Condensate System for Recuperating Energy from a Nuclear Power Plant

Abstract

A condensation system for recuperating the energy discharge of a nuclear power plant comprises a nuclear power unit, an air intake means, a compressor, a condenser, a water chamber equipped with a sprinkler, an electrical current generator, a pure water pump station, a cooling water pump station, a secondary condensate pool and a turboexpander. The air intake structure is connected to a compressor, which is connected to the condenser, which is connected to the turboexpander, which is supplied with the electric current generator and is connected to the water chamber, which is connected to the secondary condensate pool, which is connected to the pure water pump station, the condenser being connected to the cooling water pump station, wherein the air intake structure is accommodated in the discharge water channel, which is connected to the nuclear power unit and is equipped with a sealing cover.

Claims

1. A condensational recuperation system for the energy output of a nuclear power station, comprising a nuclear power plant, an air intake means, a compressor, a condenser, a water chamber provided with a sprinkler, an electric current generator, a pure water pump station, a cooling water pump station, a secondary condensate pool, and a turbo expander, the air intake means being connected to a compressor connected to a condenser connected to the turbo expander provided with an electric current generator and connected to a water chamber connected to the secondary condensate pool, the secondary condensate pool being connected to a pump station of pure water, the condenser being connected to a pump station of cooling water, all of the connections being made in the form of pressure pipelines, characterized in that the air intake means is arranged in the wastewater channel of a nuclear power plant connected to the nuclear power plant, and the wastewater channel is provided with a sealed roof

2. The system according to claim 1, characterized in that the wastewater channel is provided with bubbling tubes arranged below the surface of the wastewater and connected by means of air ducts to the water chamber.

3. The system according to claim 1, wherein the wastewater channel has an effective total area of not less than 2000 m.sup.2 per 100 m of its length.

4. The system according to claim 1, characterized in that it is further provided with a droplet separator and a primary condensate pool, the condenser is connected by a pressure pipeline to the droplet separator, which is connected to a turbo expander, and a primary condensate pool is connected to a water chamber sprinkler and a clean water pump station.

5. The system according to claim 2, characterized in that a bubbling compressor is installed in the air duct connecting the water chamber with the bubbling tubes.

6. The system according to claim 2, characterized in that the pump station of the cooling water is connected by a pressure pipeline to the channel of the wastewater below the bubbling pipes, the compressor is connected by a pressure pipeline to the channel of the wastewater above the bubbling pipes.

7. The system according to claim 4, wherein the cooling water pump station and the condenser are connected to an external heat system.

8. The system according to claim 1, wherein the sprinkler of the water chamber is connected to a secondary condensate pool by means of a pressure pipeline.

9. The system according to claim 2, characterized in that the parts of the air ducts located in the channel of the wastewater are located above the surface of the wastewater and are provided with water ducts provided with the possibility of collecting condensate and connected to the pipelines for discharge of the condensate outside the channel of the wastewater.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0022] In FIG. 1 is shown a schematic diagram of a preferred embodiment of a waste heat recuperation system of a NPP including a nuclear power plant 1 to which a discharge channel of wastewater 2 is connected, in the wastewater channel 2 below the water level are arranged bubbling tubes 3 connected to a water chamber 13 by means of a cold air duct, the air part of the discharge channel is connected by a pressure air duct to a compressor 4, which is connected to a condenser 5 connected to the pump station of the cooling water 6, the droplet separator 8 and the pool of a primary condensate 7, the droplet separator 8 is connected to the pool of the primary condensate 7 and a turbo expander 9 connected to the electric generator 10 and the water chamber 13. The water chamber 13, containing the sprinkler 14, is connected by an air duct to the nuclear power plant 1, with the bubbling compressor 15 and the pressure pipelineswith the pool of the primary condensate 7 and the pool of the secondary condensate 12 which is connected to the pump station of pure water 11, which is also connected to the pool of the primary condensate 7, wherein all of the connections are made by pressure pipelines.

[0023] FIG. 2 shows embodiments of the design of the channel 2 of wastewater and the placement of air ducts and bubbling pipes 3 therein. When the pipes are partially placed below the surface of the wastewater, the wastewater is further cooled by the cold air flowing through the air duct, and when placed above the surface of the water, it is possible to place below the air ducts grooves which are made with the possibility of collecting condensate and transferring it through pipelines outside to the consumer, which improves the productivity of the system.

[0024] The condensate system of the recuperation of the waste energy of NPP preferably is operated as follows. When the nuclear power plant 1 is operated to condense the steam leaving the turbine of the nuclear power plant, cooling water from an external water reservoir is used. In the heat exchange process the cooling water, on passing through the tube bundle of the condenser of the nuclear power plant 1, is heated by 5 to 10 C. to a temperature of approximately 35 C., whereupon it is, via the wastewater channel 2, in which the bubbling pipes 3 are mounted, discharged back to the sea, river, water reservoir or other external waters. To increase the evaporation area, to the bubbling pipes 3 air is supplied, which can be taken from the environment, but in the preferred embodiment of the invention through air ducts the cold dehydrated air is supplied from the water chamber 13 by means of the bubbling compressor 15, and because of this it has a lower temperature and humidity (relative humidity about 20%, air temperature of 4 C. to +8 C.) than the wastewater. Due to this air bubbles leaving the bubbling pipes 3 and on passing through the volume of the wastewater take the water temperature of the discharge channel and get saturated with moisture (the moisture content of the vapor in the bubbles reaches 32.3 g/kg or 39 g/m.sup.3 of air), and after the bubbles escape to the surface of the water in the discharge channel 2, they form a moist steam (warm air saturated with water vapor). The bubbling tubes 3 may be made in various versions, for example, in the form of perforated tubes.

[0025] After passing along the bubbling pipes 3, the low-temperature wastewater is returned via the discharge channel 2 to the sea or other external waters, whereas the moist steam is supplied to the compressor 4 via the pressure air duct, the inlet of which is placed in the air part of the discharge channel 2, and is supplied to the compressor 4, where it is further heated to a temperature above 100 C. due to the adiabatic pressure increase, after which it enters the condenser 5 through the pressure air duct. In condenser 5, heated vapor under pressure is contacted through the walls of heat-exchange tubes/plates with returned water of the thermal net of the NPP and any nearby buildings, or with cold natural water of a nearby water reservoir, or with water taken from the sections of the discharge channel upstream the bubbling pipes 3, by means of the pumping station of sea water 6. Due to the difference in the temperatures of the vapor and the seawater on the heat-exchange tubes/plates of the condenser 5, the temperature of the vapor is reduced to temperatures of 10 to 18 C., i.e. below the dew point of the source air, which results in partial deposition on the surfaces of the condenser 5 of moisture, which is then discharged into the pool of the primary condensate 7 and represents a freshwater corresponding in quality to rain water. This process corresponds to the first, the condensation stage of producing freshwater with purification from its salts and impurities. After that, the remaining moist steam under pressure is supplied via the pressure air duct to the droplet separator 8, which may be made, for example, in the form of a slotted-type droplet separator, in which further settling and purification from salt-containing impurities of moisture is carried out, which is then supplied to the pool of the primary condensate 7 and also represents freshwater corresponding to the quality of rain water.

[0026] The primary condensate obtained in the first stage of producing freshwater can be used for agricultural irrigation, for technical purposes, as well as, in the preferred embodiment of the invention, in the operation of the condensate system of the recuperation of the power emission of the NPP itself, as will be shown below.

[0027] The moist steam remaining after the separation of the primary condensate from the condenser 5 under pressure via the pressure line enters the turbo expander 9 in which it is subjected to an adiabatic expansion with pressure and temperature reduction in the operation of the turbine of the turbo expander 9, whereby the extracted energy is converted into electrical energy by means of an electric current generator 10, which also provides partial recuperation of the energy supplied to compressor 4 for the primary compression of steam. The abrupt adiabatic expansion of the wet vapor in the turbo expander 9 results in the cooling of the vapor to about 10 C. and in the freezing of the moisture, remaining in the wet steam up to this moment, which is the second, cryogenic vapor condensing stage. Frozen moisture containing air and particles of snow and ice enters water chamber 13.

[0028] In the sprinkler 14 of the water chamber 13 the frozen-out moisture undergoes the process of sprinkling with warm freshwater, which can be fed to the sprinkler 14 via the pressure pipeline from the condenser 5, but in the preferred embodiment of the invention is fed to the sprinkler 14 via the pressure pipeline from the pool of the primary condensate 7, or from the pool of the secondary condenser 12, which makes it possible to perform a partial recuperation of the heat of the wastewater of the NPP. As a result of sprinkling, the mixture of air, snow and ice is melted and decomposed into the secondary condensate, which in its quality corresponds to rain water, and in cooled dehydrated air suitable for conditioning of the rooms of the NPP and any nearby buildings, for which purpose pressure ducts connected to the water chamber 13 are used. An important essential feature of the present invention is the connection by means of an air duct of the water chamber 13 with the bubbling tubes 3, which, as shown above, makes it possible due to the high area of evaporation to increase the heat exchange between the pneumatic bubbles with the water of the wastewater channel 2 and thereby to ensure the achievement of the technical result of the present invention, i.e. to ensure a high efficiency of the process of producing freshwater under any conditions due to a recuperation of thermal energy of the discharge channel of the NPP, to reduce the negative effect of the wastewater on the environment and to increase the overall coefficient of performance of the heat of the NPP. In this, the high-purity secondary condensate is fed via a line to the pool of the secondary condensate 12, whereupon it is possible to use it as technical water, for the irrigation of territories surrounding the NPP, as well as in water supply systems of populated places.

[0029] In the case of a utilization of the system for NPP/TPPs having an energy output of less than 1000 MW a utilization of the recuperation system of the energy output without the use of the drop separator 8 becomes advantageous. In this utilization mode the moist steam downstream of the compressor 5 is fed directly to the turbo expander 9, from which it is sent to the water chamber 13, where it is condensed in the second stage by the method disclosed above.

[0030] For additional moisture and steam temperature is it possible to use passive floating impellers installed in channel 2 of wastewater with a possibility of forming a developed relief of the water surface. In this case, the surface area of the evaporation increases, which increases the humidity and the temperature of the vapor. In this case, in the case of an important (greater than 300 m) length of the channel 2 of wastewater, it is possible to separately apply the bubbling pipes 3 and the floating impellers at various sections of the wastewater channel 2 with a discharge of steam from each section according to the present invention.

[0031] In an embodiment of the invention, the sea water pump station can be connected via a pressure line to the channel 2 of the wastewater below the bubbling pipes 3, but the compressorabove the bubbling pipes 3. This makes it possible to carry out an additional heat exchange between the condenser 5 and the wastewater channel 2, which further reduces the temperature of the wastewater.

[0032] Furthermore, according to still another embodiment of the invention, it is possible to connect the condenser 4 and the pump station of the cooling water 6 to an external heat system, for example an urban heating system. In this case, a condensation of steam on condenser 4 will occur with heating of water for the city heating system, which further increases general heat utilization factor of the NPP.

[0033] Calculations show a high application efficiency of the present invention. At the estimated dimensions (FIG. 2) of the channel 2 of the wastewater: width10 m, height6 m, length800 m and depth of the water in the channel3 m the flow of water in the channel 2 of the wastewater is 66 t/s. The perforated underwater bubbling pipes (100 pipes, each in the section 0.07 m.sup.2) are located at the bottom (across the axis) of the discharge channel at a distance of 1 m and more from each other, connecting the main pipes and providing the process of air discharge uniformly in a volume of 400 m.sup.3/sec and more. In a preferred embodiment, the channel 2 of the wastewater can be divided into sections of 100 m in length by partitioning grids, which do not interfere with the movement of the water but divide the air space of the channel into sections. Moist steam is then taken from each section, and the moisture vapor can be supplied to separate condensate stations, each of which is comprises blocks 4-15 of the present invention. To the volume of the discharge water of each section of the channel 2 by bubbling at a rate of 1000 m/s air is charged from the outlet of the condenser station (relative humidity 20%, air temperature from 4 C. to +8 C.). Air passing as bubbles through the depth of the water of the discharge channel assumes the temperature of the water (+35 C.), while the moisture content of the vapor reaches a value of 32.3 g/kg or 39 g/m3 (air). The productivity (in freshwater) of one condensate system is more than 3 thousand tons/day. In the case of a discharge channel with 6 condensate stations of the preferred embodiment of the recuperation of the energy output, a temperature drop of the wastewater of more than 3 C. is reached.

INDUSTRIAL APPLICABILITY

[0034] The condensate system of the recuperation of the power discharge of the nuclear power plant makes it possible to substantially increase the efficiency of the process of producing freshwater by recovering the thermal energy of the wastewater of the NPP, to reduce the negative effect of the wastewater on the environment and to increase the overall coefficient of utilization of the heat of the NPP.