CN212609683U - Generator inner cooling water treatment facilities based on divide bed EDI - Google Patents
Generator inner cooling water treatment facilities based on divide bed EDI Download PDFInfo
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Abstract
The utility model relates to a cold water treatment facilities in generator based on divide bed EDI, it belongs to generator technical field. The utility model discloses the device includes a plurality of needle valves, cooler, interior cold water storage cistern, sodium type/ammonium type cation bed, resin trapper, electrical control valve one, electrical control valve two, electromagnetic flowmeter one, electromagnetic flowmeter two, electric conductivity table, hydrogen electric conductivity table, degasification hydrogen electric conductivity table, minute bed EDI and programmable controller to minute bed EDI and sodium type/ammonia type cation bed carry out bypass treatment to internal cold water, detach the CO in the interior cold water2And Cu2+Decrease ofCopper corrosion products and CO2The accumulation in the inner cold water reduces the CO in the inner cold water2And the concentration, namely the pH value of the internal cooling water is maintained to be more than 8.0, the copper corrosion of the generator is controlled in a qualified range, and meanwhile, the copper corrosion product is prevented from being deposited in a copper wire rod, so that the safe operation of the generator is ensured. The utility model has the characteristics of the system is simple, stable in water quality, no blowdown etc, can realize automatic operation.
Description
Technical Field
The utility model relates to a device especially relates to a cold water treatment facilities in generator based on bedded EDI, and it belongs to generator technical field.
Background
The cooling water of the rotor or the stator of the large and medium-sized generator is usually high-purity water, air inevitably leaks into the generator when the cold water in the generator circulates, and CO in the air is continuously circulated along with the cold water in the generator2The internal cooling water is continuously accumulated, the pH value of the internal cooling water is gradually reduced, and the corrosion of the copper coil of the generator is accelerated. Copper coil corrosion increases the copper content of internal cooling water, copper corrosion products can be deposited in the hollow copper coil, cooling water flow is reduced, and even the coil is burnt out due to overheating. Meanwhile, the electric conductivity of the inner cooling water influences the grounding resistance of the generator, so that the pH and the electric conductivity of the inner cooling water must be controlled within a proper range to prevent the corrosion of the hollow copper coil and ensure the reliable insulating property of the generator. Research shows that the conductivity of the inner cooling water is controlled to be less than 2 mu S/cm (cooling water) or 5 mu S/cm (cooling water), the pH value is controlled to be more than 8.0, the insulation performance of the generator can be ensured, and the corrosion of the hollow copper coil is minimized.
At present, the domestic mainstream treatment process of cold water in a generator belongs to an oxygen-enriched working condition, and mainly aims at adjusting pH.
According to the pH adjusting mode, the cold water treatment in the generator can be divided into 3 types: the alkali adding type is directly, the sodium type mixed bed is adopted for indirectly adding the alkali, and the adjusting type is adopted for the condensed water containing ammonia and the desalted water.
Directly adding alkali, performing bypass treatment on the internal cooling water by using an RH/ROH type small mixed bed to remove anions and cations in the internal cooling water, then independently adding an alkalizer to maintain the pH value of the internal cooling water at 8.0-9.0, and controlling the conductivity of the internal cooling water within a qualified range by adjusting the bypass treatment amount of the internal cooling water. However, the method is limited by the bypass treatment capacity, and the conductivity and the pH value cannot be simultaneously considered, so that the quality of cold water in the generator often exceeds the standard; and the alkalizer is directly added, the buffering capacity of the system is weak, and the risk of standard exceeding of the conductivity exists.
The sodium type mixed bed is adopted for indirect alkali addition, and the cold water is subjected to bypass treatment by using an RNA/ROH type small mixed bed, wherein the principle is that Cu corroded from the cold water is treated2+Or exchange of other cations with sodium cation resin to produce Na+The anion exchanges with OH type anion resin to generate OH-Finally, trace NaOH is generated in the effluent of the mixed bed, so that the pH value of the internal cooling water is increased. However, the corrosion product of the generator copper bar is mainly oxide and can not exchange with the cation in the mixed bed to generate Na+Therefore, it is difficult to adjust the pH of the internal cooling water to a desired value, and the results of field application show that the pH is 8.0 or less, and the desired corrosion control effect cannot be achieved.
The method adopts an ammonia-containing condensate and demineralized water regulation mode, mixes the ammonia-containing condensate and the demineralized water in a certain proportion to be used as the make-up water of the inner cooling water tank, and reduces CO by continuously changing water in large flow2Accumulation in the cold water, thus CO in the cold water2The concentration can be controlled at a lower level, so that the pH value of the inner cooling water is controlled to be 8.0-8.5. In addition, by adjusting the proportion of the condensed water and the desalted water, the conductivity of the inner cooling water can be controlled within a required range. However, in some units, the thermodynamic system has less water supplement amount, the water change flow rate is limited, the pH adjusting capacity of the unit is limited, and particularly, the cold water in a generator rotor is more obvious, so that the modeThere are also limitations.
At present, the control index of cold water in a generator mainly takes the conductivity and the pH value as main indexes, and the adjustment is carried out by measuring the pH value and the conductivity. However, pure water pH measurement is easily affected by static charge and the like, and measurement accuracy cannot be guaranteed, which is a worldwide problem recognized at present. The above-mentioned several internal cooling water treatment modes all rely on pH monitoring result to regulate and control alkali addition quantity and bypass treatment quantity, and because pH measurement is inaccurate and unreliable, it is difficult to regulate and control internal cooling water treatment to the desired target.
In summary, the conventional methods for treating the internal cooling water in the main stream generator all have certain problems, and the conductivity and the pH of the internal cooling water cannot be controlled at desired values simultaneously and stably for a long time, so that a simple and reliable treatment device is urgently needed.
The key of the cold water treatment in the generator is to control CO in the cold water2The content and the realization way are two, namely, reducing CO2Second, measures are taken to remove CO in the cold water2. But with reduction of CO2The leak-in is easy to do but cannot be completely avoided, so the emphasis is on removing CO2. The best treatment mode is that CO in the cold water can be removed2But also can retain the alkalizer in the inner cold water. Thus, the CO in the inner cold water can be discharged without pollution discharge2The concentration is controlled at a lower level so that the pH and conductivity of the cold water are simultaneously within the desired control range.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome the above-mentioned not enough that exists among the prior art, and provide a structural design reasonable, safe and reliable, the measuring result accuracy is high, and adaptability is good, and is with low costs, long-term stable with the generator in the generator cold water conductivity and pH simultaneous control in expectation range based on cold water treatment facilities in the generator of separating bed EDI.
The utility model provides a technical scheme that above-mentioned problem adopted is: this send out motor inner cooling water treatment facilities based on divide bed EDI, including a plurality of needle valves, cooler and interior cold water tank, this a plurality of needle valves include needle valve one, needle valve two, needle valve three, needle valve four, needle valve five, needle valve six, its characterized in that: the system also comprises a sodium/ammonium cation bed, a resin catcher, a first electric regulating valve, a second electric regulating valve, a first electromagnetic flowmeter, a second electromagnetic flowmeter, a conductivity meter, a hydrogen conductivity meter, a degassing hydrogen conductivity meter, a separate bed EDI and a programmable controller; the needle valve I, the electric regulating valve I and the electromagnetic flowmeter I are arranged on a pipeline connecting the inlet of the sodium/ammonium anode bed with the water outlet pipeline of the cooler; the needle valve II, the needle valve III and the resin catcher are arranged at the outlet of the sodium/ammonium cation bed; the outlet of the resin catcher is respectively provided with a needle valve IV and a needle valve V, and the outlet of the needle valve IV is connected with the inlet of the inner cold water tank; an outlet of the needle valve V is sequentially provided with an electric regulating valve II, an electromagnetic flow meter II and a separating bed EDI, and an outlet of the separating bed EDI is connected with an inlet of the internal cold water tank; the conductivity meter, the hydrogen conductivity meter and the degassing hydrogen conductivity meter are arranged on an original conductivity measurement water outlet pipeline of the internal cooling water system; the needle valve six is arranged at the inlet of the conductivity meter; the programmable controller receives signals sent by the electrical conductivity meter, the hydrogen conductivity meter and the degassed hydrogen conductivity meter and sends adjusting signals to the electric regulating valve I and the electric regulating valve II according to the degassed hydrogen conductivity and the hydrogen conductivity; the first electromagnetic flowmeter and the second electromagnetic flowmeter are used for displaying bypass treatment capacity.
Preferably, the sodium type/ammonium type cation bed of the utility model is internally provided with specially treated sodium type/ammonium type cation exchange resin.
As preferred, electric conductivity table, hydrogen conductivity table and the hydrogen conductivity table of degasification are used for measuring electric conductivity, hydrogen conductivity and the hydrogen conductivity of interior cold water respectively, and the three adopts same water sample to establish ties and measures in proper order, measures the back water sample and retrieves to interior cold water tank.
Preferably, the sub-bed EDI of the present invention is located behind the sodium/ammonium cation bed, and is a modular device.
Preferably, the sub-bed EDI comprises two modules, and the treatment capacity of each module is 5m3/h。
Compared with the prior art, the utility model, have following advantage and effect: (1) the whole structure is designed reasonably, and the structure is reasonable,the method is safe, reliable and stable for a long time, and simultaneously controls the conductivity and the pH of the cold water in the generator within an expected range, so that the conductivity of the cold water is less than 2 mu S/cm, the pH reaches 8.1-8.6, and the copper content of the cold water in the generator<5 mug/L (the national standard requirement is less than or equal to 20 mug/L); (2) the system is simple, the cost is low, and the transformation and installation on the existing equipment are easy; the application range is wide, and the device can be used for a fixed cooling water system and a double water internal cooling system; (3) high reliability, easy control: the hydrogen conductivity and the degassed hydrogen conductivity are used as treatment quantity control signals of the bypass of the internal cooling water, the conductivity is used for controlling the water supplement of the internal cooling water, and the conductivity measurement is an online chemical instrument with the highest reliability of the current power plant, so the system has very high operation reliability; (4) the pH measurement result has high accuracy: calculating the pH value of the internal cooling water according to the conductivity, the hydrogen conductivity and the degassed hydrogen conductivity of the internal cooling water, wherein the accuracy and the reliability of the method are far higher than those of a direct electrode method; (5) the adaptability is good, and the requirement on the sealing performance of the internal cold water tank is low. The bypass treatment capacity can be flexibly adjusted according to the hydrogen conductivity and the degassed hydrogen conductivity of the inner cooling water, the access quantity of the sub-bed EDI modules can be adjusted at any time, and meanwhile, the sub-bed EDI can not remove alkalizer in the inner cooling water, so that CO of the inner cooling water can be easily treated2Controlling the concentration within an acceptable range; (6) can operate for a long time and is maintenance-free: the separated bed EDI does not need maintenance and can be operated fully automatically; sodium/ammonium cation bed only with Cu in cold water2+Exchanging, wherein the exchange capacity at least meets the requirement of continuous work for a plurality of years; (7) the inner cooling water system has small water supply amount: as the conductivity, the hydrogen conductivity and the degassed hydrogen conductivity are monitored only in operation, and a sampled and measured water sample can directly return to the internal cold water tank, the water loss of the whole internal cold water system is small, and the sub-bed EDI drainage and the alkalizer lost due to the measured hydrogen conductivity need to be supplemented mainly.
Drawings
Fig. 1 is a schematic structural view of a cooling water treatment device in a generator according to an embodiment of the present invention.
In the figure: the system comprises a needle valve Z, a needle valve I1, a needle valve II 5, a needle valve III 6, a needle valve IV 8, a needle valve V9, a needle valve VI 10, a sodium/ammonium anode bed 4, a resin catcher 7, an electric control valve I2, an electric control valve II 11, an electromagnetic flow meter I3, an electromagnetic flow meter II 12, an electric conductivity meter 13, a hydrogen conductivity meter 14, a degassed hydrogen conductivity meter 15, a separate bed EDI16, a programmable controller 17, a generator 18, a cooler 19, an internal cooling water tank 20, a filter 21, a water pump 22, a blow-off valve 23, a vent pipe 24, condensed water 25, demineralized water 26 and an internal cooling water sample 27.
Detailed Description
The present invention will be described in further detail by way of examples with reference to the accompanying drawings, which are illustrative of the present invention and are not intended to limit the present invention.
Examples are given.
Referring to fig. 1, the internal cooling water treatment device for a generator based on the separated bed EDI in the embodiment includes a plurality of needle valves Z, sodium/ammonium anode beds 4, a resin trap 7, a first electric control valve 2, a second electric control valve 11, a first electromagnetic flow meter 3, a second electromagnetic flow meter 12, an electric conductivity meter 13, a hydrogen conductivity meter 14, a degassed hydrogen conductivity meter 15, a separated bed EDI16, a programmable controller 17, and pipelines and valves connected with each other.
The plurality of needle valves Z comprise a first needle valve 1, a second needle valve 5, a third needle valve 6, a fourth needle valve 8, a fifth needle valve 9 and a sixth needle valve 10; the needle valve I1, the electric regulating valve I2 and the electromagnetic flowmeter I3 are arranged on a pipeline connecting an inlet of the sodium/ammonium cation bed 4 with a water outlet pipeline of the cooler 19; the needle valve II 5, the needle valve III 6 and the resin catcher 7 are arranged at the outlet of the sodium/ammonium cation bed 4; the outlet of the resin catcher 7 is respectively provided with a needle valve IV 8 and a needle valve V9, and the outlet of the needle valve IV 8 is connected with the inlet of the inner cooling water tank 20; an outlet of the needle valve five 9 is sequentially provided with an electric regulating valve II 11, an electromagnetic flowmeter II 12 and a separating bed EDI16, and an outlet of the separating bed EDI16 is connected with an inlet of the inner cooling water tank 20; the conductivity meter 13, the hydrogen conductivity meter 14 and the degassed hydrogen conductivity meter 15 are arranged on an original conductivity measurement water outlet pipeline of the internal cooling water system; the needle valve six 10 is arranged at the inlet of the electric conductivity meter 13; the programmable controller 17 receives the signals sent from the electric conductivity meter 13, the hydrogen electric conductivity meter 14 and the degassed hydrogen electric conductivity meter 15, and sends adjusting signals to the electric regulating valve I2 and the electric regulating valve II 11 according to the degassed hydrogen electric conductivity and the hydrogen electric conductivity; the first electromagnetic flowmeter 3 and the second electromagnetic flowmeter 12 are used for displaying bypass treatment capacity.
The outlet of the cold water tank 20 in the cold water treatment device of the embodiment is connected with the cooler 19, the water pump 22 is arranged on the outlet pipeline of the cold water tank 20, the filter 21 is arranged on the outlet pipeline of the cooler 19, the blow-off valve 23, the vent pipe 24, the condensed water 25 and the demineralized water 26 are arranged on the cold water tank 20, and the cold water sample 27 is arranged on the pipeline of the needle valve six 10 and the conductivity meter 13.
In the embodiment, a sodium type/ammonium type cation exchange resin which is specially treated is arranged in the sodium type/ammonium type cation bed 4; the resin has high strength and wear resistance, can run in a large-flow high-flow-rate state, and has the maximum treatment flow of 10m3/h。
In this embodiment, the conductivity meter 13, the hydrogen conductivity meter 14, and the degassed hydrogen conductivity meter 15 are respectively used for measuring the conductivity, the hydrogen conductivity, and the degassed hydrogen conductivity of the internal cooling water, and the three are sequentially measured in series by using the same water sample, and the measured water sample is recycled to the internal cooling water tank 20.
The sub-bed EDI16 is a modular device in the present embodiment; the configuration can be flexibly carried out according to the requirement of the processing capacity.
The sub-bed EDI16 of the present embodiment is generally composed of two modules, and the treatment capacity of each module is 5m3H; the divided bed EDI16 is located after the sodium/ammonium cation bed 4 to ensure that corrosion products in the cold water do not affect the operation of the divided bed EDI 16.
In this embodiment, the first electric control valve 2 and the second electric control valve 11 are adjusted according to the output signal of the programmable controller 17 to control the conductivity and pH of the internal cooling water.
The control process of the internal cooling water treatment device of the generator based on the separated bed EDI in the embodiment is as follows: the cold water treatment device in the generator 18 is arranged at the outlet of a cold water system cooler 19 in the generator; the separate bed EDI16 is connected in series with the sodium/ammonium cation bed 4; needle valve, electric control valve and electromagnetic flowmeter are arranged on the pipeline connecting the inlet of the sodium/ammonium anode bed 4 with the water outlet pipeline of the cooler 19, and the electric conductivity meter 13, the hydrogen electric conductivity meter 14 and the degassed hydrogen electric conductivity meter 15 are arranged in the inner coolingThe programmable controller 17 receives the signals sent from the conductivity meter 13, the hydrogen conductivity meter 14 and the degassed hydrogen conductivity meter 15, and sends a regulating signal to the electric regulating valve according to the degassed hydrogen conductivity and the hydrogen conductivity; the flow meter is used for displaying bypass treatment capacity; the sub-bed EDI16 and the sodium/ammonia type cation bed 4 are used for carrying out the bypass treatment on the internal cooling water to remove CO in the internal cooling water2And Cu2+Reduction of copper corrosion products and CO2The accumulation in the inner cold water reduces the CO in the inner cold water2Concentration, namely maintaining the pH value of the internal cooling water to be more than 8.0, controlling the copper corrosion of the generator to be in a qualified range, and simultaneously ensuring that copper corrosion products are not deposited in a copper wire rod so as to ensure the safe operation of the generator; monitoring CO in cold water in generator by controlling hydrogen conductivity and degassed hydrogen conductivity of cold water in generator2The content, the treatment amount of the bypass is adjusted according to the electrical conductivity of the degassed hydrogen, so that the electrical conductivity and the electrical conductivity of the degassed hydrogen of the internal cooling water are maintained in a reasonable range; the conductivity and pH value of the internal cooling water in the generator are stabilized within the standard range, and the copper content of the internal cooling water is controlled within the qualified range.
The generator internal cooling water treatment device based on the separated bed EDI16 is arranged at the outlet of the generator internal cooling water system cooler 19, so that the temperature of a water sample is not too high. The separate bed EDI16 is connected in series with the sodium/ammonium cation bed 4, while the separate bed EDI16 is provided with a bypass. The water sample passes through the monitoring instrument and then is directly returned to the internal cold water tank 20 after being connected in parallel with the sub-bed EDI16 bypass. When taking a sample, the water sample flow of the measuring pipeline can be reduced for a short time, and the influence on the measurement can be ignored.
In this example, the bypass treatment of cold water adopts a separate bed EDI process to remove only the anions (OH) in the feed water-) Retaining the cation; namely, the inlet water is salt and the outlet water is alkali.
In the embodiment, when the conductivity and the pH of the inner cooling water are qualified, but the copper content exceeds the standard, the larger treatment capacity of the sodium/ammonium cation bed 4 is kept, and meanwhile, the sub-bed EDI16 bypass is opened, so that the operating pressure of the sub-bed EDI16 is reduced.
The amount of cold water treated by the side stream in this example was adjusted based on the difference between the degassed hydrogen conductivity and the hydrogen conductivity of the cold water.
In the embodiment, the water sample for measuring the conductivity, the degassed hydrogen conductivity and the hydrogen conductivity is not discharged outside, and directly returns to the internal cold water tank 20 without water loss, so that water supplement is not needed for a long time. For the measurement of the degassed hydrogen conductivity and the consumption of the hydrogen conductivity cations, the condensate water 25 is used for replenishment.
This example continuously monitors the impurity anions and CO in the cold water by measuring the hydrogen conductivity and the degassed hydrogen conductivity of the cold water2And (4) concentration.
In the embodiment, the sodium/ammonium anode bed 4 is used for performing bypass treatment on the cold water in the generator, so that corrosion products in the cold water are removed, and the hollow copper coil is prevented from being blocked.
This example measured the hydrogen conductivity and the degassed hydrogen conductivity resulting in a continuous reduction of the alkalizing agent in the cold water, and when the conductivity drops to a predetermined value, the alkalizing agent content was adjusted using the ammoniated condensate 25 as make-up water.
In the embodiment, the measurement results of the electrical conductivity, the hydrogen electrical conductivity and the degassed hydrogen electrical conductivity are processed, and the pH value of the internal cooling water is obtained through calculation without adopting a pH electrode for measurement.
In the present embodiment, the electrical conductivity, the hydrogen conductivity, and the degassed hydrogen conductivity are used as input signals of the programmable controller 17, and after data processing, the difference between the hydrogen conductivity and the degassed hydrogen conductivity is used as an output signal of the programmable controller 17.
The electric control valve in this embodiment adjusts the electric conductivity and pH of the internal cooling water to be within a desired range according to an output signal of the programmable controller 17.
In the measurement process of the electrical conductivity of the degassed hydrogen, in order to reduce the temperature of the high-temperature water sample subjected to carbon dioxide removal to an acceptable value of an instrument, one path of water is separately introduced as high-temperature water sample cooling water, and the water sample of the cooling water can be closed water or industrial water. The cooling water can be directly discharged into a unit drainage tank after heat exchange, and can also be recycled to a closed water system or an industrial water system.
The cation exchange column for measuring the hydrogen conductivity adopts a forward flow mode of top inlet and bottom outlet, and the top of the exchange column is provided with the exhaust valve, so that air possibly accumulated at the top of the exchange column can be exhausted. The charged resin is color-changing resin, and when the color-changing resin reaches 3/4 of the total resin amount, the regenerated hydrogen-type resin is charged again.
In the process of measuring the hydrogen conductivity, the alkalizer in the internal cooling water is continuously consumed, and when the conductivity of the internal cooling water is reduced to the preset lower limit value, the electric valve for supplementing the water by the condensed water 25 connected with the internal cooling water tank 20 is started, so that the conductivity of the internal cooling water is increased to the preset upper limit value. In order to ensure the regulation stability, a micro-flow water supplementing mode is adopted. The flow rate of the sampled water sample is 20L/h, and the inner cooling water tank 20 is 2.0m3And the upper and lower limits of the conductivity of the inner cooling water are 1.0 mu S/cm and 1.5 mu S/cm respectively, so that the conductivity of the inner cooling water can be reduced from 1.5 mu S/cm to 1.0 mu S/cm within 100 hours. If the conductivity of the condensed water 25 is 5 mu S/cm, the amount of the condensed water 25 is only required to be supplemented for 100h to be 200L, so that the water supplementing flow is recommended to be controlled to be 100L/h-200L/h, and the water is supplemented for 1 h-2 h every 100 h.
The electric conductivity, the hydrogen electric conductivity and the degassed hydrogen electric conductivity of the embodiment are used as input signals of the programmable controller 17, and the pH value of the internal cooling water can be displayed after data processing. Meanwhile, the programmable controller 17 takes the difference between the hydrogen conductivity and the degassed hydrogen conductivity as an output signal, adjusts the opening of the electric regulating valve, controls the bypass treatment capacity, and finally enables the conductivity of the internal cooling water to be stabilized at 1.0 muS/cm-1.5 muS/cm, the pH value to be 8.0-8.5, and the difference between the hydrogen conductivity and the degassed hydrogen conductivity to be less than 0.5 muS/cm.
According to the characteristics of the cold water in the generator, the cold water is bypassed by using the separate bed EDI16 and the sodium/ammonia type anode bed to remove CO in the cold water2And Cu2+Reduction of copper corrosion products and CO2The accumulation in the inner cold water reduces the CO in the inner cold water2And the concentration, namely the pH value of the internal cooling water is maintained to be more than 8.0, the copper corrosion of the generator is controlled in a qualified range, and meanwhile, the copper corrosion product is prevented from being deposited in a copper wire rod, so that the safe operation of the generator is ensured. Monitoring CO in cold water in generator by controlling hydrogen conductivity and degassed hydrogen conductivity of cold water in generator2The content of the by-pass treatment is adjusted according to the electrical conductivity of the degassed hydrogen, so that the electrical conductivity of the degassed hydrogen of the internal cooling water is equal to that of the by-pass treatmentThe conductivity is maintained within a reasonable range.
The embodiment has the characteristics of simple system, stable water quality, no pollution discharge and the like, and can realize automatic operation; the device and the control method of the embodiment can stabilize the conductivity and the pH value of the internal cooling water of the generator within a standard range, and further control the copper content of the internal cooling water within a qualified range.
And will be apparent to those skilled in the art from the foregoing description.
In addition, it should be noted that the specific embodiments described in the present specification may be different in the components, the shapes of the components, the names of the components, and the like, and the above description is only an example of the structure of the present invention. All the equivalent changes or simple changes made according to the structure, characteristics and principle of the utility model are included in the protection scope of the utility model. Various modifications, additions and substitutions may be made by those skilled in the art without departing from the scope of the invention as defined in the accompanying claims.
Claims (5)
1. The utility model provides a cold water treatment facilities in generator based on divide bed EDI, includes a plurality of needle valves, cooler and interior cold water tank, and this a plurality of needle valves include needle valve one, needle valve two, needle valve three, needle valve four, needle valve five and needle valve six, its characterized in that: the system also comprises a sodium/ammonium cation bed, a resin catcher, a first electric regulating valve, a second electric regulating valve, a first electromagnetic flowmeter, a second electromagnetic flowmeter, a conductivity meter, a hydrogen conductivity meter, a degassing hydrogen conductivity meter, a separate bed EDI and a programmable controller; the needle valve I, the electric regulating valve I and the electromagnetic flowmeter I are arranged on a pipeline connecting the inlet of the sodium/ammonium anode bed with the water outlet pipeline of the cooler; the needle valve II, the needle valve III and the resin catcher are arranged at the outlet of the sodium/ammonium cation bed; the outlet of the resin catcher is respectively provided with a needle valve IV and a needle valve V, and the outlet of the needle valve IV is connected with the inlet of the inner cold water tank; an outlet of the needle valve V is sequentially provided with an electric regulating valve II, an electromagnetic flow meter II and a separating bed EDI, and an outlet of the separating bed EDI is connected with an inlet of the internal cold water tank; the conductivity meter, the hydrogen conductivity meter and the degassing hydrogen conductivity meter are arranged on an original conductivity measurement water outlet pipeline of the internal cooling water system; the needle valve six is arranged at the inlet of the conductivity meter; the programmable controller receives signals sent by the electrical conductivity meter, the hydrogen conductivity meter and the degassed hydrogen conductivity meter and sends adjusting signals to the electric regulating valve I and the electric regulating valve II according to the degassed hydrogen conductivity and the hydrogen conductivity; the first electromagnetic flowmeter and the second electromagnetic flowmeter are used for displaying bypass treatment capacity.
2. The subbed EDI-based cooling water treatment device in a generator according to claim 1, wherein: the sodium type/ammonium type cation bed is internally provided with specially treated sodium type/ammonium type cation exchange resin.
3. The subbed EDI-based cooling water treatment device in a generator according to claim 1, wherein: the electric conductivity meter, the hydrogen electric conductivity meter and the degassed hydrogen electric conductivity meter are respectively used for measuring the electric conductivity, the hydrogen electric conductivity and the degassed hydrogen electric conductivity of the internal cooling water, the three are sequentially measured by adopting the same water sample in series, and the measured water sample is recycled to the internal cooling water tank.
4. The subbed EDI-based cooling water treatment device in a generator according to claim 1, wherein: the sub-bed EDI is located behind the sodium/ammonium cation bed, and is a modular device.
5. The subbed EDI-based cooling water treatment apparatus in a generator according to claim 4, wherein: the sub-bed EDI comprises two modules, and the treatment capacity of each module is 5m3/h。
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| CN112225291A (en) * | 2020-08-11 | 2021-01-15 | 华电电力科学研究院有限公司 | Generator inner cooling water treatment device based on separated bed EDI and control method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112225291A (en) * | 2020-08-11 | 2021-01-15 | 华电电力科学研究院有限公司 | Generator inner cooling water treatment device based on separated bed EDI and control method |
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