CN202116392U - Precision processing device of condensation water of nuclear power station - Google Patents
Precision processing device of condensation water of nuclear power station Download PDFInfo
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- CN202116392U CN202116392U CN 201120065387 CN201120065387U CN202116392U CN 202116392 U CN202116392 U CN 202116392U CN 201120065387 CN201120065387 CN 201120065387 CN 201120065387 U CN201120065387 U CN 201120065387U CN 202116392 U CN202116392 U CN 202116392U
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Abstract
The utility model discloses a precision processing device of condensation water of a nuclear power station, which comprises a preposing filter, a cation exchanger, a resin catcher A, a zwitterion exchanger, a resin catcher B, a pipeline inlet and a pipeline outlet. The pipeline inlet, the preposing filter, the cation exchanger, the resin catcher A, the zwitterion exchanger, the resin catcher B and the pipeline outlet are sequentially connected in series, a first valve is arranged between the pipeline inlet and the preposing filter, a second valve and a third valve are arranged between the preposing filter and the cation exchanger, and a fourth valve is arranged between the resin catcher B and the pipeline outlet. The inlet end of the first valve is connected with one end of a fifth valve, the other end of the fifth valve is connected with the inlet end of the third valve, the outlet end of the second valve is connected with one end of a sixth valve, and the other end of the sixth valve is connected with the pipeline outlet. The precision processing device can meet the depth processing requirements for the condensation water under different operation working conditions.
Description
Technical field
The utility model relates to a kind of Nuclear power plants polishing unit that condenses, and belongs to the Treatment of Industrial Water field.
Background technology
At present in nuclear power generating sets, adopt cation exchanger, resin catcher, zwitterion interchanger, the placed in-line successively mode of resin catcher to accomplish purification of water quality usually to the condensed water of secondary circuit.Treat positively charged ion and the positive resin extender removals of corrosion product in cation exchanger such as ammonia contained in the advanced treatment condensed water; The yin and yang resin filler of condensed water intermediate ion property salt in the zwitterion interchanger further removed; To reach the advanced treatment of condensed water; Because the resin extender that is seated in the ion-exchanger is very sensitive to MOXs such as iron; Need treat in the condensed water of advanced treatment that suspended substance such as MOX puts into operation less than the ion-exchanger that certain content (being mainly iron level less than 1000 μ g/L) could will be equipped with resin extender, avoid causing the pollution of iron, influence resin property and work-ing life resin in the ion-exchanger; Bring unnecessary financial loss (this resinoid is imported product at present, once changes and will spend the millions of units of Renminbi).
At unit starting and new unit operation initial stage; Metallic corrosion products in the condensed water (mainly being the oxide compound of iron) content very high (iron-holder can reach thousands of micrograms per litre); Need the very long flush time of cost (needing several time-of-weeks usually); Great amount of water resources need be consumed simultaneously, the condition (iron-holder is less than 1000 μ g/L) that ion-exchanger is put into operation could be satisfied.In Nuclear power plants, a million kilowatt unit if can shift to an earlier date 1 day and get into commercial operation, just has more than 1,000 ten thousand income, and economic benefit is considerable.
In order to solve at unit starting and new unit operation initial stage; High to metallic corrosion products in the condensed water, as to need the labor water resources to wash problem; The contriver of this patent once invented a kind of power station condensed water accurate process equipment; Its patent No. is ZL201020228931.4, and this power station condensed water accurate process equipment is through adjusting the flow direction of condensed water to the control of valve in the connecting tube, thereby satisfies the requirement of condensate system at the operation condition of different steps.This equipment not only can be saved great lot of water resources than traditional condensed water accurate process equipment, effectively prevents the waste of water resources, and can shorten the unit starting time greatly, has very big economic benefit and social benefit.But the flow direction that this equipment claimed uses a large amount of pipelines and valve to control condensed water; System pipeline is comparatively complicated, and strainer is at the filter core that is used for preposition with the rearmounted different filtering accuracies of use needs replacing, and facility investment is bigger; Operation is relative complex also; And the very high material for core of filtering accuracy adopts plastic material to be made usually, is prone to aging, life-span weak point, needs often to change.When strainer is arranged on the ion-exchange unit back, exist the plastic material after wearing out to get into secondary circuit, cause the risk of secondary pollution.In addition; This device is as no longer being provided with resin catcher in the ion-exchange unit back; When adopting strainer to add ion-exchange unit or only to adopt the operating mode that ion-exchange unit purifies; Existence resin streak occurs and crosses ion-exchange unit entering secondary circuit, causes the risk of heavy corrosion infringement for the secondary circuit heat power equipment.
In sum; Develop and a kind ofly can effectively remove metallic corrosion products and suspended impurity, the cycle of operation that prolongs ion-exchanger is also protected resin extender, and can satisfy the condition (iron level is less than 1000 μ g/L) that ion-exchanger puts into operation as early as possible; Shorten the flushing of pipeline time; Reduce water resource waste, can make running maintenance more simple again, and under different operation conditions; The tiny resin particle of effectively catching guarantees that the condensate clean-up plant of secondary circuit heat power equipment safety has crucial meaning.
The utility model content
The purpose of the utility model is; A kind of Nuclear power plants polishing unit that condenses is provided; It can effectively remove metallic corrosion products and suspended impurity, prolongs the cycle of operation of ion-exchanger and protects resin extender, greatly shortens the time of satisfying the ion-exchanger condition that puts into operation; Can satisfy the operating requirement of condensate clean-up plant under different operating modes again; Effectively solve the serious problem of water resource waste, and can carry out effectively catching the ultrafine particle in the condensed water, but also can increase economic efficiency, simplified system pipeline, the serviceability that improves system and the simplification of operation.
The technical scheme of the utility model: a kind of Nuclear power plants polishing unit that condenses; Comprise fore filter, cation exchanger, resin catcher A, zwitterion interchanger, resin catcher B, pipeline inlet and pipeline outlet; Pipeline inlet, fore filter, cation exchanger, resin catcher A, zwitterion interchanger, resin catcher B and pipeline outlet are connected in series successively; Be provided with valve one between pipeline inlet and the fore filter; Be provided with valve two and valve three between fore filter and the cation exchanger, be provided with valve four between resin catcher B and the pipeline outlet; The inlet end of valve one also is connected with an end of valve five, and the other end of valve five is connected with the inlet end of valve three, and the exit end of valve two also is connected with an end of valve six, and the other end of valve six is connected with the pipeline outlet.The effect of fore filter is with most of metallic corrosion products and suspended substance removal, prolongs the cycle of operation of ion-exchanger and protects resin not contaminated; The effect of cation exchanger is with positively charged ion and part suspended substance removals such as ammonia in the condensed water; The effect of resin catcher A is that the resin that cation exchanger leaks is held back; The effect of zwitterion interchanger is that zwitterion in the condensed water is further removed, to reach the deep purifying of condensed water; The effect of resin catcher B is that the resin that the zwitterion interchanger leaks is held back; Prevent to get into secondary coolant circuit system; After being set, resin catcher B just do not need to be provided with again post-filter; Save the investment of post-filter or save pipeline and the valve that strainer carries out preposition and rearmounted switching, all can save millions of first capital funds.Simultaneously, the trapezoidal wrapping wire pipe of resin catcher adopts stainless steel, has avoided the post-filter filter core to adopt plastic material secondary circuit water quality to be caused the risk of secondary pollution.
Aforesaid this Nuclear power plants condenses in the polishing unit; Described fore filter is made up of fore filter housing, filter core, water-in and water outlet; Filter core is located at the inside of fore filter housing; Water-in is located on the fore filter housing of filter core water inlet side, and water outlet is located on the fore filter housing of filter core water outlet side, and the feed-water end of fore filter housing is provided with manhole; The filtering accuracy of filter core is 1 μ m～30 μ m.
Aforesaid this Nuclear power plants condenses in the polishing unit, and described cation exchanger is the container that positive resin extender is equipped with in inside; Positive resin floor height is 800mm～1600mm in the cation exchanger.
Aforesaid this Nuclear power plants condenses in the polishing unit, and described zwitterion interchanger is the container that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 800mm～1600mm in the zwitterion interchanger, and the ratio of negative resin and positive resin is 1: 2 or 2: 1 or 2: 3 or 3: 2 or 1: 1 or 3: 1.
Aforesaid this Nuclear power plants condenses in the polishing unit; Described resin catcher A is identical with the structural shape of resin catcher B; Form by resin catcher housing, the trapezoidal wrapping wire pipe of stainless steel, fluid inlet and liquid outlet; The trapezoidal wrapping wire pipe of stainless steel is located in the resin catcher housing; Fluid inlet is located on the resin catcher housing of the trapezoidal wrapping wire pipe of stainless steel water inlet side, liquid outlet is located on the resin catcher housing of the trapezoidal wrapping wire pipe of stainless steel water outlet oral-lateral, and the resin catcher lower part of frame also is provided with sewage draining exit.
Aforesaid this Nuclear power plants condenses in the polishing unit, and the slit of the trapezoidal wrapping wire pipe of stainless steel that resin catcher A is inner is 0.1mm～0.3mm; The slit of the trapezoidal wrapping wire pipe of stainless steel that resin catcher B is inner is 0.025mm～0.3mm.
Aforesaid this Nuclear power plants condenses in the polishing unit, and the slit of the trapezoidal wrapping wire pipe of stainless steel that resin catcher B is inner is preferably 0.025mm～0.05mm.Because the effect of resin catcher B is that the resin that the zwitterion interchanger leaks is held back; Prevent to get into secondary coolant circuit system; So extremely small particle can't be held back greater than 0.15mm in the trapezoidal wrapping wire pipe seam of the stainless steel of conventional resins catcher crack, therefore need to use the littler resin catcher in stainless steel trapezoidal wrapping wire pipe seam crack.
Compared with prior art; The utility model is through treating the flow through sequencing of fore filter, cation exchanger, resin catcher A, zwitterion interchanger and resin catcher B of the condensed water of advanced treatment to the control adjustment of valve open and close state in the pipeline; Satisfied the operating requirement of condensate clean-up plant under different operating modes; It can effectively remove metallic corrosion products and suspended impurity, prolongs the cycle of operation of ion-exchanger and protects resin, greatly shortens the time of ion-exchanger condition of putting into operation of satisfying, effectively solves the serious problem of water resource waste; And ultrafine broken resin particle carried out effectively catching; When greatly increasing economic efficiency, also simplify the pipeline of system, improved the serviceability of system and the simplification of operation.Because the trapezoidal wrapping wire pipe of resin catcher adopts stainless steel, also avoided the post-filter filter core to adopt plastic material secondary circuit water quality to be caused the risk of secondary pollution.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 is the structural representation of fore filter;
Fig. 3 is the structural representation of resin catcher.
Being labeled as in the accompanying drawing: 1-fore filter, 2-cation exchanger, 3-resin catcher A, 4-zwitterion interchanger, 5-resin catcher B, 6-pipeline inlet; The outlet of 7-pipeline, 8-valve one, 9-valve two, 10-valve three, 11-valve four, 12-valve five; 13-valve six, 14-filter core, the trapezoidal wrapping wire pipe of 15-stainless steel, 16-fore filter housing, 17-water-in, 18-water outlet; The 19-manhole, 20-resin catcher housing, 21-fluid inlet, 22-liquid outlet, 23-sewage draining exit.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is further described.
The embodiment 1 of the utility model: a kind of Nuclear power plants polishing unit that condenses; Comprise fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5, pipeline inlet 6 and pipeline outlet 7; Pipeline inlet 6, fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and pipeline outlet 7 are connected in series successively; Be provided with valve 1 between pipeline inlet 6 and the fore filter 1; Be provided with valve 29 and valve 3 10 between fore filter 1 and the cation exchanger 2, be provided with valve 4 11 between resin catcher B5 and the pipeline outlet 7; The inlet end of valve 1 also is connected with an end of valve 5 12, and the other end of valve 5 12 is connected with the inlet end of valve 3 10, and the exit end of valve 29 also is connected with an end of valve 6 13, and the other end of valve 6 13 is connected with pipeline outlet 7.Described fore filter 1 is made up of fore filter housing 16, filter core 14, water-in 17 and water outlet 18; Filter core 14 is located at the inside of fore filter housing 16; Water-in 17 is located on the fore filter housing 16 of filter core 14 water inlet sides; Water outlet 18 is located on the fore filter housing 16 of filter core 14 water outlet sides, and the feed-water end of fore filter housing 16 is provided with manhole 19; The filtering accuracy of filter core 14 is 1 μ m.Described cation exchanger 2 is containers that positive resin extender is equipped with in inside; Positive resin floor height is 800mm in the cation exchanger.Described zwitterion interchanger 4 is containers that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 800mm in the zwitterion interchanger, and the ratio of negative resin and positive resin is 1: 2.Described resin catcher A3 is identical with the structural shape of resin catcher B5; Form by the trapezoidal wrapping wire pipe of resin catcher housing 20, stainless steel 15, fluid inlet 21 and liquid outlet 22; The trapezoidal wrapping wire pipe 15 of stainless steel is located in the resin catcher housing 20; Fluid inlet 21 is located on the resin catcher housing 20 of trapezoidal wrapping wire pipe 15 water inlet sides of stainless steel, liquid outlet 22 is located on the resin catcher housing 20 of the trapezoidal wrapping wire pipe 15 water outlet oral-laterals of stainless steel, and the bottom of resin catcher housing 20 also is provided with sewage draining exit 23.The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher A3 is inner is 0.1mm; The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher B5 is inner is 0.025mm.
The embodiment 2 of the utility model: a kind of Nuclear power plants polishing unit that condenses; Comprise fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5, pipeline inlet 6 and pipeline outlet 7; Pipeline inlet 6, fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and pipeline outlet 7 are connected in series successively; Be provided with valve 1 between pipeline inlet 6 and the fore filter 1; Be provided with valve 29 and valve 3 10 between fore filter 1 and the cation exchanger 2, be provided with valve 4 11 between resin catcher B5 and the pipeline outlet 7; The inlet end of valve 1 also is connected with an end of valve 5 12, and the other end of valve 5 12 is connected with the inlet end of valve 3 10, and the exit end of valve 29 also is connected with an end of valve 6 13, and the other end of valve 6 13 is connected with pipeline outlet 7.Described fore filter 1 is made up of fore filter housing 16, filter core 14, water-in 17 and water outlet 18; Filter core 14 is located at the inside of fore filter housing 16; Water-in 17 is located on the fore filter housing 16 of filter core 14 water inlet sides; Water outlet 18 is located on the fore filter housing 16 of filter core 14 water outlet sides, and the feed-water end of fore filter housing 16 is provided with manhole 19; The filtering accuracy of filter core 14 is 5 μ m.Described cation exchanger 2 is containers that positive resin extender is equipped with in inside; Positive resin floor height is 1000mm in the cation exchanger.Described zwitterion interchanger 4 is containers that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 1000mm in the zwitterion interchanger, and the ratio of negative resin and positive resin is 2: 1.Described resin catcher A3 is identical with the structural shape of resin catcher B5; Form by the trapezoidal wrapping wire pipe of resin catcher housing 20, stainless steel 15, fluid inlet 21 and liquid outlet 22; The trapezoidal wrapping wire pipe 15 of stainless steel is located in the resin catcher housing 20; Fluid inlet 21 is located on the resin catcher housing 20 of trapezoidal wrapping wire pipe 15 water inlet sides of stainless steel, liquid outlet 22 is located on the resin catcher housing 20 of the trapezoidal wrapping wire pipe 15 water outlet oral-laterals of stainless steel, and the bottom of resin catcher housing 20 also is provided with sewage draining exit 23.The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher A3 is inner is 0.15mm; The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher B5 is inner is 0.05mm.
The embodiment 3 of the utility model: a kind of Nuclear power plants polishing unit that condenses; Comprise fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5, pipeline inlet 6 and pipeline outlet 7; Pipeline inlet 6, fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and pipeline outlet 7 are connected in series successively; Be provided with valve 1 between pipeline inlet 6 and the fore filter 1; Be provided with valve 29 and valve 3 10 between fore filter 1 and the cation exchanger 2, be provided with valve 4 11 between resin catcher B5 and the pipeline outlet 7; The inlet end of valve 1 also is connected with an end of valve 5 12, and the other end of valve 5 12 is connected with the inlet end of valve 3 10, and the exit end of valve 29 also is connected with an end of valve 6 13, and the other end of valve 6 13 is connected with pipeline outlet 7.Described fore filter 1 is made up of fore filter housing 16, filter core 14, water-in 17 and water outlet 18; Filter core 14 is located at the inside of fore filter housing 16; Water-in 17 is located on the fore filter housing 16 of filter core 14 water inlet sides; Water outlet 18 is located on the fore filter housing 16 of filter core 14 water outlet sides, and the feed-water end of fore filter housing 16 is provided with manhole 19; The filtering accuracy of filter core 14 is 10 μ m.Described cation exchanger 2 is containers that positive resin extender is equipped with in inside; Positive resin floor height is 1200mm in the cation exchanger.Described zwitterion interchanger 4 is containers that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 1200mm in the zwitterion interchanger, and the ratio of negative resin and positive resin is 2: 3.Described resin catcher A3 is identical with the structural shape of resin catcher B5; Form by the trapezoidal wrapping wire pipe of resin catcher housing 20, stainless steel 15, fluid inlet 21 and liquid outlet 22; The trapezoidal wrapping wire pipe 15 of stainless steel is located in the resin catcher housing 20; Fluid inlet 21 is located on the resin catcher housing 20 of trapezoidal wrapping wire pipe 15 water inlet sides of stainless steel, liquid outlet 22 is located on the resin catcher housing 20 of the trapezoidal wrapping wire pipe 15 water outlet oral-laterals of stainless steel, and the bottom of resin catcher housing 20 also is provided with sewage draining exit 23.The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher A3 is inner is 0.15mm; The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher B5 is inner is 0.1mm.
The embodiment 4 of the utility model: a kind of Nuclear power plants polishing unit that condenses; Comprise fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5, pipeline inlet 6 and pipeline outlet 7; Pipeline inlet 6, fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and pipeline outlet 7 are connected in series successively; Be provided with valve 1 between pipeline inlet 6 and the fore filter 1; Be provided with valve 29 and valve 3 10 between fore filter 1 and the cation exchanger 2, be provided with valve 4 11 between resin catcher B5 and the pipeline outlet 7; The inlet end of valve 1 also is connected with an end of valve 5 12, and the other end of valve 5 12 is connected with the inlet end of valve 3 10, and the exit end of valve 29 also is connected with an end of valve 6 13, and the other end of valve 6 13 is connected with pipeline outlet 7.Described fore filter 1 is made up of fore filter housing 16, filter core 14, water-in 17 and water outlet 18; Filter core 14 is located at the inside of fore filter housing 16; Water-in 17 is located on the fore filter housing 16 of filter core 14 water inlet sides; Water outlet 18 is located on the fore filter housing 16 of filter core 14 water outlet sides, and the feed-water end of fore filter housing 16 is provided with manhole 19; The filtering accuracy of filter core 14 is 15 μ m.Described cation exchanger 2 is containers that positive resin extender is equipped with in inside; Positive resin floor height is 1400mm in the cation exchanger.Described zwitterion interchanger 4 is containers that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 1400mm in the zwitterion interchanger, and the ratio of negative resin and positive resin is 3: 2.Described resin catcher A3 is identical with the structural shape of resin catcher B5; Form by the trapezoidal wrapping wire pipe of resin catcher housing 20, stainless steel 15, fluid inlet 21 and liquid outlet 22; The trapezoidal wrapping wire pipe 15 of stainless steel is located in the resin catcher housing 20; Fluid inlet 21 is located on the resin catcher housing 20 of trapezoidal wrapping wire pipe 15 water inlet sides of stainless steel, liquid outlet 22 is located on the resin catcher housing 20 of the trapezoidal wrapping wire pipe 15 water outlet oral-laterals of stainless steel, and the bottom of resin catcher housing 20 also is provided with sewage draining exit 23.The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher A3 is inner is 0.2mm; The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher B5 is inner is 0.15mm.
The embodiment 5 of the utility model: a kind of Nuclear power plants polishing unit that condenses; Comprise fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5, pipeline inlet 6 and pipeline outlet 7; Pipeline inlet 6, fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and pipeline outlet 7 are connected in series successively; Be provided with valve 1 between pipeline inlet 6 and the fore filter 1; Be provided with valve 29 and valve 3 10 between fore filter 1 and the cation exchanger 2, be provided with valve 4 11 between resin catcher B5 and the pipeline outlet 7; The inlet end of valve 1 also is connected with an end of valve 5 12, and the other end of valve 5 12 is connected with the inlet end of valve 3 10, and the exit end of valve 29 also is connected with an end of valve 6 13, and the other end of valve 6 13 is connected with pipeline outlet 7.Described fore filter 1 is made up of fore filter housing 16, filter core 14, water-in 17 and water outlet 18; Filter core 14 is located at the inside of fore filter housing 16; Water-in 17 is located on the fore filter housing 16 of filter core 14 water inlet sides; Water outlet 18 is located on the fore filter housing 16 of filter core 14 water outlet sides, and the feed-water end of fore filter housing 16 is provided with manhole 19; The filtering accuracy of filter core 14 is 20 μ m.Described cation exchanger 2 is containers that positive resin extender is equipped with in inside; Positive resin floor height is 1500mm in the cation exchanger.Described zwitterion interchanger 4 is containers that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 1500mm in the zwitterion interchanger, and the ratio of negative resin and positive resin is 1: 1.Described resin catcher A3 is identical with the structural shape of resin catcher B5; Form by the trapezoidal wrapping wire pipe of resin catcher housing 20, stainless steel 15, fluid inlet 21 and liquid outlet 22; The trapezoidal wrapping wire pipe 15 of stainless steel is located in the resin catcher housing 20; Fluid inlet 21 is located on the resin catcher housing 20 of trapezoidal wrapping wire pipe 15 water inlet sides of stainless steel, liquid outlet 22 is located on the resin catcher housing 20 of the trapezoidal wrapping wire pipe 15 water outlet oral-laterals of stainless steel, and the bottom of resin catcher housing 20 also is provided with sewage draining exit 23.The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher A3 is inner is 0.25mm; The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher B5 is inner is 0.2mm.
The embodiment 6 of the utility model: a kind of Nuclear power plants polishing unit that condenses; Comprise fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5, pipeline inlet 6 and pipeline outlet 7; Pipeline inlet 6, fore filter 1, cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and pipeline outlet 7 are connected in series successively; Be provided with valve 1 between pipeline inlet 6 and the fore filter 1; Be provided with valve 29 and valve 3 10 between fore filter 1 and the cation exchanger 2, be provided with valve 4 11 between resin catcher B5 and the pipeline outlet 7; The inlet end of valve 1 also is connected with an end of valve 5 12, and the other end of valve 5 12 is connected with the inlet end of valve 3 10, and the exit end of valve 29 also is connected with an end of valve 6 13, and the other end of valve 6 13 is connected with pipeline outlet 7.Described fore filter 1 is made up of fore filter housing 16, filter core 14, water-in 17 and water outlet 18; Filter core 14 is located at the inside of fore filter housing 16; Water-in 17 is located on the fore filter housing 16 of filter core 14 water inlet sides; Water outlet 18 is located on the fore filter housing 16 of filter core 14 water outlet sides, and the feed-water end of fore filter housing 16 is provided with manhole 19; The filtering accuracy of filter core 14 is 30 μ m.Described cation exchanger 2 is containers that positive resin extender is equipped with in inside; Positive resin floor height is 1600mm in the cation exchanger.Described zwitterion interchanger 4 is containers that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 1600mm in the zwitterion interchanger, and the ratio of negative resin and positive resin is 3: 1.Described resin catcher A3 is identical with the structural shape of resin catcher B5; Form by the trapezoidal wrapping wire pipe of resin catcher housing 20, stainless steel 15, fluid inlet 21 and liquid outlet 22; The trapezoidal wrapping wire pipe 15 of stainless steel is located in the resin catcher housing 20; Fluid inlet 21 is located on the resin catcher housing 20 of trapezoidal wrapping wire pipe 15 water inlet sides of stainless steel, liquid outlet 22 is located on the resin catcher housing 20 of the trapezoidal wrapping wire pipe 15 water outlet oral-laterals of stainless steel, and the bottom of resin catcher housing 20 also is provided with sewage draining exit 23.The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher A3 is inner is 0.3mm; The slit of the trapezoidal wrapping wire pipe 15 of stainless steel that resin catcher B5 is inner is 0.3mm.
The principle of work of the utility model: at unit starting and new unit operation initial stage; Suspension contents such as the metallic corrosion products in the condensed water are very high; Wherein metallic corrosion products mainly is the oxide compound of iron; At first need confirm the content of iron in the corrosion product, judge how to handle condensed water according to the content of iron in the condensed water then.
In treating the advanced treatment condensed water iron-holder of metallic corrosion products before processing greater than 1000 μ g/L; Then Open valve 1, valve 29 and valve 6 13; Valve-off 5 12, valve 3 10 and valve 4 11 treat that the advanced treatment condensed water gets into pipeline through pipeline inlet 6, flows in the fore filter 1 through valve 1; Through metallic corrosion products and the suspended impurity that fore filter 1 is removed in the condensed water, metallic corrosion products and suspended impurity content in the condensed water are reduced; If the iron level in the condensed water after fore filter 1 is handled is still greater than 1000 μ g/L; Then valve-off 3 10 and valve 4 11; Open valve 6 13 from fore filter 1 effusive condensed water directly flow through valve 29 and valve 6 13, directly flows out from pipeline outlet 7 at last;
If the iron level in the condensed water after process fore filter 1 is handled is between 500 μ g/L～1000 μ g/L; Then Open valve 3 10 and valve 4 11; Valve-off 6 13;, flow out from pipeline outlet 7 at last through valve 29 and valve 3 10 flow through successively cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and valve 4 11 from fore filter 1 effusive condensed water; Perhaps, flow out from pipeline outlet 7 at last letting its cation exchanger 2 of flowing through, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and valve 4 11 after condensed water process fore filter filtration again again.
If the iron level in the condensed water after process fore filter 1 is handled is less than 500 μ g/L; Then Open valve 3 10 and valve 4 11; Valve-off 6 13;, flow out from pipeline outlet 7 at last through valve 29 and valve 3 10 flow through successively cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and valve 4 11 from fore filter 1 effusive condensed water.
If the iron-holder of treating metallic corrosion products in the condensed water of advanced treatment before handling less than 1000 μ g/L; Then Open valve 1, valve 29, valve 3 10 and valve 4 11; Valve-off 5 12 and valve 6 13; Treat that the advanced treatment condensed water gets into pipeline through pipeline inlet 6; Flow in the fore filters 1 through valve 1, through valve 29 and valve 3 10 flow through successively cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and valve 4 11, flow out from pipeline outlet 7 at last from fore filter 1 effusive condensed water; Can also let the condensed water of treating advanced treatment flow directly into cation exchanger 2, resin catcher A3, zwitterion interchanger 4, resin catcher B5 and valve 4 11, flow out from pipeline outlet 7 at last through valve 5 12 and valve 3 10.
Claims (7)
1. Nuclear power plants polishing unit that condenses; It is characterized in that: comprise fore filter (1), cation exchanger (2), resin catcher A (3), zwitterion interchanger (4), resin catcher B (5), pipeline inlet (6) and pipeline outlet (7); Pipeline inlet (6), fore filter (1), cation exchanger (2), resin catcher A (3), zwitterion interchanger (4), resin catcher B (5) and pipeline outlet (7) are connected in series successively; Be provided with valve one (8) between pipeline inlet (6) and the fore filter (1); Be provided with valve two (9) and valve three (10) between fore filter (1) and the cation exchanger (2), be provided with valve four (11) between resin catcher B (5) and the pipeline outlet (7); The inlet end of valve one (8) also is connected with an end of valve five (12); The other end of valve five (12) is connected with the inlet end of valve three (10); The exit end of valve two (9) also is connected with an end of valve six (13), and the other end of valve six (13) is connected with pipeline outlet (7).
2. the Nuclear power plants according to claim 1 polishing unit that condenses; It is characterized in that: described fore filter (1) is made up of fore filter housing (16), filter core (14), water-in (17) and water outlet (18); Filter core (14) is located at the inside of fore filter housing (16); Water-in (17) is located on the fore filter housing (16) of filter core (14) water inlet side; Water outlet (18) is located on the fore filter housing (16) of filter core (14) water outlet side, and the feed-water end of fore filter housing (16) is provided with manhole (19); The filtering accuracy of filter core (14) is 1 μ m～30 μ m.
3. the Nuclear power plants according to claim 1 polishing unit that condenses, it is characterized in that: described cation exchanger (2) is the container that positive resin extender is equipped with in inside; Positive resin floor height is 800mm～1600mm in the cation exchanger.
4. the Nuclear power plants according to claim 1 polishing unit that condenses, it is characterized in that: described zwitterion interchanger (4) is the container that negative resin and positive mixed with resin filler are equipped with in inside; Total floor height of negative resin and positive resin is 800mm～1600mm in the zwitterion interchanger.
5. the Nuclear power plants according to claim 1 polishing unit that condenses; It is characterized in that: described resin catcher A (3) is identical with the structural shape of resin catcher B (5); Form by resin catcher housing (20), the trapezoidal wrapping wire pipe of stainless steel (15), fluid inlet (21) and liquid outlet (22); The trapezoidal wrapping wire pipe of stainless steel (15) is located in the resin catcher housing (20); Fluid inlet (21) is located at that the resin catcher housing (20) of the trapezoidal wrapping wire pipe of stainless steel (15) water inlet side is gone up, liquid outlet (22) is located on the resin catcher housing (20) of the trapezoidal wrapping wire pipe of stainless steel (15) water outlet oral-lateral, and the bottom of resin catcher housing (20) also is provided with sewage draining exit (23).
6. the Nuclear power plants according to claim 5 polishing unit that condenses is characterized in that: the slit of the trapezoidal wrapping wire pipe of stainless steel (15) that resin catcher A (3) is inner is 0.1mm ~ 0.3mm; The slit of the trapezoidal wrapping wire pipe of stainless steel (15) that resin catcher B (5) is inner is 0.025 mm ~ 0.3mm.
7. the Nuclear power plants according to claim 6 polishing unit that condenses is characterized in that: the slit of the trapezoidal wrapping wire pipe of stainless steel (15) that resin catcher B (5) is inner is preferably 0.025 mm ~ 0.05mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120065387 CN202116392U (en) | 2011-03-14 | 2011-03-14 | Precision processing device of condensation water of nuclear power station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120065387 CN202116392U (en) | 2011-03-14 | 2011-03-14 | Precision processing device of condensation water of nuclear power station |
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| Publication Number | Publication Date |
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| CN202116392U true CN202116392U (en) | 2012-01-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201120065387 Expired - Lifetime CN202116392U (en) | 2011-03-14 | 2011-03-14 | Precision processing device of condensation water of nuclear power station |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102161542A (en) * | 2011-03-14 | 2011-08-24 | 华电水处理技术工程有限公司 | Method and device for precisely processing nuclear power station condensation water |
-
2011
- 2011-03-14 CN CN 201120065387 patent/CN202116392U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102161542A (en) * | 2011-03-14 | 2011-08-24 | 华电水处理技术工程有限公司 | Method and device for precisely processing nuclear power station condensation water |
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Owner name: HUADIAN WATER ENGINEERING CO., LTD. Free format text: FORMER OWNER: HUADIAN WATER TREATMENT TECHNOLOGY ENGINEERING CO.,LTD Effective date: 20120521 |
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| C41 | Transfer of patent application or patent right or utility model | ||
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Effective date of registration: 20120521 Address after: 100035, B building, Huadian building, No. 273, inner main street, Xizhimen, Beijing, Xicheng District Co-patentee after: China Huadian Engineering (Group) Co., Ltd. Patentee after: Huadian Water Engineering Co., Ltd. Address before: 100035 Beijing City, Xicheng District Xizhimen Avenue 273 Huadian Engineering building B block 503 Co-patentee before: China Huadian Engineering (Group) Co., Ltd. Patentee before: Huadian Water Treatment Technology Engineering Co., Ltd. |
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