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Novel efficient water supply heat recovery system for secondary reheating unit

A secondary reheating and reheating system technology, applied in the direction of feed water heaters, preheating, lighting and heating equipment, etc., can solve the problems of increasing exergy loss, damaging the energy saving effect of high parameters, and reducing the work of reheating, so as to improve High-pressure cylinder efficiency, reduce the risk of water shock, increase the effect of output

Active Publication Date: 2015-03-25
章礼道
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  • Summary
  • Abstract
  • Description
  • Claims
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AI Technical Summary

Problems solved by technology

[0004] The high-efficiency ultra-supercritical double-reheating unit has high and medium-pressure cylinder inlet steam temperatures as high as 620°C, and the enthalpy value of the 2-extraction (pre-extraction of the high-pressure cylinder) increases, and the temperature can reach above 540°C; 3-extraction (high-pressure cylinder) 4 extraction (exhaust steam of the high-pressure cylinder) is 434 °C; 5 extraction (pre-stage extraction of the medium pressure cylinder) is as high as 545 °C; 6 extraction (the rear stage extraction of the medium pressure cylinder steam) for the deaerator is still as high as 432 ℃, and even need to use a special temperature and pressure reducer to reduce the temperature and pressure before sending it into the deaerator; 2 pumping, 3 pumping, 4 pumping, 5 pumping, 6 pumping The heat-to-work ratio drops sharply, and the use of high-enthalpy, high-superheat high- and medium-pressure cylinders to extract steam to heat the feedwater will greatly increase the exergy (exergy) loss during the feedwater reheating process and increase the heat consumption of the unit
[0005] The reheat temperature gradually rises from 535°C of the subcritical unit to 620°C of the high-efficiency ultra-supercritical unit, and the evolution from primary reheating to secondary reheating makes the problem of increased exergy (exergy) loss during feedwater reheating become a problem. It is becoming more and more prominent. If it is not improved, it will seriously damage the energy saving effect brought by high parameters and double reheating when it reaches 700℃ / 720℃, 700℃ / 720℃ / 720℃ units

Method used

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Embodiment 1

[0055] Combine now figure 2 , taking a 1000MW grade secondary reheat steam turbine unit with design values ​​of main steam temperature / primary reheat steam temperature / secondary reheat steam temperature at 600°C / 620°C / 620°C as an example to illustrate the realization of the invention Preferred way. This type of double reheat steam turbine unit adopts 5 high-pressure heaters and 3 separate steam coolers. The high-pressure cylinder has an extra stage of extraction (steam extraction at the rear stage of the high-pressure cylinder) to send to the No. 3 high-pressure heater, and the high-pressure cylinder exhaust The steam is pumped into No. 4 high-pressure heater with 4 pumps, and the steam used by the deaerator and small machine is pumped with 6 pumps (steam extraction at the rear stage of the medium pressure cylinder).

[0056]A novel high-efficiency feed water recuperation system for secondary reheating units of the present invention includes: No. 1 high-fill steam inlet chec...

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Abstract

The invention provides a novel efficient water supply heat recovery system for a secondary reheating unit, and relates to a novel water supply heat recovery technical scheme for the secondary reheating unit of a thermal power station, wherein the water supply heat recovery system is capable of reducing the heat consumption of the unit remarkably. A new 2 extraction component, a new 3 extraction component and a new 4 extraction component which are lower in enthalpy value and lower in the degree of superheat replace a 2 extraction component, a 3 extraction component, a 4 extraction component, a 5 extraction component and a 6 extraction component which are higher in enthalpy value and higher in the degree of superheat and arranged on a high-pressure cylinder or a middle-pressure cylinder; due to the fact that the exergy loss is reduced greatly in the water supply and heat recovery processes, the output power of a generator is increased remarkably, the heat consumption of the unit is reduced, the operation safety is improved, and obvious heat economy benefits are provided; the degree of superheat of the new 3 extraction component is reduced greatly, so that the opening of the No. 3 high-pressure steam-inlet check regulation valve is controlled to improve the transient response capacity of load increasing of a main engine; the new 2 extraction component, the new 3 extraction component and the new 4 extraction component increase the pressure stage of a 6-stage short blade in an ultrahigh pressure cylinder, the diffluent steam continuously conducts expansion acting, and extracted steam with low enthalpy value is output from connectors of the new 2 extraction component, the new 3 extraction component and the new 4extraction component.

Description

(1) Technical field: [0001] The invention relates to a novel high-efficiency feed water recuperation system for a double reheat unit, which relates to a new feed water recuperation technical scheme used in a thermal power station reheat unit, which can significantly reduce the heat consumption of the unit. (two) background technology: [0002] The double-reheat power plant boiler used in the thermal power station in the prior art is used to supply steam to the double-reheat turbine generator set. The typical steam turbine side main steam temperature / primary reheat steam temperature / second reheat steam temperature The design value is 600°C / 620°C / 620°C; the steam turbine unit for secondary reheating is usually composed of coaxial ultra-high pressure cylinders, high-pressure cylinders, medium-pressure cylinders, low-pressure cylinders and many auxiliary equipment; the primary reheater is arranged in the super Between the exhaust cylinder of the high-pressure cylinder and the pr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F22D1/32F22D1/50
Inventor 章礼道
Owner 章礼道
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