WO2019132703A1 - Конденсатная система рекуперации энергосброса атомной электростанции - Google Patents
Конденсатная система рекуперации энергосброса атомной электростанции Download PDFInfo
- Publication number
- WO2019132703A1 WO2019132703A1 PCT/RU2017/001008 RU2017001008W WO2019132703A1 WO 2019132703 A1 WO2019132703 A1 WO 2019132703A1 RU 2017001008 W RU2017001008 W RU 2017001008W WO 2019132703 A1 WO2019132703 A1 WO 2019132703A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- nuclear power
- channel
- condensate
- condenser
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0036—Multiple-effect condensation; Fractional condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0027—Condensation of vapours; Recovering volatile solvents by condensation by direct contact between vapours or gases and the cooling medium
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/041—Treatment of water, waste water, or sewage by heating by distillation or evaporation by means of vapour compression
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
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- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03B—INSTALLATIONS OR METHODS FOR OBTAINING, COLLECTING, OR DISTRIBUTING WATER
- E03B3/00—Methods or installations for obtaining or collecting drinking water or tap water
- E03B3/28—Methods or installations for obtaining or collecting drinking water or tap water from humid air
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- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21D—NUCLEAR POWER PLANT
- G21D1/00—Details of nuclear power plant
- G21D1/02—Arrangements of auxiliary equipment
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- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21D—NUCLEAR POWER PLANT
- G21D1/00—Details of nuclear power plant
- G21D1/04—Pumping arrangements
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/10—Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Definitions
- the invention relates to nuclear energy, and in particular to systems for the recovery of energy savings of nuclear power plants using thermal energy and humidity of the air above the water surface of the discharge channel of a nuclear power plant.
- NPP nuclear power plant
- TPPs thermal power plants
- fuel combustion products coal, natural gas, fuel oil, peat, oil shale is unavoidable
- the only factor in which NPPs are inferior in the environmental plan of thermal power plants is thermal pollution caused by high consumption of waste water used to cool the turbine condensers, which is slightly higher at NPP due to lower efficiency (efficiency; not more than 35%). If the cooling water is taken from a natural reservoir (river, lake or sea), which is economically preferable for NPPs, this leads to an increase in the temperature of the reservoir and damages its biogeocenosis.
- a device for mass production of fresh water by condensation of water vapor from air containing a thermally insulated refrigerating chamber, a pump-compressor for sucking air from the environment into the refrigerating chamber with a branch pipe for releasing from a chamber dehydrated cooled air, electric heaters for melting ice obtained by condensation of water vapor from the air, a container for collecting the formed water with a tap and a pipe for releasing water to the outside, with a pump com the pressor is connected to the coil heat exchanger, which, in turn, is connected to the nozzle, and the refrigerating chamber is connected to the settling chamber, where the electric heaters and the branch pipe with a tap are located to discharge the produced water to the outside.
- the device is designed to obtain water from atmospheric moisture through freezing of water vapor using air compression, cooling and adiabatic expansion. The resulting small ice crystals are periodically melted by an electric heater with the release of water through the faucet.
- the closest analogue of the claimed invention is the atomic-energy complex (RF patent> G ° 2504417, publ. 01/20/2009), designed primarily to produce fresh water by condensation of water vapor from atmospheric air, including a means for air intake, a compressor connected to a heat exchanger a device for cooling compressed air, a turbo-expander, means for transporting water and air with fittings, a nuclear power plant, with the means for taking air in the form of a tower height not less than 200 m from the intake windows placed at a height of the tower, a heat exchanger for cooling the compressed air is a capacitor which is connected with a drip catcher, both of which are arranged to discharge condensate in primary condensate pool and a turboexpander coupled to the water a chamber equipped with an irrigator connected to the secondary condensate basin and circulating water heat exchanger, which is connected to the nuclear power plant.
- RF patent> G ° 2504417, publ. 01/20/2009 designed primarily to produce fresh water by condensation
- water vapor from the atmospheric air passes through the air intake facility and the compressor, then undergoes the first stage of condensation when cooled in a condenser, which allows to obtain a primary condensate that corresponds to rain water in its environmental qualities. Then, in the second stage of condensation, the compressed air passes through a turboexpander, where it performs work due to a sharp adiabatic expansion with a drop in temperature, as a result of which the moisture contained in it is frozen / condensed to produce secondary condensate corresponding to the qualities of natural thaw / rainwater.
- the atomic energy complex according to the RF patent JN ° 2504417 ensures the production of freshwater ecologically clean condensate from atmospheric moisture seas in large volumes.
- Its disadvantages are (1) insufficient productivity of the process of obtaining fresh water while locating the atomic-energy complex far from the sea coast and the dependence of the productivity of the process of obtaining fresh water on the daily and seasonal changes in ambient temperature, and (2) the overall coefficient is not high enough the use of heat from nuclear power plants and (3) the impossibility of reducing the negative impact of thermal emissions of waste water from nuclear power plants on the environment.
- the present invention is to develop a condensate drainage system of a nuclear power plant, which provides: (1) high performance of the process of obtaining fresh water in any conditions due to the recovery of thermal energy of the water from the NPP exhaust channel by disposing of its high-temperature wet steam, use of heat from nuclear power plants and (3) reducing the negative impact of heat from waste water on the environment.
- the technical result of the present invention is: (1) ensuring high productivity of the process of obtaining fresh water in any conditions due to the recovery of thermal energy of the water from the discharge channel of a nuclear power plant by disposing of its moist high-temperature steam, and (2) increasing the overall coefficient use of heat from nuclear power plants and (3) reducing the negative impact of waste water on the environment.
- the condensate system with a droplet separator and a primary condensate pool, while the condenser is connected to a pressure pipe with a droplet separator connected to the turbo-expander and primary condensate pool connected to a water chamber sprinkler and a clean water pumping station.
- the irrigator water chamber pressure pipe It is preferable to connect the irrigator water chamber pressure pipe with a pool of secondary condensate. It is reasonable to place the parts of the air ducts located in the waste water channel above the surface of the waste water and provide them with canals made with the possibility of collecting condensate and connected to pipelines for draining condensate outside the waste water channel.
- the advantages of the present invention are: ensuring high productivity of the process of obtaining fresh water in any conditions due to the recovery of thermal energy of water from the NPP exhaust channel by disposing of its moist high-temperature steam, increasing the overall heat utilization factor of nuclear power plants and reducing the negative impact of waste water on the environment.
- FIG. 1 shows a diagram of a preferred variant of a condensate recovery system for an NPP energy saving system
- a nuclear power plant 1 to which the waste water channel 2 is connected, bubbling pipes 3, connected to the water chamber 13 by means of a cold air duct, are placed below the waste water channel 2 the discharge channel is connected by a pressure air duct to a compressor 4, which is connected to a condenser 5 connected to a cooling water pumping station 6, a droplet separator 8 and a pool primary condensate 7, the droplet separator 8 is connected to the pool of primary condensate 7 and the turbine expander 9 connected to the electric generator 10 and the water chamber 13.
- the water chamber 13 containing the irrigator 14 is connected to the nuclear power plant 1 with a bubbling compressor 15 and pressurized pipelines - the primary condensate basin 7 and the secondary condensate basin 12, which is connected to the clean water pumping station 11, also connected to the primary condensate basin 7, all connections are made by means of molecular weight pipelines.
- FIG. 2 shows embodiments of channel 2 of waste water and placement of duct pipes and bubbling pipes 3 in it.
- Condensate recovery system of energy saving NPP works as follows.
- cooling water from an external reservoir is used to condense steam leaving the turbine of a nuclear power plant.
- the cooling water passes through the tube bundle of the condenser of a nuclear power plant 1, the cooling water is heated by 5-10 ° C to a temperature of approximately 35 ° C, then through channel 2 of the waste water, in which bubbling pipes 3 are installed, is discharged back into the sea, river, reservoir or other external reservoir.
- the bubbling tubes 3 which can be taken from the environment, and in the preferred embodiment of the invention, cold, dehydrated air from the water chamber 13 is supplied through the duct through the bubbling compressor 15 and thereby has a lower temperature and humidity (relative humidity about 20%, air temperature from -4 ° C to + 8 ° C), than the waste water.
- Bubble pipes 3 can be made in various versions, for example, in the form of perforated pipes.
- the waste water with a reduced temperature returns through the discharge channel 2 to the sea or another external reservoir, and the wet evaporation through the discharge air duct, whose entrance is located in the air part of the discharge channel 2, enters the compressor 4, where due to adiabatic increase the pressure is additionally heated to a temperature above 100 ° C, after which it flows through the pressure air duct into the condenser 5.
- the heated evaporator under pressure contacts through the walls of the heat exchange tubes / plates with reverse water heating systems of the NPP and any nearby buildings, or with cold bottom water a nearby reservoir, or with water taken from the sections of the discharge channel preceding the bubbling tubes 3, using a seawater pumping station 6.
- the temperature of the steam drops to 10- 18 ° C, i.e. below the dew point of the source air, which leads to a partial deposition of moisture on the surfaces of the condenser 5, which is then discharged into the basin of the primary condensate 7 and represents fresh water, which is appropriate in its qualities of rainwater.
- This process corresponds to the first, condensation stage of obtaining fresh water with the purification of its salts and impurities.
- the remaining wet steam under pressure enters through the pressure air duct into the droplet separator 8, which can be performed, for example, as a slit-type droplet separator, in which further precipitation and purification of salt-containing impurities occurs, which then enters the primary condensate basin 7 and also represents is fresh water, suitable for its quality rainwater.
- the droplet separator 8 can be performed, for example, as a slit-type droplet separator, in which further precipitation and purification of salt-containing impurities occurs, which then enters the primary condensate basin 7 and also represents is fresh water, suitable for its quality rainwater.
- the primary condensate obtained at the first stage of freshwater production can be used for agricultural irrigation, for technical needs, and, in a preferred embodiment of the invention, in the operation of the condensate recovery system of NPP energy recovery itself, as will be shown below.
- the wet vapor from the condenser 5 that remains after separation of the primary condensate enters the turbo expander 9 through the pressure pipe, in which it is adiabatically expanded with a decrease in pressure and temperature while the turbine expander 9 is working on the turbine, and the energy released is converted into electricity using an electric generator current 10, which also provides partial recovery of the energy expended by the compressor 4 on the primary compression of the vapor.
- the sharp adiabatic expansion of the wet vapor in the expander 9 causes the vapor to cool to about -10 ° C and freeze the moisture remaining in the wet vapor to this point, which is the second cryogenic vapor condensation step. Frozen moisture containing air and particles of snow and ice enters the water chamber 13.
- the frozen moisture undergoes the process of irrigation with warm fresh water, which can be fed into the sprinkler 14 via a pressure pipe from condenser 5, and in a preferred embodiment of the invention it is fed to the sprinkler 14 via pressure pipe from the primary condensate pool 7 or from secondary condenser 12, which allows partial heat recovery of waste water from nuclear power plants.
- pressure pipe from the primary condensate pool 7 or from secondary condenser 12, which allows partial heat recovery of waste water from nuclear power plants.
- melting occurs. mixtures of air, snow and ice, decomposing it into secondary condensate, suitable for rainwater in its qualities, and cooled dehydrated air, suitable for conditioning the premises of the NPP and any nearby buildings, for which purpose are used pressure air ducts connected to the water chamber 13.
- the present invention is a connection through the duct of the water chamber 13 with bubbling pipes 3, which, as shown above, allows to increase due to the larger area of evaporation n bubbling with bubbles water channel 2 the waste water and thus ensure the achievement of the technical result of the present invention, i.e. to ensure high productivity of the process of obtaining fresh water in any conditions due to the recovery of heat energy from the NPP exhaust channel, reduce the negative impact of waste water on the environment and increase the overall heat utilization factor of nuclear power plants.
- high-purity secondary condensate is supplied through a pipeline to the secondary condensate basin 12, after which it can be used as process water, for irrigation of territories adjacent to NPPs, as well as in water supply systems of settlements.
- the seawater pumping station can be connected to the discharge pipe 2 with the discharge water channel 2 below the bubbling tubes 3, and the compressor above the bubbling tubes 3. This allows additional heat exchange between the condenser 5 and the discharge water channel 2, which further reduces the temperature of the waste water .
- the waste water channel 2 can be divided into sections of 100 m length each with lattice partitions that do not interfere with the movement of water, but divide the air space of the canal sections.
- a wet vapor is collected from each section; wet vapor can be fed to separate condensate stations, each of which contains blocks 4–15 of the present invention.
- the volume of waste water of each section of channel 2 is supplied by means of bubbling air with a flow rate of 1000 m / s from the outlet of the condensate station (relative humidity 20%, air temperature from 4 ° C to + 8 ° C).
- the air passing in the form of bubbles in the water column of the discharge channel, takes the water temperature (+ 35 ° C), while the moisture content of the vapor reaches a value of 32.3 g / kg or ⁇ 9g / m 3 (air).
- productivity (in fresh water) of one condensate system will be more than 3 thousand tons / day.
- the preferred option for energy recovery recovery will reduce the temperature of waste water by more than 3 ° C.
- the condensate recovery system of the energy saving of a nuclear power plant can significantly improve the productivity of the process of obtaining fresh water due to the recovery of thermal energy of waste water from nuclear power plants, reduce the negative impact of waste water on the environment and increase the overall heat utilization factor of nuclear power plants.
Abstract
Description
Claims
Priority Applications (12)
Application Number | Priority Date | Filing Date | Title |
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CN201780098076.4A CN112135675A (zh) | 2017-12-29 | 2017-12-29 | 用于回收核电站的排放能量的冷凝系统 |
EP17936024.3A EP3733255B1 (en) | 2017-12-29 | 2017-12-29 | Condensation system for recuperating energy discharge of nuclear power plant |
BR112020013368-0A BR112020013368B1 (pt) | 2017-12-29 | Sistema de condensado para recuperar energia de uma usina de potência nuclear | |
EA202091562A EA202091562A1 (ru) | 2017-12-29 | 2017-12-29 | Конденсатная система рекуперации энергосброса атомной электростанции |
PCT/RU2017/001008 WO2019132703A1 (ru) | 2017-12-29 | 2017-12-29 | Конденсатная система рекуперации энергосброса атомной электростанции |
US16/959,091 US20200335235A1 (en) | 2017-12-29 | 2017-12-29 | Condensate System for Recuperating Energy from a Nuclear Power Plant |
KR1020207021670A KR102545027B1 (ko) | 2017-12-29 | 2017-12-29 | 원자력 발전소의 폐열 회수를 위한 응축식 회수 시스템 |
RU2019128158A RU2737376C1 (ru) | 2017-12-29 | 2017-12-29 | Конденсатная система рекуперации энергосброса атомной электростанции |
JP2020536123A JP7188795B2 (ja) | 2017-12-29 | 2017-12-29 | 原子力発電所のエネルギーを回収する復水システム |
JOP/2020/0163A JOP20200163A1 (ar) | 2017-12-29 | 2017-12-29 | نظام تكثيف لاسترجاع الطاقة المنصرفة من محطة طاقة نووية |
CA3107479A CA3107479C (en) | 2017-12-29 | 2017-12-29 | Condensate system for recuperating energy from a nuclear power plant |
FIEP17936024.3T FI3733255T3 (fi) | 2017-12-29 | 2017-12-29 | Lauhdutusjärjestelmä ydinvoimalan energiapäästön talteenottoa varten |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/RU2017/001008 WO2019132703A1 (ru) | 2017-12-29 | 2017-12-29 | Конденсатная система рекуперации энергосброса атомной электростанции |
Publications (1)
Publication Number | Publication Date |
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WO2019132703A1 true WO2019132703A1 (ru) | 2019-07-04 |
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Family Applications (1)
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PCT/RU2017/001008 WO2019132703A1 (ru) | 2017-12-29 | 2017-12-29 | Конденсатная система рекуперации энергосброса атомной электростанции |
Country Status (11)
Country | Link |
---|---|
US (1) | US20200335235A1 (ru) |
EP (1) | EP3733255B1 (ru) |
JP (1) | JP7188795B2 (ru) |
KR (1) | KR102545027B1 (ru) |
CN (1) | CN112135675A (ru) |
CA (1) | CA3107479C (ru) |
EA (1) | EA202091562A1 (ru) |
FI (1) | FI3733255T3 (ru) |
JO (1) | JOP20200163A1 (ru) |
RU (1) | RU2737376C1 (ru) |
WO (1) | WO2019132703A1 (ru) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN113035386B (zh) * | 2021-03-05 | 2022-11-18 | 哈尔滨工程大学 | 一种采用双轮双叶复合动力吸气式的安全壳内置高效换热器 |
CN114941863A (zh) * | 2022-05-12 | 2022-08-26 | 华能(大连)热电有限责任公司 | 一种热网疏水分级回收装置及其回收方法 |
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2017
- 2017-12-29 WO PCT/RU2017/001008 patent/WO2019132703A1/ru active Application Filing
- 2017-12-29 KR KR1020207021670A patent/KR102545027B1/ko active IP Right Grant
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- 2017-12-29 EA EA202091562A patent/EA202091562A1/ru unknown
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- 2017-12-29 FI FIEP17936024.3T patent/FI3733255T3/fi active
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Patent Citations (4)
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US6829319B2 (en) * | 1999-11-22 | 2004-12-07 | Organo Corporation | Condensate demineralization |
RU122199U1 (ru) * | 2012-06-04 | 2012-11-20 | Открытое акционерное общество "Российский концерн по производству электрической и тепловой энергии на атомных станциях" (ОАО "Концерн Росэнергоатом") | Водосброс атомной электростанции |
RU2504417C1 (ru) | 2012-09-19 | 2014-01-20 | Открытое акционерное общество "Восточно-Европейский головной научно- исследовательский и проектный институт энергетических технологий" (ОАО "Головной институт "ВНИПИЭТ") | Атомно-энергетический комплекс |
US20160141056A1 (en) * | 2014-01-22 | 2016-05-19 | Willard Harvey Wattenburg | Passive Nuclear Reactor Emergency Cooling System Using Compressed Gas Energy and Coolant Storage Outside Nuclear Plant |
Also Published As
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EP3733255B1 (en) | 2023-11-22 |
JP7188795B2 (ja) | 2022-12-13 |
EP3733255A1 (en) | 2020-11-04 |
EA202091562A1 (ru) | 2021-04-08 |
JP2021516331A (ja) | 2021-07-01 |
EP3733255A4 (en) | 2021-04-28 |
KR102545027B1 (ko) | 2023-06-20 |
KR20200102482A (ko) | 2020-08-31 |
CA3107479C (en) | 2023-07-04 |
FI3733255T3 (fi) | 2024-02-15 |
JOP20200163A1 (ar) | 2020-06-29 |
US20200335235A1 (en) | 2020-10-22 |
CN112135675A (zh) | 2020-12-25 |
RU2737376C1 (ru) | 2020-11-27 |
BR112020013368A2 (pt) | 2020-12-01 |
CA3107479A1 (en) | 2019-07-04 |
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