156 results about "Boiler feedwater" patented technology

The invention discloses a double-turbine power generation device suitable for a thermal power generating unit, relates to the technical field of thermal power generation, and mainly aims to improve the power generation efficiency of the thermal power generating unit. According to the main technical scheme, a boiler system is connected with steam inlet valves of a first steam turbine power generation sub-set and a second steam turbine power generation sub-set through pipelines, and corresponding steam is conveyed to the two sub-sets by adjusting the opening degree of a valve to be matched with a load distribution target. After the two subsets do work, part of steam is fed into a steam extraction heat regeneration system to recover heat and is used for heating boiler feed water; and the residual exhaust steam enters the condenser system to be condensed into water, and the condensed water is conveyed to the steam extraction heat regeneration system to be heated to become boiler feed water, so that circulating power generation is realized.

The utility model provides a system for directly recycling wastewater of a medium-high pressure boiler. The system comprises a collecting and regulating tank, a heat exchanger, a coagulation clarifier, a multi-medium filter, an ultrafiltration system, a secondary reverse osmosis system, an EDI (Electronic Data Interchange) device, a mixed bed and a user high-purity water tank which are connected in sequence, the second-stage reverse osmosis system comprises a first-stage reverse osmosis system and a second-stage reverse osmosis system, the first-stage reverse osmosis system comprises a first-stage RO raw water tank, a precision filter and a first-stage RO device, effluent of the ultrafiltration system enters the first-stage RO raw water tank and then enters the precision filter to be filtered, and water produced by the precision filter is fed into the first-stage RO device; the second-stage reverse osmosis system comprises a second-stage RO raw water tank and a second-stage RO device, fresh water produced by the first-stage RO device is fed into the second-stage RO raw water tank and then enters the second-stage RO device, and fresh water produced by the second-stage RO device is fed into the EDI device to be treated. According to the utility model, a full-flow treatment system is developed aiming at the water quality condition of the wastewater of the medium-high pressure boiler, and the finished water can stably meet the water supply requirements of the medium-high pressure boiler.

The invention discloses an automatic boiler dosing method based on response surface modeling-PID coupling control, and relates to the field of thermal power boiler feed water treatment, and the method comprises the steps: collecting historical operation data, and employing a Pearson correlation coefficient method to screen out the correlation between the frequency of a boiler dosing pump and each parameter index; bBD design is carried out through response surface analysis, response values and factors in the dosing process are determined, and three different levels are selected for the factors; establishing a mathematical model between the response value and each factor through model fitting; setting a target value, substituting the target value into the response surface model for calculation, and taking the calculated value as a feedforward input quantity of a PID controller of the boiler dosing system; setting the deviation between the target value and the feedback value to obtain the adjusting frequency of dosing; and obtaining the final frequency of the ammonia adding pump by adopting a weighted average algorithm. According to the method, a mathematical model is constructed, an algorithm model and control logic are fused, and real-time response and control optimization of the boiler dosing control process are achieved.

The application provides a coupling system and a control method for improving the variable load rate of a secondary reheat unit integrated with a medium-temperature energy storage, wherein the medium-temperature energy storage system is connected with the high-pressure cylinder outlet through a high-pressure cylinder outlet steam extraction valve during the energy storage process, is connected with the deaerator outlet through a pressure relief valve, is connected with the feed water pump outlet through a deaerator outlet regulating valve during the energy release process, and is connected with the boiler feed water inlet through a pipeline, so as to form a secondary reheat unit integrated with the medium-temperature energy storage; and a load splitting method is provided, which splits the whole unit load instruction into a medium-temperature energy storage system load instruction and a secondary reheat unit boiler coordination system load instruction, and the medium-temperature energy storage system load instruction is realized through high-pressure cylinder exhaust valve opening degree control and deaerator outlet regulating valve opening degree control in the load decreasing and increasing processes; through the coupling system and the load splitting method, the time-space transfer of the unit energy in the variable load process is realized, the variable load rate of the secondary reheat unit is improved, and the flexibility of the unit is enhanced.

This invention provides a boiler system that can effectively utilize the heat contained in ammonia decomposition gas. Furthermore, it provides a boiler system that can maintain the temperature of the ammonia decomposition gas at the boiler inlet within a predetermined temperature range. [Solution] The boiler system comprises an ammonia decomposition device that decomposes ammonia to produce ammonia decomposition gas containing hydrogen and nitrogen, a boiler that burns the ammonia decomposition gas as fuel, an ammonia decomposition gas supply line that supplies the ammonia decomposition gas from the ammonia decomposition device to the boiler, a feedwater line that supplies feedwater to the boiler, and a heat exchanger that heats the feedwater by exchanging heat between the ammonia decomposition gas and the feedwater.

The utility model discloses a boiler feed water treatment device which comprises a hollow fiber membrane pipe, a vacuum connector and shells detachably installed at the two ends of the vacuum connector, a water inlet pipe is installed at the position of the shell on one side, and a water outlet pipe is installed at the position of the shell on the other side. The shell moves in the axial direction of the water inlet pipe and the water outlet pipe. The hollow fiber membrane tubes are mounted on the two end surfaces of the vacuum connector and located in the shell, and a water passing tube group is mounted through the vacuum connector; according to the device, the hollow fiber membrane tube can be directly exposed through transverse movement of the shell, so that the hollow fiber membrane tube can be conveniently maintained or replaced, and relatively convenience is provided.

An apparatus for steam reforming includes a reactor, a condensate separator, a condensate stripper, and a steam boiler. The reactor produces hydrogen and is connected to the condensate separator such that a gas mixture is conducted from the reactor into the condensate separator. The condensate separator and the condensate stripper are connected so that condensate separated out in the condensate separator is conducted into the condensate stripper. The condensate separator and the steam boiler are connected such that cleaned condensate can be conducted into the steam boiler. The steam boiler is connected to the reactor and to the condensate stripper in a steam-conducting manner. The boiler water feed line of the steam boiler is connectable to the condensate stripper in a liquid-conducting manner. A supply from the boiler water feed line is at a same location of the condensate stripper as a supply of the condensate from the condensate separator.

The utility model relates to the technical field of boiler make-up water, in particular to a gas turbine boiler make-up water deoxidizing and desalting device which comprises a deoxidizing cylinder, a fixing frame is fixedly connected to the outer portion of the deoxidizing cylinder, a deoxidizing assembly used for deoxidizing make-up water is arranged in the deoxidizing cylinder, and the deoxidizing assembly comprises a rotating cylinder rotationally connected to the interior of the deoxidizing cylinder. A first rotational flow plate and a second rotational flow plate are fixedly connected to the exterior of the rotary drum, the length of the first rotational flow plate is larger than that of the second rotational flow plate, and a liquid inlet pipe and a material adding pipe are communicated with the top of the deoxidizing drum. The efficient deoxidization and desalination integration is realized, the problems of large occupied space and non-uniform fluid distribution caused by a split structure of traditional equipment are avoided, the introduction of a rotating structure improves the water flow disturbance, and the deoxidization and desalination process is more sufficient.

The present application belongs to the technical field of oil and gas field produced water treatment, and particularly relates to an ammonia nitrogen treatment system and method for oil field sulfur-containing produced water. The method comprises the following steps: sending the oil field sulfur-containing produced water into a first buffer pool, reducing sulfides through two-stage aeration of a cyclone aerator and an aeration nozzle device, overflowing from the first buffer pool to a second buffer pool when the first buffer pool reaches a water outlet height, and removing ammonia nitrogen by adding an ammonia nitrogen remover through a conventional dosing port of a dosing device. The present application fully utilizes the characteristics of aeration sulfur removal, and through the addition of a targeted chemical agent and the control of key parameters, purifies and softens the oil field sulfur-containing produced water in one step. After treatment, the water quality only needs to be further filtered by two stages of fine filtration, and the outlet water quality directly meets the steam boiler feed water requirements.

The utility model discloses an energy-saving device for hazardous waste incineration flue gas treatment, which comprises a hazardous waste treatment system and an energy circulation system which are matched with each other, and the hazardous waste treatment system comprises a rotary kiln (1), a secondary combustion chamber (2), a waste heat boiler (3) and a dry deacidification and bag-type dust collector (4), the energy circulation system comprises a flue gas heat collector (5), a wet slag drying system (6), a primary air heater (7), a secondary air heater (8) and a boiler feed water heater (9); an outlet of the bag-type dust collector (4) is connected with the flue gas heat collector (5), a waterway outlet (5a) of the flue gas heat collector (5) is respectively connected with the wet slag drying system (6), the primary air heater (7), the secondary air heater (8) and the boiler feed water heater (9) through four branches, and return water is connected with the flue gas heat collector (5) through a circulating pipe (24). The waste heat recycling device has the advantages that waste heat generated by hazardous waste incineration is effectively recycled, and the hazardous waste disposal cost is reduced.

The utility model provides a multi-container stepped water supply device which comprises a concentration tank, a water storage chamber, a connecting pipe, a buoyancy valve assembly, a water inlet pipe and a water outlet pipe. A plurality of water storage chambers are arranged, and the communication of every two adjacent water storage chambers is controlled by the buoyancy valve assembly; therefore, direct heat exchange among various kinds of water is prevented, and the temperature of water supplied to the boiler is prevented from being affected. Energy for boiler heating is reduced, and energy consumption is reduced.

The embodiment of the invention provides a coupled double-tank active solar photo-thermal boiler complementary five-stage steam supply system. The coupled double-tank active solar photo-thermal boiler complementary five-stage steam supply system comprises a coal-fired power generation unit and a water supply regenerative system, wherein the coal-fired power generation unit comprises a boiler, a steam turbine high-pressure cylinder, a reheater, a steam turbine intermediate-pressure cylinder and a steam turbine low-pressure cylinder which are connected in sequence; the tower type solar photo-thermal system comprises a low-temperature molten salt tank, a solar heat collection tower and a high-temperature molten salt tank which are connected through a molten salt pump and a pipeline; an outlet of the high-temperature molten salt tank is sequentially connected with hot-side molten salt inlets of the main heat exchanger and the second-stage heat exchanger through a molten salt pump, and a cold-side molten salt outlet of the second-stage heat exchanger is connected to the low-temperature molten salt tank; a water supply inlet of the main heat exchanger is connected with a boiler water supply pipeline, and a steam outlet is connected to a boiler main steam system; a feed water inlet of the second-stage heat exchanger is connected with an outlet of a pressurizing water pump, an inlet of the pressurizing water pump is connected to a condensed water pipeline of an outlet of the deaerator, and a steam outlet of the second-stage heat exchanger is used for providing industrial steam supply of a first pressure grade.

This invention belongs to the field of thermal power generation and discloses a steam preheating system for the primary air of a lignite boiler, including a steam matching system, a primary air heating system, and a feedwater heating system. This invention achieves stable full-load control of the primary air temperature in a lignite boiler above 350℃, solving the drying output problem of medium-speed mill pulverizing systems in lignite boiler applications. This invention is applicable to lignite power plant boilers of various capacities equipped with medium-speed mill positive pressure direct-fired pulverizing systems. It is suitable for the overall design of boiler systems in newly built lignite power plants, as well as for energy-saving upgrades and retrofits of the primary air systems in existing lignite power plant boilers. It is used to stably increase the inlet temperature of the primary air from the lignite boiler mill, ensuring the drying output and coal powder fineness of the medium-speed mill pulverizing system, while optimizing the steam supply of the boiler feedwater heating system, thus improving the overall operational economy and safety stability of thermal power generating units.

The invention discloses a coal-fired power generation system for coal power unit structure reconstruction and thermodynamic system reconstruction, which comprises a power generator and two steam turbines, and the power generator is connected in series between the two steam turbines; a steam outlet of the superheater is connected with steam inlets of high-pressure cylinders of the two steam turbines through a main steam pipeline, and steam outlets of the high-pressure cylinders are connected with a steam inlet of the reheater through a reheating cold section steam pipeline. A steam outlet of the reheater is respectively connected with steam inlets of intermediate pressure cylinders of the two steam turbines through reheating hot section steam pipelines; the system further comprises a heat storage system, a superheated steam pipeline is led out of the main steam pipeline or the reheating hot section steam pipeline and connected with the heat storage system, the heat storage system is connected with the deaerator through a drainage pipeline, and two heating sections are formed on the boiler water supply pipeline and connected with the heat storage system to heat supplied water. On the premise of economic conditions and intrinsic safety, coal power deep peak regulation, efficient regulation and wide-load efficiency protection are achieved.

The utility model provides a fused salt energy storage device and an electric furnace waste heat recovery device, and belongs to the technical field of electric furnace waste heat recovery. A heat storage unit, a heat storage pipeline and a heat release pipeline are arranged between a waste heat boiler and steam utilization equipment; high-parameter steam generated by the waste heat boiler is guided into a coil pipe of the heat storage unit through a boiler steam conveying pipe, heat storage is conducted on the high-parameter steam in a box body through a low-temperature fused salt medium, and steam condensation water serves as waste heat boiler water through a boiler water supply pipe; when heat energy in the heat storage unit is used, condensed water of the steam utilization equipment is conveyed into the coil pipe of the heat storage unit through the condensed water conveying pipe, the high-temperature fused salt medium in the box body exchanges heat with the condensed water in the coil pipe, and formed high-parameter steam is supplied to the steam utilization equipment through the steam conveying pipe. The modularized heat storage structure effectively solves the problems that in an existing double-tank technology, waste heat integration and control are difficult, stability is poor, and the molten salt corrosion leakage risk is high.

The invention relates to the field of boiler water feeding, and discloses a control method and system for preventing cold water and cold steam from entering a steam feed pump, and the method comprises the steps: collecting RB or load and temperature and pressure values on a pipeline connected with the steam feed pump in a boiler water feeding system in real time, judging whether the RB or load drop rate of the boiler water feeding system exceeds a safety threshold value or not, and if yes, judging whether the RB or load drop rate exceeds the safety threshold value; if yes, the boiler water supply system breaks down, the fault of the system is judged step by step and processed correspondingly, the possible cold water and steam inlet accidents of the steam feed pump can be pre-judged in advance, the electric water feed pump is started in time for standby application, and sudden tripping of the steam feed pump, boiler water supply interruption and boiler MFT are prevented; the operation stability of the boiler water supply system is improved, and faults can be found and solved in time.

The utility model relates to an efficient energy-saving no-load running check valve. The valve comprises a valve body, a main valve channel is arranged in the valve body, one end is used for being connected with a boiler, the other end is used for being connected with a water pump, a main valve clack is arranged in the valve body, and an auxiliary channel is arranged on the valve body and used for being communicated with a deaerator or a condenser. The valve body is provided with an electromagnetic valve used for stopping or opening the auxiliary valve channel, and the electromagnetic valve is in a normally-open type. The valve is directly and vertically arranged at the outlet of the water pump. In the working state, when the water feeding pump is just started or the water feeding amount is as small as the limit requirement, the electromagnetic valve is not electrified and is kept in the open state, the main valve clack of the valve is normally opened, and fed water enters the deaerator or the condenser through the auxiliary valve channel. According to the water supply requirement of the boiler, when the required flow is larger than a certain value (the minimum flow of the pump), the electromagnetic valve is powered on, and the auxiliary valve channel is stopped. Compared with the prior art, a shifting fork, an auxiliary valve clack and linkage action between the shifting fork and the auxiliary valve clack are omitted in the valve body, the structure is simple, faults are not prone to occurring, and use is convenient.

The utility model belongs to the technical field of thermal power plant equipment, and provides a main path and bypass switching device of a once-through boiler water supply system of a thermal power plant, which comprises a main path pipeline, a bypass pipeline and a buffer tank, two ends of the main path pipeline are respectively connected with a water supply inlet and a water supply source of a once-through boiler, and a main path stop valve is arranged on the main path pipeline; the bypass pipeline and the main pipeline are connected in parallel between a water supply inlet and a water supply source of the once-through boiler, and a bypass regulating valve is arranged on the bypass pipeline; the buffer tank is connected to the bypass pipeline, the length direction of the buffer tank is arranged in the transverse direction, and a buffer plate is arranged in the buffer tank. By means of the technical scheme, the problem that pipelines and equipment are damaged due to the fact that the water attack phenomenon is prone to being generated when an existing switching device switches water ways is solved.

The boiler flue gas treatment system is used for treating flue gas generated by boiler combustion in a power plant and comprises a heat exchange device, a flue gas treatment device and a boiler feed water preheating system, and the boiler feed water preheating system comprises a first heating system and a second heating system located on the downstream of the first heating system. The first heating system comprises more than one first heat exchanger and directly utilizes first steam extracted from a steam turbine to heat condensate water, and the second heating system comprises a steam pressurizing device for pressurizing second steam; and a second heat exchanger for further heating the condensed water heated by the first heating system by using the second steam supercharged by the steam supercharging device. By means of the boiler flue gas treatment system, even if the load of a power plant unit is extremely reduced, the flue gas treatment system can operate normally, and existing equipment does not need to be transformed on a large scale.

The present application belongs to the technical field of leakage detection of water supply heating system, and discloses a high-pressure heater leakage detection system and method, which comprises a tracer adding subsystem, a sampling subsystem, a detection subsystem and an AI processing unit; the tracer adding subsystem is used for injecting a helium tracer into a high-pressure heater in a boiler water heating system; the sampling subsystem is used for sampling the exhaust of the high-pressure heater to obtain a high-pressure heater exhaust sample; the detection subsystem is used for detecting the content of the helium tracer in the high-pressure heater exhaust sample to obtain tracer content detection data; and the AI processing unit is used for analyzing the tracer content detection data to obtain a high-pressure heater leakage detection result; the present application utilizes the principle that gas will leak into the steam side of the high-pressure heater when the heat exchange tube of the high-pressure heater leaks, and realizes rapid and accurate detection of the leakage of the high-pressure heater by analyzing the helium tracer content detection data in the sample.

The utility model relates to the technical field of energy-saving and water-saving system equipment, and discloses an SGT-800 type gas turbine system for increasing production water temperature by using cooling return water temperature rise, which comprises a heat exchanger and a condensing tower, a heat exchange mechanism is arranged on one side of the condensing tower, the heat exchange mechanism comprises a heat exchanger, a plurality of heat exchange fins are arranged in the heat exchanger, and the heat exchange fins are arranged on the other side of the condensing tower. A first water inlet hole, a second water inlet hole, a first water outlet hole and a second water outlet hole are formed in the four corners of each heat exchange piece correspondingly, and a first drainage groove and a second drainage groove are formed in one side of the outer wall of each heat exchange piece. In the utility model, the plate-type water-water heating heat exchanger is adopted, and the original steam heating mode is optimized into a closed cooling water return heating mode. On the system, a heating pipeline enters and returns, that is, inlet water is closed cooling water return water, enters a circulating water return main pipe after heat exchange and enters a cooling tower, a raw water heating pipeline raw water workshop enters a heat exchanger, and enters a boiler make-up water workshop for use after heat regeneration.

The utility model discloses a conversion and gasification waste heat comprehensive utilization device, which is characterized in that conversion gas enters a secondary conversion furnace for chemical reaction to release heat, and then enters a low-pressure steam generator for heat exchange with boiler water to produce 0.5 MPa saturated steam. After heat exchange, the converted gas enters a boiler feed water preheater to exchange heat with boiler feed water, the boiler feed water after heat exchange enters a low-pressure steam generator, the converted gas enters a first desalted water heater to exchange heat with normal-temperature desalted water, and hot desalted water after heat exchange enters a gasification deaerator. One path of low-pressure flash steam discharged from the top of the gasification low-pressure flash separator enters the gasification deaerator, the other path of low-pressure flash steam enters the generator set for power generation, during normal production, the third regulating valve is in a closed state, and all the gasification low-pressure flash steam is used for power generation. The conversion low-grade chemical reaction waste heat is used for heating the desalted water of the gasification deaerator, the gasification low-pressure flash steam is reduced and used for heating the desalted water of the gasification deaerator, the generating capacity of the gasification low-pressure flash steam is improved, and comprehensive utilization of conversion and gasification waste heat is achieved.

The invention discloses a sulfur recovery flue gas waste heat and condensed water waste heat recovery system and process. The system comprises a steam superheater, an incinerator waste heat boiler, an economizer, a boiler feed water preheater, a condensed water heat exchanger, a condensed water recovery tank and a condensed water pump which are sequentially connected. The system further comprises a flue, the flue is connected with the steam superheater, and the incinerator waste heat boiler and the economizer are arranged in the flue. Low-temperature waste heat of condensed water and incineration flue gas can be recovered at the same time, the boiler feed water preheater is arranged, low-temperature boiler feed water enters the economizer after the temperature of the low-temperature boiler feed water is increased through the boiler feed water preheater, and dew point corrosion of the economizer can be prevented. The economizer is arranged in the flue, so that low-temperature waste heat of flue gas at an outlet of the waste heat boiler can be efficiently recycled; the condensation water heat exchanger is arranged to recover low-temperature waste heat of condensation water, and meanwhile the cooling load of the condensation water recovery system is reduced. The method can be suitable for various working conditions of normal production of sulfur recovery, failure of tail gas treatment and start-stop.

This invention provides an online measurement method for leakage from high-pressure cylinder exhaust to third-stage extraction steam in a combined-cylinder turbine unit, belonging to the field of combined-cylinder turbine operation monitoring technology. The method includes: establishing a typical data benchmark to obtain the benchmark third-stage extraction enthalpy value; real-time acquisition of boiler feedwater flow rate, exhaust parameters of each high-pressure heater and cylinder as raw parameters; preprocessing the raw data and calculating the enthalpy value at each state point based on the preprocessed data; establishing and solving the heat balance equations for each high-pressure heater based on the feedwater flow rate and enthalpy value to obtain the steam inlet flow rate of the third high-pressure heater; combining the benchmark third-stage extraction enthalpy value, high-pressure cylinder exhaust enthalpy, enthalpy after mixing of the third-stage extraction steam, and steam inlet flow rate of the third high-pressure heater to establish a set of mass and energy conservation equations for the mixer, and back-calculating the leakage amount; displaying the leakage amount in real time and providing early warning. This invention requires no shutdown modification and can accurately quantify the internal leakage from high-pressure cylinder exhaust to third-stage extraction steam online, effectively improving the unit's economy and safety.

The invention relates to the technical field of waste heat recovery, in particular to a system and method for recovering compression heat of an air compressor for preheating boiler feed water. The system comprises an air compressor waste heat recovery subsystem and a boiler feed water preheating subsystem. The air compressor waste heat recovery subsystem comprises a multi-stage centrifugal air compressor, a first-stage compressor, a second-stage compressor and a third-stage compressor are sequentially integrated in the multi-stage centrifugal air compressor, and an outlet of the first-stage compressor and an outlet of the second-stage compressor are connected to the hot side of the efficient heat exchanger through pipelines. The cold side of the efficient heat exchanger, the circulating water pump and the surge tank form a closed circulating water loop through pipelines; the make-up pump is connected to the closed circulating water loop; the boiler feed water preheating subsystem comprises a desalting water tank, a deoxidizing feed pump, a water-water heat exchanger, a deaerator and a boiler which are sequentially connected through pipelines, and the water-water heat exchanger is connected into a circulating water pipeline of the air compressor waste heat recovery subsystem. Compression heat of the centrifugal air compressor is recycled and used for preheating boiler feed water. The waste heat utilization rate is improved.

The invention discloses a super-hydrophobic membrane for boiler feed water oxygen removal and a preparation method thereof.The preparation method comprises the steps that octadecyl trichlorosilane is dissolved in n-octane, surface spraying is conducted with a commercial polyvinylidene fluoride (PVDF) membrane as a base membrane, and after spraying is completed, the PVDF membrane is dried; the preparation method comprises the following steps: adding zinc oxide nanoparticles into n-octane for ultrasonic dispersion, adding perfluorodecyl trichlorosilane in a stirring state to obtain fluorinated zinc oxide, and spraying the fluorinated zinc oxide on a PVDF film to form a micro-nano composite structure on the surface of the film, thereby greatly enhancing the hydrophobicity of the film. When the membrane prepared by the method is applied to a boiler make-up water deoxygenization process, the removal rate of oxygen in water can be effectively improved.

The boiler water supply sampling system comprises a primary cooler, the top of a cooler body is connected with one end of a three-way sampling pipe through a flange, and the other two ends of the three-way sampling pipe are connected with a water supply pump and a pressure gauge respectively and used for inputting high-temperature sampling water; the cooler main body is spirally provided with a cooling coil, and the cooling coil vertically extends downwards from the top wall of the cooler main body to the bottom of the cooler main body and then spirally ascends; the secondary temperature and pressure reducer comprises a U-shaped pipe communicated with an outlet of the cooling coil; the U-shaped pipe is sequentially connected in series with the needle valve and the circulating groove; a water inlet of the online pH monitor is connected with an outlet of the circulation tank, and a monitoring signal is accessed to the automatic dosing control system; sampling of the high-temperature boiler feed water on-line pH detector is achieved, the whole system from the sampling opening to the detector is closed in detection, free of pollution and high in precision, real-time accurate monitoring and automatic adjustment of the feed water pH value are achieved, and monitoring signals are monitored in real time.

The utility model discloses a coal-fired unit rapid and flexible peak and frequency regulation system based on high-temperature working medium energy storage / supply, which relates to the field of conventional power generation technology and energy storage technology and comprises a coal-fired unit thermodynamic cycle system and a high-temperature furnace water energy storage / supply system, the high-temperature furnace water storage and supply / energy system is deeply coupled with the coal-fired unit thermodynamic cycle system, and the power capability and the power generation load of the coal-fired unit are quickly improved by reducing the steam extraction amount of each stage of a steam turbine in the coal-fired unit thermodynamic cycle system, so that the climbing rate of the coal-fired unit is improved; and meanwhile, through direct cooperative energy supply of the high-temperature boiler water storage / energy supply system, the high-enthalpy-value working medium stored by the high-temperature boiler water storage / energy supply system heats boiler feed water in the regenerative system, the temperature of the boiler feed water is increased, then the boiler steam yield is increased, and the rapid variable load response capacity of the coal-fired unit is improved.

The utility model discloses a dual-pressure gas turbine waste heat boiler sharing an economizer, which comprises a boiler flue, and a second high-pressure superheater, a first high-pressure superheater, a high-pressure evaporator, a low-pressure superheater, a high-pressure economizer high-temperature section, a low-pressure evaporator and a high amp are sequentially arranged in the boiler flue; disclosed is a low-pressure shared economizer. High amp; the low-pressure shared economizer is communicated with a boiler water supply inlet and a high amp; the low-pressure shared economizer communicates with the low-pressure boiler barrel through a pipeline, and meanwhile the amp is high; the low-pressure shared economizer further communicates with the high-pressure economizer high-temperature section through a pipeline. According to the dual-pressure waste heat boiler, only one water feeding pump is adopted, steam of two different pressure grades is generated, the system is greatly optimized, and the investment and construction cost is reduced; high amp; the working medium flow circulating in the low-pressure shared economizer is the total flow of a high-pressure system and a low-pressure system, and the vaporization risk of the economizer is reduced; the working medium temperatures of all the hot surfaces are increased step by step, flue gas heat is utilized in a cascade mode, and the efficiency of the waste heat boiler is improved to the maximum degree.

The utility model provides an operation system configuration of a coal power unit based on feed water supplementary heating, which is characterized in that on the basis of an existing boiler feed water heating system, a newly-added final-stage high-pressure heater and a newly-added external steam cooler are additionally arranged on a water supply pipeline, and a steam side inlet of the newly-added external steam cooler is connected with a pressurization module; steam lower than the target steam extraction pressure grade is introduced into an inlet of the pressurization module, and a steam side outlet of the newly-added external steam cooler is connected with a steam inlet of the newly-added final-stage high-pressure heater; supplementary heating is conducted on feed water heated by an existing final-stage high-pressure heater at the position of a newly-added external steam cooler and in the newly-added final-stage high-pressure heater, so that the temperature of feed water entering a furnace of a unit under the deep peak regulation working condition is increased, and meanwhile certain feed water pressure is maintained to enable the feed water at an outlet of a coal economizer to be kept at a certain supercooling degree; dry-state operation of the boiler is maintained under the deep peak regulation working condition, the hydrodynamic stability is kept, and the denitration system is continuously and stably put into operation.