans of the 3 rows, the 4 rows, the 5 rows and the 6 rows to zero. Adjusting the exhaust pressure to 35 kilopascals and the exhaust temperature to 120 ℃, and acquiring monitoring data.

Table 3 lists the monitoring data of the target condenser column during the hot flushing of the air cooling island;

TABLE 3

Step 4.2, calculating the head-on wind speed of the condenser row which stops running, selecting a performance curve with the environment temperature of 10 ℃ and the heat load rate of 50% in the performance curve schematic diagram of the figure 3, and setting v_tThe initial value is 0.01m/S, the step length is 0.001, the iteration stop condition is set to be | delta | less than or equal to 0.005, the head-on wind speed is iteratively calculated according to the method of S102, and the result is as follows: v. of_t＝0.394m/s；

Step 5, solving the steam flow of the target condenser row

Step 5.1, calculating a second heat exchange coefficient according to the monitoring data and the formula (7), wherein the result is as follows: the heat exchange coefficient of the condenser row 1 is 29.161W/(. degree.C.. m)²) And the heat exchange coefficient of the 8 condenser rows is 16.950W/(℃·m²The heat exchange coefficients of the condenser arrays of the 3, 4, 5 and 6 arrays are 8.785W/(° C. m)²)。

Step 5.2, calculating the heat exchange quantity according to the second heat exchange coefficient and the formula (8), wherein the result is as follows: the heat exchange capacity of the 1-row condenser row is 105.923MW, the heat exchange capacity of the 8-row condenser row is 63.022MW, and the heat exchange capacity of the 3-row, 4-row, 5-row and 6-row condenser rows is 128.793MW

Step 5.3, calculating the steam flow according to the heat exchange quantity and the formula (9), wherein the result is as follows: the steam flow of the 1-row condenser row is 156.233t/h, the heat exchange quantity of the 8-row condenser row is 92.992t/h, and the steam flow of the 3-row, 4-row, 5-row and 6-row condenser rows is 190.200 t/h. Optionally, adjusting the rotating speed of the fan and the evaporation capacity of the boiler, and increasing the steam flow of 8 rows of condensers by about 60 t/h; or closing the isolation valves and the fans of the 8 rows of condenser rows, correspondingly reducing the evaporation capacity of the boiler, and only intensively washing 1 row of condenser rows.

Through the process, the pertinence of the washing process can be improved, and the condition that each target condenser row is in an invalid low-flow washing state for a long time is avoided, so that the efficiency of the washing process is improved.

It should be understood that, the sequence numbers of the steps in the foregoing embodiments do not imply an execution sequence, and the execution sequence of each process should be determined by its function and inherent logic, and should not constitute any limitation to the implementation process of the embodiments of the present invention.

Referring to fig. 4, an embodiment of the present invention provides a steam flow calculation device 40 during hot flushing of an air cooling island, including:

the fouling thermal resistance acquisition module 410 is used for acquiring test data of the air cooling island under a checking working condition and calculating fouling thermal resistance of the air cooling island according to the test data under the checking working condition;

the monitoring data acquisition module 420 is used for acquiring monitoring data of a target condenser column when the air cooling island is flushed in a hot state; the target condenser column is any condenser column of the air cooling island;

the heat exchange coefficient calculation module 430 is configured to calculate a heat exchange coefficient of the target condenser row according to the fouling thermal resistance and the monitoring data;

the heat exchange amount calculation module 440 is configured to calculate a heat exchange amount of the target condenser row according to the heat exchange coefficient;

and the steam flow calculating module 450 is configured to calculate the steam flow of the target condenser row according to the heat exchange amount.

The steam flow calculation method during the hot washing of the air cooling island can accurately calculate the steam flow in each condenser row during the hot washing of the air cooling island according to the dirt thermal resistance of the air cooling island, and provides a basis for controlling and adjusting the hot washing process of the air cooling island, so that the hot washing time of the air cooling island is shortened, the steam consumption is saved, the washing effect is improved, and the washing efficiency is improved.

In this embodiment, the fouling thermal resistance obtaining module 410 includes:

the heat transfer unit number calculation unit is used for calculating the heat transfer unit number of the air cooling island according to the test data and a heat transfer unit number calculation formula;

the checking working condition heat exchange coefficient calculation unit is used for calculating the heat exchange coefficient of the air cooling island under the checking working condition according to the number of the heat transfer units and a first heat exchange coefficient calculation formula;

the fouling thermal resistance calculation unit is used for calculating the fouling thermal resistance of the air cooling island according to the heat exchange coefficient and the fouling thermal resistance calculation formula of the air cooling island under the checking working condition;

the heat transfer unit number calculation formula is as follows:

wherein NTU is the number of heat transfer units, Q_pIs the heat released by the steam, t_s1To check the temperature of the condensate in the operating mode, t_a1To check the inlet cold air temperature under operating conditions, D_a1For checking the inlet air quantity under operating conditions, C_pa1The specific heat capacity of the cold air under the checking working condition is constant pressure, and rho is the density of the cold air under the checking working condition;

the first heat exchange coefficient calculation formula is as follows:

k is the heat exchange coefficient of the air cooling island under the checking working condition, and A is the heat exchange area of the air cooling island;

the fouling thermal resistance calculation formula is as follows:

wherein R is_fThermal resistance to fouling, K₀And designing the heat exchange coefficient for the air cooling island.

In this embodiment, the target condenser row includes a condenser row which stops operating, and the monitoring data includes an oncoming wind speed; the monitoring data acquisition module 420 includes:

the system comprises a windward speed initialization unit, a windward speed control unit and a windward speed control unit, wherein the windward speed initialization unit is used for initializing the windward speed and taking the initialized windward speed as the current windward speed;

the judgment difference value calculation unit is used for calculating a judgment difference value corresponding to the current head-on wind speed according to the current head-on wind speed and a judgment difference value calculation formula;

the windward speed updating unit is used for comparing the judgment difference value corresponding to the current windward speed with the judgment threshold value, if the judgment difference value corresponding to the current windward speed is larger than or equal to the judgment threshold value, the current windward speed is increased according to a preset step length, and the increased windward speed is adopted to update the current windward speed in the second step; repeatedly executing the second step to the third step until the judgment difference value is smaller than the judgment threshold value;

the head-on wind speed determining unit is used for taking the current head-on wind speed as the head-on wind speed of the condenser row which stops running when the judgment difference value corresponding to the current head-on wind speed is smaller than the judgment threshold value;

the judgment difference value calculation formula is as follows:

wherein, Delta is a judgment difference value, Q_pIs the heat released by the steam, t_s1tFor stopping operationTemperature of condensate of steam turbine, t_a1tInlet cold air temperature for the condenser row to be stopped, A_yTo stop the frontal area of the condenser row, v_tHead-on wind speed for stopping condenser train operation, C_pa1tFor stopping the cold air of the condenser row at a constant pressure and specific heat capacity, rho_tIn order to stop the cold air density of the condenser row, A is the heat exchange area of the air cooling island; alpha is alpha_iIs the steam side heat exchange coefficient under the reference working condition, A_iIs the steam side heat exchange area, delta is the tube wall thickness, A_mFor measuring heat transfer area, alpha, of the tube wall_oIs the air side heat exchange coefficient eta under the reference working condition_oFor fin heat exchange efficiency, v_tHead-on wind speed, v, for stopping operation of the condenser bank_oThe head-on wind speed of the air cooling condenser row under the reference working condition.

In one embodiment of the invention, the monitoring data comprises: the heat exchange area of the air cooling island, the heat exchange area of the steam side, the heat exchange area of the pipe wall, the heat exchange area of the air side, the heat exchange efficiency of fins of the air cooling island, the thermal resistance of dirt, the heat exchange coefficient of the air side under a reference working condition, the head-on wind speed under the reference working condition, the heat exchange coefficient of the steam side under the current working condition, the heat conductivity coefficient of the pipe wall under the current working condition and the heat exchange coefficient of the air side under the current working condition;

the heat exchange coefficient calculation module 430 is specifically configured to:

substituting the monitoring data into a second heat exchange coefficient calculation formula, and calculating the heat exchange coefficient of the target condenser row;

the second heat exchange coefficient calculation formula is as follows:

wherein K' is the heat exchange coefficient of the target condenser row, A is the heat exchange area of the air cooling island, and alpha_i' is the steam side heat transfer coefficient under the current working condition, A_iIs the heat exchange area of the steam side, lambda' is the heat conductivity coefficient of the pipe wall under the current working condition, A_mIs the heat exchange area of the pipe wall, delta is the pipe wall thickness of the air cooling island, alpha_oIs the current operating conditionAir side heat transfer coefficient, A_oIs the air side heat exchange area, eta_oFor air cooling island fin heat exchange efficiency, R_fIs fouling resistance; alpha is alpha_oIs the air side heat exchange coefficient v under the reference working condition_o' is the head-on wind speed under the current working condition, v_oIs the head-on wind speed under the reference working condition.

In this embodiment, the heat exchange amount calculation module 440 is specifically configured to:

calculating the heat exchange quantity of the target condenser array according to a heat exchange quantity calculation formula and the heat exchange coefficient;

the heat exchange quantity calculation formula is as follows:

wherein Q is_p' is the heat exchange quantity of the target condenser row under the current working condition, t_s1' is the temperature of the condensate water under the current operating conditions, t_a1' is the inlet cold air temperature under the current operating condition, D_a1' is the inlet air quantity under the current working condition, C_pa1The specific heat capacity of cold air at constant pressure under the current working condition is ' shown, rho ' is the density of the cold air under the current working condition, K ' is the heat exchange coefficient of the target condenser row, and A is the heat exchange area of the air cooling island.

In this embodiment, the steam flow calculating module 450 is specifically configured to:

calculating the steam flow of the target condenser row according to a steam flow calculation formula and the heat exchange amount;

the steam flow calculation formula is as follows:

wherein D is_p' is the steam flow of the target condenser row under the current working condition, Q_p' is the heat exchange quantity of the target condenser row under the current working condition, h_p' is the inlet enthalpy under the current working condition, h_s1' is the enthalpy of the condensed water under the current operating conditions.

Fig. 5 is a schematic diagram of a terminal device according to an embodiment of the present invention. As shown in fig. 5, the terminal device 5 of this embodiment includes: a processor 50, a memory 51 and a computer program 52 stored in said memory 51 and executable on said processor 50, such as a steam flow calculation program at hot flushing of an air cooling island. The processor 50, when executing the computer program 52, implements the steps in the above-mentioned embodiments of the method for calculating the steam flow rate during the hot flushing of the air cooling island, such as S101 to S105 shown in fig. 2. Alternatively, the processor 50, when executing the computer program 52, implements the functions of the modules/units in the above-mentioned device embodiments, such as the functions of the modules 410 to 450 shown in fig. 4.

Illustratively, the computer program 52 may be partitioned into one or more modules/units that are stored in the memory 51 and executed by the processor 50 to implement the present invention. The one or more modules/units may be a series of computer program instruction segments capable of performing specific functions, which are used to describe the execution process of the computer program 52 in the terminal device 5. For example, the computer program 52 may be divided into a fouling resistance acquisition module, a monitoring data acquisition module, a heat exchange coefficient calculation module, a heat exchange amount calculation module, a steam flow calculation module (a module in a virtual device).

The terminal device 5 may be a desktop computer, a notebook, a palm computer, a cloud server, or other computing devices. The terminal device may include, but is not limited to, a processor 50, a memory 51. Those skilled in the art will appreciate that fig. 5 is merely an example of a terminal device 5 and does not constitute a limitation of terminal device 5 and may include more or fewer components than shown, or some components may be combined, or different components, e.g., the terminal device may also include input-output devices, network access devices, buses, etc.

The Processor 50 may be a Central Processing Unit (CPU), other general purpose Processor, a Digital Signal Processor (DSP), an Application Specific Integrated Circuit (ASIC), an off-the-shelf Programmable Gate Array (FPGA) or other Programmable logic device, discrete Gate or transistor logic, discrete hardware components, etc. A general purpose processor may be a microprocessor or the processor may be any conventional processor or the like.

The memory 51 may be an internal storage unit of the terminal device 5, such as a hard disk or a memory of the terminal device 5. The memory 51 may also be an external storage device of the terminal device 5, such as a plug-in hard disk, a Smart Media Card (SMC), a Secure Digital (SD) Card, a Flash memory Card (Flash Card), and the like, which are provided on the terminal device 5. Further, the memory 51 may also include both an internal storage unit and an external storage device of the terminal device 5. The memory 51 is used for storing the computer program and other programs and data required by the terminal device. The memory 51 may also be used to temporarily store data that has been output or is to be output.

It will be apparent to those skilled in the art that, for convenience and brevity of description, only the above-mentioned division of the functional units and modules is illustrated, and in practical applications, the above-mentioned function distribution may be performed by different functional units and modules according to needs, that is, the internal structure of the apparatus is divided into different functional units or modules to perform all or part of the above-mentioned functions. Each functional unit and module in the embodiments may be integrated in one processing unit, or each unit may exist alone physically, or two or more units are integrated in one unit, and the integrated unit may be implemented in a form of hardware, or in a form of software functional unit. In addition, specific names of the functional units and modules are only for convenience of distinguishing from each other, and are not used for limiting the protection scope of the present application. The specific working processes of the units and modules in the system may refer to the corresponding processes in the foregoing method embodiments, and are not described herein again.

In the above embodiments, the descriptions of the respective embodiments have respective emphasis, and reference may be made to the related descriptions of other embodiments for parts that are not described or illustrated in a certain embodiment.

Those of ordinary skill in the art will appreciate that the various illustrative elements and algorithm steps described in connection with the embodiments disclosed herein may be implemented as electronic hardware or combinations of computer software and electronic hardware. Whether such functionality is implemented as hardware or software depends upon the particular application and design constraints imposed on the implementation. Skilled artisans may implement the described functionality in varying ways for each particular application, but such implementation decisions should not be interpreted as causing a departure from the scope of the present invention.

In the embodiments provided in the present invention, it should be understood that the disclosed apparatus/terminal device and method may be implemented in other ways. For example, the above-described embodiments of the apparatus/terminal device are merely illustrative, and for example, the division of the modules or units is only one logical division, and there may be other divisions when actually implemented, for example, a plurality of units or components may be combined or integrated into another system, or some features may be omitted, or not executed. In addition, the shown or discussed mutual coupling or direct coupling or communication connection may be an indirect coupling or communication connection through some interfaces, devices or units, and may be in an electrical, mechanical or other form.

The units described as separate parts may or may not be physically separate, and parts displayed as units may or may not be physical units, may be located in one place, or may be distributed on a plurality of network units. Some or all of the units can be selected according to actual needs to achieve the purpose of the solution of the embodiment.

In addition, functional units in the embodiments of the present invention may be integrated into one processing unit, or each unit may exist alone physically, or two or more units are integrated into one unit. The integrated unit can be realized in a form of hardware, and can also be realized in a form of a software functional unit.

The integrated modules/units, if implemented in the form of software functional units and sold or used as separate products, may be stored in a computer readable storage medium. Based on such understanding, all or part of the flow of the method according to the embodiments of the present invention may also be implemented by a computer program, which may be stored in a computer-readable storage medium, and when the computer program is executed by a processor, the steps of the method embodiments may be implemented. . Wherein the computer program comprises computer program code, which may be in the form of source code, object code, an executable file or some intermediate form, etc. The computer-readable medium may include: any entity or device capable of carrying the computer program code, recording medium, usb disk, removable hard disk, magnetic disk, optical disk, computer Memory, Read-Only Memory (ROM), Random Access Memory (RAM), electrical carrier wave signals, telecommunications signals, software distribution medium, and the like. It should be noted that the computer readable medium may contain content that is subject to appropriate increase or decrease as required by legislation and patent practice in jurisdictions, for example, in some jurisdictions, computer readable media does not include electrical carrier signals and telecommunications signals as is required by legislation and patent practice.

The above-mentioned embodiments are only used for illustrating the technical solutions of the present invention, and not for limiting the same; although the present invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; such modifications and substitutions do not substantially depart from the spirit and scope of the embodiments of the present invention, and are intended to be included within the scope of the present invention.