Low-position-arranged combined cycle unit drainage system and operation method
Technical Field
The invention relates to the technical field of hydrophobic cycle recycling of power plants, in particular to a combined cycle unit hydrophobic system arranged at a low position and an operation method.
Background
Along with the increase of the installed capacity of the domestic gas-steam combined cycle power generating unit, part of plants can adopt a low-level arrangement structure during design, the design provides convenience for unit installation and maintenance work, and the amount investment of a combined cycle power plant is reduced. Panhua et al in chinese patent 201410832031.3 disclose a combined plant low-level layout structure of a multi-shaft combined cycle thermal power generating unit, which reduces the floor space and volume of the main plant and facilitates the installation and maintenance of the unit. However, the patent does not relate to the operation method of the unit system and the specific arrangement mode of the system.
The design of the drainage system of the steam turbine has direct influence on the economy and the safety of unit operation, and the plant design of the low-level arrangement structure enables the drainage flash tank part to be below 0 meter in the plant, so that the reasonable drainage recovery method and the control mode are favorable for improving the reliability of unit operation.
Disclosure of Invention
In order to overcome the defects of the prior art, the invention aims to provide a combined cycle unit drainage system arranged at a low position and an operation method thereof, so that the economical efficiency and the safety of the steam turbine drainage system in the use process when a factory building is arranged at the low position are improved.
In order to achieve the purpose, the invention adopts the technical scheme that:
a combined cycle unit drainage system arranged at a low position comprises a low-pressure drainage pipe 2 and a high-pressure drainage pipe 13, wherein the output end of the low-pressure drainage pipe 2 is connected with a low-pressure drainage flash tank 5 through a low-pressure drainage collecting pipe 1, the output end of the high-pressure drainage pipe 13 is connected with a high-pressure drainage flash tank 6 through a high-pressure drainage collecting pipe 14, a steam exhaust pipeline 4 is arranged at the top of the drainage flash tank, the steam exhaust pipeline 4 is used for exhausting steam in the drainage flash tank, and the output end of the steam exhaust pipeline 4 is connected with a condenser 11;
the side of the hydrophobic flash tank is provided with a hydrophobic flash tank desuperheating water pipeline 3, the hydrophobic flash tank desuperheating water pipeline 3 is used for spraying desuperheating water into the hydrophobic flash tank, and a condensed water output end at the bottom of the hydrophobic flash tank is connected with a condenser hot well 12 through a hydrophobic drain pipe 9.
And an overflow pipeline 7 is arranged at the middle lower part of the side edge of the drainage drain pipe 9, and a drainage flash tank liquid level meter 15 is arranged at the side edge of the drainage flash tank.
And a check valve is arranged on the drainage flash tank overflow pipeline 7, and an outlet of the drainage flash tank overflow pipeline is connected to a condenser hot well 12.
The drain flash tank liquid level meter 15 is designed with two remote transmission type guided wave radar liquid level meters and an in-situ magnetic turning plate liquid level meter.
The steam exhaust pipeline 4 is divided into a steam exhaust pipeline 4 of a high-pressure hydrophobic flash tank 6 and a steam exhaust pipeline 4 of a low-pressure hydrophobic flash tank 5.
An electric valve and a check valve are arranged on the steam exhaust pipeline 4, and an outlet of the electric valve is connected with the throat part of the condenser 11.
The drain flash tank is divided into a high-pressure drain flash tank 6 and a low-pressure drain flash tank 5, the high-pressure drain flash tank 6 and the low-pressure drain flash tank are respectively used for receiving the high-pressure level drain water and the low-pressure level drain water of the unit in the operation process, the high-pressure drain flash tank 6 and the low-pressure drain flash tank 5 are independently and separately arranged, and the pipeline connection modes are the same.
The drain headers are divided into a high pressure drain header 14 and a low pressure drain header 1, and drain pipes after pressure classification are connected to the high pressure drain header 14 and the low pressure drain header 1, respectively, by pressure classification of drain.
The drain pipe 9 is divided into two branches after a main pipe is led out from the bottom of the drain flash tank, a drain pump 8, an electric valve and a check valve are respectively arranged on each branch, and the tail end of the pipeline of the drain pipe 9 is connected with a condenser hot well 12.
The main pipe of the drainage pipe 9 is connected with a sewage pipeline 10, the sewage pipeline 10 is provided with an electric door and a manual valve, and the tail end of the sewage pipeline 10 is connected to a condensed water pump pit.
The operation mode of the combined cycle unit drainage system arranged at a low position comprises the following steps;
in the operation process of the steam turbine, the drainage after pressure classification flows into a low-pressure drainage collecting pipe 1 and a high-pressure drainage collecting pipe 14 through a low-pressure drainage pipe 2 and a high-pressure drainage pipe 13 respectively, after the drainage reaches a low-pressure drainage flash tank 5 and a high-pressure drainage flash tank 6, after the processes of temperature reduction, pressure reduction and flash tank expansion are carried out in the drainage flash tank, part of steam generated after flash tank expansion enters a condenser 11 through a steam exhaust pipeline 4 connected to the top of the drainage flash tank for recondensation, so that working media are recovered;
a drain flash tank temperature-reducing water pipeline 3 arranged at the upper part of the side edge of the drain flash tank sprays temperature-reducing water into the drain flash tank, so that steam in the drain flash tank is better condensed, the temperature of condensed water in the drain flash tank is controlled, and the condensed water condensed in the drain flash tank is discharged into a condenser hot well 12 at the bottom of the drain flash tank through a corresponding drain water pipe 9;
the drain flash tank liquid level meter 15 is used for monitoring the condensate water liquid level of the drain flash tank, so that the condensate water in the drain flash tank is timely discharged through the drain pump 8, and the liquid level scores are three, namely two remote transmission type guided wave radar liquid level meters and a local magnetic turning plate liquid level meter;
when the liquid level of the condensed water in the drainage flash tank reaches a high I-position alarm value, one drainage pump 8 on a pipeline of a drainage drain pipe 9 is automatically started, the condensed water of the drainage flash tank is pumped into a condenser hot well 12, when the liquid level of the condensed water in the drainage flash tank rises and reaches a high II-position alarm value, the other drainage pump 8 is automatically started in a linked mode, and after the liquid level of the condensed water in the drainage flash tank is kept at a normal value, the two drainage pumps 8 are sequentially stopped;
when the two drainage pumps 8 are started, the liquid level of the drainage flash tank continues to rise, and the overflow pipeline 7 can enable condensed water in the drainage flash tank to overflow to the condenser hot well 12;
when the unit is in the shutdown maintenance stage, the condensed water in the drainage flash tank is completely discharged through the drainage pipeline 10 arranged at the bottom of the drainage flash tank, so that the maintenance work can be carried out conveniently.
The invention has the beneficial effects that:
the connection mode of the system in the invention ensures that the whole drainage system is in a complete vacuum state, thereby effectively and reliably maintaining the vacuum degree of the unit during operation. In addition, when the plant is arranged at a low position, the drainage system selects the connection mode to effectively prevent the drainage flash tank from flowing back to the steam turbine cylinder through the drainage pipe when the drainage flash tank is full of water, so that the steam turbine water impact accident is caused.
The invention can improve the reliability of the steam turbine drainage system of the combined cycle generator set arranged at a low position in the operation process. Through recycling the drainage, the heat economy of the unit is improved, the water inlet accident of the steam turbine can be effectively prevented in the running process, and the safe and stable running of the unit is ensured.
The invention ensures the running safety of the low-position arranged combined cycle unit in the starting and stopping processes, simultaneously avoids the waste of working media and improves the heat economy of the unit.
Drawings
FIG. 1 is a schematic diagram of the system of the present invention.
The system comprises a low-pressure drain header 1, a low-pressure drain pipe 2, a drain flash tank temperature-reducing water pipeline 3, a steam exhaust pipeline 4, a low-pressure drain flash tank 5, a high-pressure drain flash tank 6, an overflow pipeline 7, a drain pump 8, a drain pipe 9, a drain pipeline 10, a condenser 11, a condenser heat well 12, a high-pressure drain pipe 13, a high-pressure drain header 14 and a drain flash tank liquid level meter 15.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
As shown in fig. 1, a drain system of a combined cycle unit arranged at a low position comprises a condenser 11, a drain flash tank desuperheating water pipeline 3, a drain header, a drain pipe 9, a steam exhaust pipeline 4, an overflow pipeline 7, a drain pipeline 10 and a drain flash tank liquid level meter 15;
the drain flash tank is connected with a steam exhaust pipeline 4, a drain flash tank temperature-reducing water pipeline 3, a drain collecting pipe, an overflow pipeline 7, a drain pipe 9 and a drain flash tank liquid level meter 15.
One end of the steam exhaust pipeline 4 is connected with the top end of the drainage flash tank. The drain flash tank temperature-reducing water pipeline 3 is derived from a condensate pump outlet and is connected to the upper part of the side edge of the drain flash tank. The drain pipe on each steam pipeline is connected to the drain collecting pipe of the drain flash tank, and the drain collecting pipe is connected to the middle of the side edge of the drain flash tank. The overflow conduit 7 is arranged in the middle and lower part of the side edge of the hydrophobic flash tank. One end of the drainage drain pipe 9 is connected with the bottom of the drainage flash tank. One end of a drainage flash tank liquid level meter 15 is arranged at the side edge of the drainage flash tank.
In one embodiment, the vent line 4 is divided into a high pressure hydrophobic flash tank 6 vent line 4 and a low pressure hydrophobic flash tank 5 vent line 4.
In one embodiment, an electric valve and a check valve are arranged on the exhaust pipe 4, and the outlet is connected to the throat of the condenser.
In one embodiment, the flash tank is divided into a high pressure flash tank 6 and a low pressure flash tank 5, which receive the high pressure level of flash and the low pressure level of flash during operation of the unit, respectively.
In one embodiment, the high pressure hydrophobic flash tank 6 and the low pressure hydrophobic flash tank 5 are separately arranged and connected in the same way.
In one embodiment, the hydrophobic headers are divided into a high pressure hydrophobic header 14 and a low pressure hydrophobic header 1. The pressure-staged drain pipe connections are connected to the high pressure drain header 14 and the low pressure drain header 1, respectively, by pressure-staging the drain.
In one embodiment, the high pressure and low pressure hydrophobic headers 14 and 1 are connected to a high pressure hydrophobic flash tank and a low pressure hydrophobic flash tank 5, respectively.
In one embodiment, the drain pipe 9 is divided into two branches after a main pipe is led out from the bottom of the drain flash tank, and each branch is provided with a drain pump 8, an electric valve and a check valve. The end of the pipeline is connected with a condenser hot well 12.
In one embodiment, the sewerage pipe 10 is connected to the main pipe of the hydrophobic drain pipe 9.
In one embodiment, a non-return valve is arranged on the drain flash tank overflow pipe 7, and the outlet is connected to the condenser hot well 12.
In one embodiment, the drain 10 is provided with an electrically operated valve and a manually operated valve, and the drain 10 is terminated to a condensate pump sump.
In one embodiment, the hydrophobic flash tank level gauge 15 is provided with two remote guided wave radar level gauges and one in-situ magnetic flip plate level gauge.
The working principle of the invention is as follows:
during the operation of the steam turbine, the pressure-classified drain flows into the low-pressure drain header 1 and the high-pressure drain header 14 through the low-pressure drain pipe 2 and the high-pressure drain pipe 13, respectively. After the drainage reaches the low-pressure drainage flash tank 5 and the high-pressure drainage flash tank 6, after the processes of temperature reduction, pressure reduction and flash expansion are carried out in the drainage flash tank, part of steam generated after the flash tank is expanded enters the condenser 11 through the steam exhaust pipeline 4 connected to the top of the drainage flash tank to be condensed again, and therefore the working medium is recovered.
Arrange in the hydrophobic flash tank temperature reduction water pipe 3 on hydrophobic flash tank side upper portion and spout into the hydrophobic flash tank in the temperature reduction water, make the better condensation of steam in the hydrophobic flash tank, control the temperature of the interior condensate water of hydrophobic flash tank simultaneously.
The condensed water condensed in the drain flash tank is discharged into a condenser hot well 12 at the bottom of the drain flash tank through a corresponding drain pipe 9.
The drain flash tank level meter 15 is used for monitoring the level of drain flash tank condensate water, so that the condensate water in the drain flash tank is timely discharged through the drain pump 8. The liquid level scores are three, namely two remote transmission type guided wave radar liquid level meters and an in-situ magnetic turning plate liquid level meter, so that the reliability of liquid level monitoring of the drainage flash tank is ensured.
When the liquid level of the condensed water in the drainage flash tank reaches a high I-position alarm value, a drainage pump 8 on a pipeline of a drainage pipe 9 can be automatically started, and the condensed water of the drainage flash tank is pumped into a condenser hot well 12. When the level of the condensed water in the drainage flash tank rises and reaches a high II level for alarming, the other drainage pump 8 can be automatically started in a linked mode. After the level of the condensed water in the drain flash tank is kept at a normal value, the two drain pumps 8 are stopped in sequence.
After the two drainage pumps 8 are started, the liquid level of the drainage flash tank continues to rise, the overflow pipeline 7 enables the condensed water in the drainage flash tank to overflow to the hot well 12 of the condenser, the whole system is protected, the condensed water of the drainage flash tank is effectively prevented from overflowing the drainage collecting pipe, the drainage pipeline flows into the steam turbine, and water hammer accidents of the steam turbine are caused.
When the unit is in a shutdown maintenance stage, the condensed water in the drainage flash tank can be thoroughly discharged through the drainage pipeline 10 arranged at the bottom of the drainage flash tank, so that the maintenance work can be conveniently carried out.
Because the whole drainage system is not communicated with the atmosphere during normal operation, the whole drainage system effectively ensures the vacuum degree of the steam turbine and further ensures the normal operation of the unit.
The drainage system provided by the invention enables the unit to effectively recover the working medium and heat in the operation process, avoids the thermal economic loss caused by the discharge of the working medium, improves the unit efficiency and saves energy. Meanwhile, powerful guarantee is provided for the safety of unit operation.
The meanings of the symbols in FIG. 1 are shown in Table 1.
TABLE 1 description of the symbolic meanings
The invention provides some ideas and methods for the operation safety of the drainage system of the combined cycle unit arranged at the low position, and the method is suitable for medium and large combined cycle units arranged at the low position, but not limited to the units. All the above description sets forth the fundamental principles of the invention, its essential features and the advantages of the invention. The present invention is not limited by the above-described embodiments, which are merely illustrative of the principles of the present invention. The present invention may be subject to various changes and modifications depending on the actual design and construction, which are within the scope of the present invention as claimed.