272 results about "Condensate pump" patented technology

The invention discloses an energy-saving efficient refrigerating unit and process for preventing cavitation of a steam condensate pump in the technical field of refrigeration. The energy-saving efficient refrigerating unit comprises a high-pressure generator, a medium-pressure generator, a high-pressure evaporator, the steam condensate pump, a composite power generation compressor and a refrigerating assembly. Heat of saturated steam condensate flowing out of the high-pressure generator is absorbed by the high-pressure liquid refrigerant through the high-pressure evaporator, and the saturated steam condensate is changed into supercooled steam condensate, so that cavitation cannot be generated when the supercooled steam condensate enters the steam condensate pump, an original mode of increasing the height difference between the generator and the steam condensate pump is replaced, and the production efficiency is improved. The cost of a unit pipeline is reduced, meanwhile, the cost of ultrahigh transportation is reduced, heat contained in saturated steam condensate is converted into pressure energy of a high-pressure gaseous refrigerant to be used for driving a composite power generation compressor to work, the pressure energy is converted into electric energy and pressure energy of a low-pressure gaseous refrigerant, and the electric energy is used for a solution pump. The deep utilization of the internal energy of the unit can be realized, and the COP of the unit is improved.

The invention relates to the technical field of coalification black water treatment, and particularly discloses a coal gasification black water flash steam waste heat steam turbine gradient utilization system which comprises a black water flash steam turbine module and a steam exhaust condensation module. The black water flash steam turbine module comprises a high-pressure flash evaporator, a low-pressure flash evaporator, a vacuum flash evaporator, a supplementary condensing steam turbine, a generator and a settling tank, and a water outlet of the vacuum flash evaporator is connected with the settling tank; the steam exhaust condensation module comprises an evaporative condenser and a condensate pump. Through the design of the scale scraping and water uniformizing piece, part of cooling water falling around the heat exchange coil from top to bottom falls on the water uniformizing plate to drive the water uniformizing plate to rotate, when the water uniformizing plate rotates, water on the water uniformizing plate is thrown out under the action of centrifugal force, cooling water without heat exchange can be uniformized to other heat exchange pipes for heat exchange, and the heat exchange efficiency is improved. Therefore, the cooling water flows more uniformly among the heat exchange coils, the utilization rate of the cooling water is improved, and the heat exchange efficiency is improved.

The invention belongs to the technical field of thermal power generation control, and particularly discloses an automatic control method for tripping of a high-pressure heater drain pump of a thermal power generating unit, which comprises the following steps: step 1, gradually reducing the coal quantity of the thermal power generating unit according to a preset first rate, and enabling the thermal power generating unit to run in a sliding pressure manner in a steam turbine tracking manner; 2, the real-time coal quantity of the thermal power generating unit is obtained, the total air volume and the primary air pressure are regulated and controlled according to the real-time coal quantity, meanwhile, the locking preset time of boiler core equipment of the thermal power generating unit is regulated and controlled, and the operation number of a coal pulverizing system is regulated and controlled; 3, the feed water flow of a feed pump, the pressure of a condensate pump, main steam parameters of a steam turbine and the final-stage high-pressure heater liquid level are regulated and controlled; and 4, whether the unit load, the feed water flow, the main steam parameters and the final-stage high-pressure heater liquid level meet the control ending conditions or not is judged in real time, and if not, the step 2 to the step 4 are repeated. According to the method, the non-planned shutdown frequency can be remarkably reduced, and the operation reliability and safety of the thermal power generating unit are greatly improved.

The utility model provides a condensate water recovery system of a compressed air energy storage power station, which comprises a flash tank with a plurality of pipeline inlets, and the pipeline inlets of the plurality of pipeline inlets are respectively connected with drainage pipelines corresponding to all stages of gas-liquid separators. The flash tank is used for receiving condensate water separated by each stage of gas-liquid separator through the drainage pipeline; the condensate pump bypass is connected with the condensate pump in parallel, pipeline inlets of the condensate pump and the condensate pump bypass are connected with a pipeline outlet of the flash tank, and pipeline outlets of the condensate pump and the condensate pump bypass are connected with a circulating cooling system of the compressed air energy storage power station through a recycling pipeline. And the condensate pump or the condensate pump bypass is used for conveying condensate water to the circulating cooling system through the recovery pipeline when being started. According to the scheme, the condensed water separated by each stage of gas-liquid separator can be safely and effectively recovered and utilized, so that the waste of water resources can be avoided.

Provided in the present invention are a primary frequency regulation dynamic simulation method and apparatus based on a thermal power condensate water throttling strategy, which are used for analyzing the dynamic characteristics of a unit when a power plant executes a primary frequency regulation instruction by means of a condensate water throttling strategy after a power disturbance occurs in a power grid. The dynamic characteristics mainly comprise the characteristics of a steam turbine speed governor system, the characteristics of a variable-frequency condensate pump system, the dynamic heat exchange characteristics of a low-pressure heater and extraction steam, the flow characteristics of an extraction steam pipeline, and the output characteristics of a steam turbine body. A moving boundary method is mainly applied to a heat exchange process between condensate water (a cold fluid) and shell-side extraction steam (a hot fluid) in a low-pressure heater. The heat exchange process between the cold and hot fluids can be divided into a superheated section, a phase change section and a subcooled section on the basis of the aggregation state of the extraction steam. When the moving boundary method is applied to a steam turbine regenerative system, the dynamic variation laws of extraction steam temperature and pressure can be more accurately obtained, and the extraction steam pressure on a low-pressure heater side is a key factor in determining the extraction steam flow rate on a low-pressure cylinder side, and is also critical in determining the instantaneous power increment of a steam turbine. Moving boundary method-based frequency regulation dynamic simulation for thermal power condensate water throttling takes into account relatively comprehensive actual process factors, and only one-dimensional modeling along an axial main flow direction is taken into account, thus combining the advantages of fast and accurate simulation. A fast and accurate simulation method is a prerequisite for implementing power grid frequency security analysis. By mastering the dynamic process of power plant load response from the moment a frequency deviation exceeds a dead band to the moment same returns to the dead band, a foundation can be provided for the primary frequency regulation control of power plants and the frequency security analysis of power grids.

The invention provides a vibration reduction method and device for a vertical condensate pump. The vertical condensate pump aims at accurately adjusting resonance points, reducing vibration hazards and improving the running stability of the vertical condensate pump. The vibration reduction method of the vertical condensate pump is applied to the vibration reduction device, and the vibration reduction device comprises a motor, a controller, a fixing support and a lead screw. Acquiring the real-time rotating speed of the vertical condensate pump; on the basis that the real-time rotating speed is matched with a target rotating speed in a preset information base, a vibration reduction adjusting scheme of the vertical condensate pump at the target rotating speed is stored in the preset information base, and the vibration reduction scheme is used for controlling a vibration reduction device to adjust the supporting force of a lead screw for supporting the vertical condensate pump at the target rotating speed. The amplitude data corresponding to the resonance point of the vertical condensate pump is adjusted to be within the corresponding standard amplitude data range; and if the matching is consistent, determining a motor control instruction based on the corresponding vibration reduction adjustment scheme, and sending the motor control instruction to the controller.

The invention belongs to the technical field of thermal power generation, and particularly relates to a feed pump recirculation system for preventing cavitation of a minimum flow valve of a thermal power generating unit. The feed pump recirculation system comprises a condenser, a condensate pump, a low-pressure heat regenerator set, a deaerator, a feed pump and a high-pressure heat regenerator set which are sequentially connected, each stage of extraction steam of an external steam turbine is connected with steam inlets of the high-pressure heat regenerator set, the deaerator and the low-pressure heat regenerator set, and a condensate outlet of the high-pressure heat regenerator set is connected with a condensate inlet of the deaerator. A condensed water outlet of the low-pressure heat regenerator set is connected with a condensed water inlet of the condenser, the water feeding pump sequentially passes through the minimum flow valve, the heat exchanger and the first stop valve and is connected with the deaerator, and external cooling water enters the heat exchanger through the third stop valve for heat exchange and then is discharged. The return water temperature of the feed pump recirculation system is reduced through the heat exchanger, the saturated steam pressure corresponding to the return water is reduced, the cavitation risk of the minimum flow valve is reduced, and the service condition of the minimum flow valve can be obviously improved.

The present invention provides an anti-cavitation condensate pump, an anti-cavitation condensate pump control method and a control system. The anti-cavitation condensate pump includes: a volute; a diameter-adjustable pipe is installed at the water inlet end of the volute; a water pressure sensor is installed at least at the inlet of the diameter-adjustable pipe, the impeller inlet of the volute and the water outlet end of the volute, and is used to obtain water pressure measurement data, wherein the water pressure measurement data is used to generate an adjustment instruction; a driving device, which is connected to the diameter-adjustable pipe and is used to adjust the diameter of the diameter-adjustable pipe according to the adjustment instruction. The anti-cavitation condensate pump, the anti-cavitation condensate pump control method and the control system provided by the present invention obtain water pressure measurement data, that is, the operating conditions of the condensate pump, through the water pressure sensor, obtain an adjustment instruction for various operating condition information, and adjust the diameter of the diameter-adjustable pipe according to the adjustment instruction, so that the condensate pump meets the anti-cavitation performance requirements under the corresponding operating conditions.

The utility model relates to a small-size low-weight condensate pump for a chemical offshore platform, which comprises a pump body provided with a horizontal inlet and a horizontal outlet, a pump cover connected above the pump body, and a pump shaft arranged between the pump body and the pump cover, a driving side bearing body and a non-driving side bearing body are arranged on the two sides of the pump shaft, the driving side bearing body and the non-driving side bearing body adopt a semi-flange plate form, the driving side bearing body adopts a radial bearing of a deep groove ball bearing, and the non-driving side bearing body adopts two thrust bearings which are arranged back to back and have angular contact ball bearing structures. The blades on the two sides of the impeller are arranged in a staggered mode, the main axial force in the operation process of the pump shaft can be balanced, the leakage phenomenon of the sealing face can be effectively prevented, the sealing effect is guaranteed, and the working efficiency of the pump is improved. And the bearing body adopts a semi-flange form, so that the vibration is further reduced, and the stable operation of the pump is ensured.

The utility model belongs to the technical field of dry quenching waste heat power generation, and particularly relates to a dry quenching waste heat power generation deoxygenization water supply system. Comprising EDI (electrodeionization) equipment, a steam extraction condensing steam turbine or a pure condensing steam turbine, a condenser, a condensate pump, a demineralized water tank of a dry quenching boiler water supply pump station, a deoxygenization water supply pump, a deoxygenization water supply regulating valve group, a three-way valve, a water-water heat exchanger, a water supply preheater and a thermal deaerator. The utility model has the beneficial effects that a desalting water tank and a secondary desalting water pump of a desalting water station are omitted; the fixed pressure difference of the regulating valve is used as main regulation, and the three-way valve is used as auxiliary regulation to ensure normal operation of sampling equipment; after deoxygenated water supply is heated by the water-water heat exchanger, one part of sewage is fed into the dry quenching body circulating water tank for normal production, and the other part of sewage is fed back to a sewage discharge well, so that the temperature of the sewage is reduced, heat and water resources are fully utilized, and meanwhile, the adverse effect of white smoke generated by sewage discharge on a drainage system and the environment is eliminated.

The invention belongs to the technical field of energy conservation and emission reduction of sintering circular coolers, and particularly relates to a sintering circular cooler medium-temperature area cross circulation combined waste heat total recovery and zero emission system which comprises a circular cooler, a circular cooling air blower, a waste heat boiler, a circulating fan, a steam turbine generator unit, a condenser and a condensate pump. The waste heat boiler is formed by combining two sets of waste heat boilers, one set of waste heat boiler is a first-section and second-section waste heat boiler, flue gas is taken from a first section and a second section, and exhaust air at the bottom of the first-section and second-section waste heat boiler returns to the first section and the second section through a circulating fan; the other set of waste heat boiler is an overhead three-section waste heat boiler, flue gas of the three-section waste heat boiler is taken from a third section, exhaust air of the three-section waste heat boiler returns to a fourth section, and flue gas of the fourth section returns to the third section; the two waste heat boilers are communicated with a steam supplementing opening of the steam turbine generator unit. The system has the advantages that a new waste heat utilization steam and hot water circulation system is constructed by utilizing the steam supplementing and condensing type steam turbine, and zero emission is realized.

1. Name of the product in this design: Condensate pump with liquid level sensor (for clothes dryer). 2. Purpose of this design: For draining condensate from a clothes dryer. 3. The key design feature of this product is its shape. 4. The image or photograph that best illustrates the design's key points: 3D view 1.

The invention relates to the field of coal electricity, in particular to a steam extraction transformation and heat supply system of a secondary reheat unit. The existing secondary reheating unit cannot meet the requirements of heat consumption and deep peak regulation of a power plant, is difficult to transform and is easy to jump. The invention provides a secondary reheat unit steam extraction transformation and heat supply system which comprises a boiler, a heat supply part, a cylinder part with an ultrahigh pressure cylinder, a high pressure cylinder, an intermediate pressure cylinder and a low pressure cylinder, a steam extraction unit composed of an ultrahigh pressure side and steam part, a high pressure side and steam part and a low pressure side and steam part, and a condensation water and water supply part with a condenser, a condensation pump, a deaerator and an electric pump. The boiler is connected with all the parts through pipelines, when a unit is started and parameters of the ultrahigh pressure cylinder, the high pressure cylinder and the intermediate pressure cylinder are unqualified, steam sent to the pressure cylinders is sent to the heat supply part through the steam extraction unit, and water of the condenser is sent to the boiler through the condensate pump, the deaerator and the electric pump. The steam supply demand change and heat supply of the unit in the deep peak regulation period can be met, stable operation is achieved, and trip is prevented.

The present application relates to a kind of thermal power generating unit control technical field, is a kind of thermal power generating unit condensate pump automatic control system energy-saving optimization method and device, the former includes determining by deaerator water regulating valve control condensate pump outlet header pressure, then judge deaerator water regulating valve whether full open;In response to no, reduce condensate pump outlet header pressure set value, until deaerator water regulating valve full open;In response to yes, judge current deaerator water regulating valve opening degree whether with condensate pump energy-saving operation match;In response to no, increase condensate pump outlet header pressure set value, until current deaerator water regulating valve opening degree with condensate pump energy-saving operation match.The present application is by lifting the opening degree of deaerator water regulating valve, reduce the throttling loss caused by deaerator water regulating valve opening degree low, simultaneously make the throttling loss of deaerator water regulating valve minimum and condensate pump outlet header pressure maximum, in reducing energy loss while guaranteeing the economy of condensate pump operation.

Disclosed is a method of controlling a condensate pump system which comprises a pump and a controller connected to the pump, the method comprising measuring a current value I­m drawn by the pump durin

The invention provides a thermal deoxidization performance experiment system suitable for a negative pressure environment, which belongs to the technical field of thermal waterpower and comprises a condensate tank, a deaerator, a cooling heat exchanger, a cooling water tank, a vacuum tank, a flow measurement system, a pressure measurement system and a temperature measurement system. The condensate tank is connected with the deoxidizing loop, the cooling water tank is connected with the cooling loop, the deaerator is connected with the sampling pipeline, the cooling water tank is connected with the water replenishing pipeline, and the condensate tank is connected with the water draining pipeline; the deoxidizing loop is used for heating and deoxidizing the condensate water in the deoxidizing water tank; the cooling loop cools the heated water to prevent the condensate pump from cavitation; the sampling loop is used for sampling the liquid before and after oxygen removal and measuring the oxygen content of the liquid; the water replenishing loop is used for filling the deoxidizing loop with water before an experiment is carried out; and the drainage loop is used for draining water in the deoxidizing loop after the experiment is finished. The experimental system provided by the invention realizes the functions of negative pressure oxygen removal environment, oxygen content on-line measurement and continuous operation of the system.

The invention belongs to the technical field of nuclear power, and particularly relates to a nuclear power station condensate pump turnover device and method. The nuclear power station condensate pump turnover device can be directly fixed to the ground, an inlet of the condensate pump is connected with a tool, operation can be conducted only through a single travelling crane, the condensate pump is simply and reliably turned over, the industrial safety risk of field operation is reduced to the minimum, the occupied time of a conventional island main travelling crane is shortened, and the working efficiency is improved. The number of workers is reduced, and the whole maintenance period is optimized.

The utility model discloses a waste incineration plant low-pressure heater heat exchange system which comprises a steam turbine, a low-pressure heater and a condenser, the steam turbine is connected with a steam inlet chamber of the condenser through a steam exhaust pipeline, the steam turbine is connected with a steam side inlet of the low-pressure heater through a steam extraction pipeline, and a steam side outlet of the low-pressure heater is connected with the condenser through a drainage pipeline. The condenser is connected with a water side inlet of the low-pressure heater through a first condensation water pipeline, and a condensation water pump is arranged on the first condensation water pipeline. A water side outlet of the low-pressure heater is connected with the deaerator through a second condensation water pipeline, a steam side outlet of the low-pressure heater is connected with the second condensation water pipeline through a drainage recovery pipeline, and a low-pressure heater drainage pump is arranged on the drainage recovery pipeline. The drain water can be prevented from being recycled to the condenser repeatedly, the temperature of the drain water is prevented from being reduced, the working pressure of the condenser is prevented from being influenced, and heat economy is effectively improved.

The system comprises a condenser, a condensate pump, a chemical precision treatment device, a steam seal cooler, a low-pressure heater and a deaerator which are sequentially connected through electric valves, and the condenser is used for condensing steam discharged by a steam turbine to form condensed water; the condensate pump is used for pressurizing the condensate and conveying the condensate into the chemical precision treatment device; the chemical precision treatment device is used for purifying condensed water; the steam seal cooler is used for cooling steam seal steam of the steam turbine; the low-pressure heater is used for heating condensed water; the deaerator is used for removing oxygen in the condensed water; according to the method, whether system energy-saving optimization conditions are met or not is judged by obtaining the vibration value of a condensate pump, the opening degree of a water feeding main adjusting valve of a deaerator and the overall load of the system, and the frequency of the condensate pump is adjusted according to system parameters. Compared with the prior art, the vibration condition of the motor of the condensate pump in the low-load stage is improved, and the problem of high power consumption rate caused by high-frequency operation of the condensate pump under the low load is solved.

The utility model provides a steam condensate water recycling system for a chemical industry park, and belongs to the technical field of steam condensate water recycling. The system comprises a drain valve, a first condensate pump, a condensate pipe network, a condensate water tank, a second condensate pump, a plate heat exchanger and a heat pump system. And through the arrangement that the plate heat exchanger is coupled with the heat pump system, the waste heat of the condensate water is further recovered, and ideal condensate water waste heat recovery is achieved. The system further comprises an iron removal device, an oil removal device and a condensate water recovery system for fine treatment, the condensate water recovery system for fine treatment is connected with the heat pump system in parallel, and the problems that waste heat utilization is not thorough and water and heat utilization requirements change along with seasons can be solved. According to the steam condensate water recycling system for the chemical industry park, the waste heat utilization efficiency is high, condensate water is utilized more thoroughly, and the requirements of users for heat and various different process water can be met.

The present invention relates to the technical field of heat dissipation of energy storage batteries, and discloses a microchannel condenser for heat dissipation of energy storage batteries, comprising a condenser body arranged in an energy storage battery cabinet, wherein the energy storage battery cabinet is further provided with a liquid-cooled battery pack, a plate heat exchanger, a compressor, a condensate pump, and an air pump. A fan is provided on the surface of the condenser body, and the condenser body is sequentially connected to the plate heat exchanger, the compressor, and the condensate pump via working medium circulation pipelines to form a circulation loop. The condenser body comprises: This condenser body solves the problems of gas-liquid two-phase flow distribution, high liquid phase retention, low-temperature liquid hammer, channel blockage, etc. of the microchannel condenser, and significantly improves the heat dissipation efficiency, environmental adaptability, and long-term operation stability of the energy storage battery thermal management system.

Provided in the present invention are a flue-gas-heat-storage-based frequency regulation method and apparatus for a thermal power unit including a low-temperature economizer. The method comprises: in response to a power-grid frequency deviation exceeding a dead zone, starting up a steam-turbine governor system, and on the basis of the steam-turbine governor system and the power-grid frequency deviation, calculating an expected power increment of a thermal power unit, an expected frequency variation of a condensate-water throttling condensate pump, and an expected fan frequency variation of a variable-frequency fan in a flu gas duct; on the basis of the expected frequency variation of the condensate-water throttling condensate pump and the expected fan frequency variation, controlling one or a combination of a flow-regulating valve in a condensate and extraction direction, a flow-regulating valve in a condensate and flue gas direction, and the fan frequency of the variable-frequency fan in the flue gas duct, so as to obtain a power control result; and when the power control result satisfies the requirement of the expected power increment of the thermal power unit, obtaining a frequency regulation result after the completion of frequency regulation. The present invention solves the problems in the prior art of the frequency regulation capability and utilization of flue-gas waste heat being insufficient.

The present invention relates to the field of electric power, and specifically to a thermal peak-shaving system for a new type of thermal power plant complementary to light and coal. The oil pipeline between the oil outlet and the oil inlet of the trough-type heat collecting device is sequentially provided with a hot oil heat storage tank, a high-temperature oil-water heat exchanger, a low-temperature oil-water heat exchanger, a cold oil heat storage tank and an oil transfer pump along the flow direction of the internal heating oil. The condensate main pipe at the bottom of the condenser is provided with a condensate pump. The condensate main pipe at the outlet of the condensate pump is connected to the water side inlet of the high-temperature oil-water heat exchanger through the water inlet pipe of the high-temperature oil-water heat exchanger. The heat is supplemented for the heating extraction steam through an external heat source, breaking the heat user's demand for the heating extraction steam parameters, limiting the problem of variable load operation of the cogeneration unit, thereby enhancing the peak-shaving flexibility of the unit. This system can also adopt different operation modes one and two according to the actual peak-shaving demand of the power grid, thereby realizing a flexible operation mode integrating heating, power generation and peak-shaving.

The utility model provides a back-jacking dismounting device of a condensate pump vertical motor coupling snap ring, the back-jacking dismounting device comprises a back-jacking sleeve, at least one positioning screw, a jacking disc and a jack, the back-jacking sleeve is provided with an accommodating cavity with an opening at one end, and the bottom surface of the accommodating cavity is provided with a first through hole; the jacking disc is arranged on the side, away from the opening of the containing cavity, of the back-jacking sleeve, and a second through hole and a third through hole are formed in the jacking disc; the number of the first through holes and the number of the second through holes are the same as the number of the positioning screw rods, the positioning screw rods sequentially penetrate through the second through holes and the first through holes, the positioning screw rods are sleeved with first fastening pieces, and the first fastening pieces are arranged on the side, away from the back-jacking sleeve, of the jacking disc; the jack penetrates through the third through hole. The back-jacking dismounting device is simple and safe to operate, and equipment cannot be damaged.

The invention relates to the technical field of energy conservation of industrial steam systems, in particular to an exhaust natural convection condensation system of an open type condensation water recovery device. Comprising an air-cooling heat exchanger, a water collecting tank and a condensate pump, the water collecting tank is provided with a saturated condensed water inlet pipeline and a condensed water outlet pipeline; an inlet of the air cooling heat exchanger is communicated with the steam space of the water collecting tank and is used for receiving and condensing flash steam from the water collecting tank; the air cooling heat exchanger is provided with an exhaust port used for exhausting uncondensed gas to the atmosphere. And the condensate pump is connected to a condensate outlet pipeline of the water collecting tank. The advantages of simple structure, low cost, safety and reliability of an open system can be reserved, visual and noise pollution can be effectively eliminated, and the heat energy recovery efficiency is improved.

The utility model discloses a forced circulation evaporation crystallizer, which comprises a feed pump, the circulating separation assembly comprises a heater, an evaporation separator, a circulating pump and a discharging pump; the condensation assembly comprises a condenser, a condensation water tank and a condensation water pump; the solid-liquid separation assembly is used for carrying out solid-liquid separation on the materials discharged by the discharging pump, separated solids are discharged out of the system, one part of mother liquor is discharged out of the system, and the other part of mother liquor is returned to the circulation separation assembly; the negative pressure assembly comprises a vacuum pump. According to the forced circulation evaporation crystallizer, condensate water generated during evaporation and concentration operation is conveyed into the circulation separation assembly and the solid-liquid separation assembly in a branch mode through the condensate water pump, sediment and crystallizers accumulated in a pipeline are washed, cleaning of the interior of the pipeline is achieved, materials are avoided, and stable proceeding of follow-up equipment production is guaranteed.

The present invention provides a self-balancing reheating system for a waste incineration and disposal power station and an operation method thereof. The biogas does not directly enter the furnace for incineration, which will not affect the operation of the waste heat boiler, and avoids the problems of high-temperature corrosion of the reheater in the traditional in-furnace reheating method and the low economy of the out-of-furnace reheating unit. The landfill leachate treatment station is connected to the biogas storage tank; the biogas storage tank is connected to the biogas incineration furnace through a biogas booster fan; the steam outlet of the superheater is connected to the steam inlet of the high-pressure cylinder of the steam turbine; the steam outlet of the high-pressure cylinder of the steam turbine is connected to the low-temperature steam inlet of the low-temperature reheater; the low-temperature reheater is connected to the high-temperature reheater; the steam outlet of the high-temperature reheater is connected to the steam inlet of the intermediate and low-pressure cylinders of the steam turbine; the extraction steam outlet of the high-pressure cylinder of the steam turbine is connected to the extraction steam inlet of the low-temperature reheater; the exhaust steam outlet of the intermediate and low-pressure cylinders of the steam turbine is connected to the exhaust steam inlet of the condenser; the low-temperature reheater is connected to the deaerator; the condenser is connected to the deaerator through a condensate pump; the deaerator is connected to the superheater through a boiler feed pump.

The invention relates to the technical field of sealing water adjustment, and particularly discloses a condensate pump sealing water intelligent adjusting system which comprises at least two sealing water supply branches, an adjustable flow control assembly, a manual flow control assembly and an anti-backflow assembly. The sealing water supply branches are selectively connected into the water inlet end of the adjustable flow control assembly through the anti-backflow assembly, and the water outlet end of the adjustable flow control assembly is connected to the sealing end of the condensate pump through the manual flow control assembly so that the sealing requirements of the condensate pump in different operation stages can be met through the different sealing water supply branches. The adjustable flow control assembly is combined with two-stage adjustment logic to adapt to frequent and great change of unit loads, core adjustment and control components of the sealing water system are prevented from being damaged due to continuous pressure impact, the equipment overhaul frequency and replacement cost are reduced, and the system operation continuity is improved. Compared with a traditional manual gate valve, adjustment hysteresis and randomness are achieved.

The utility model discloses a process water circulating cooling system for treating desulfurization wastewater of a power plant. The process water circulating cooling system mainly comprises a cooling water pump unit and a condensing unit, the cooling water pump unit is composed of two cooling water pump branches which are connected in parallel, and each cooling water pump branch mainly comprises a cooling water pump; the condensation unit is composed of a head end condensate water trunk and a tail end condensate water trunk which are connected in parallel. Each condensate water trunk mainly comprises a condenser, a condensate water tank and a condensate pump which are connected in sequence. The input end of the condenser is connected with the output end of the cooling water pump unit; and the condensed water tank is connected with a condensed gas-liquid separator. As desulfurization process water is adopted, compared with a conventional circulating cooling water system, the circulating cooling water system disclosed by the utility model overcomes the defects of large occupied area, complex system and difficulty in management, and realizes simplification and flexibility of equipment. In addition, a desulfurization wastewater treatment cooling system and a desulfurization process water system are combined for use, so that occupied land and investment are saved, energy consumption is reduced, energy can be saved to the maximum extent, and energy conservation and emission reduction in the industrial production field are facilitated.