[go: up one dir, main page]

CN204111377U - A kind of nuclear power condensate polishing treatment strainer - Google Patents

A kind of nuclear power condensate polishing treatment strainer Download PDF

Info

Publication number
CN204111377U
CN204111377U CN201420618797.7U CN201420618797U CN204111377U CN 204111377 U CN204111377 U CN 204111377U CN 201420618797 U CN201420618797 U CN 201420618797U CN 204111377 U CN204111377 U CN 204111377U
Authority
CN
China
Prior art keywords
water
water outlet
porous plate
water distribution
plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN201420618797.7U
Other languages
Chinese (zh)
Inventor
王旭
吴银
张进
王俊坚
刘勇
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nanjing Cec Environmental Protection Co Ltd
Original Assignee
Nanjing Cec Environmental Protection Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nanjing Cec Environmental Protection Co Ltd filed Critical Nanjing Cec Environmental Protection Co Ltd
Priority to CN201420618797.7U priority Critical patent/CN204111377U/en
Application granted granted Critical
Publication of CN204111377U publication Critical patent/CN204111377U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Treatment Of Water By Ion Exchange (AREA)

Abstract

一种凝结水精处理用过滤器,包括壳体、布水装置和出水装置,所述的壳体为柱状结构,壳体的直径为3200mm至4200mm,柱体高度为2000mm至3500mm;所述的壳体由两个等径曲面封头和一个柱形筒体焊接而成;所述的布水装置由可拆卸的挡水板、外围圈板、支撑杆、布水多孔板、布水多孔板上设有布水水帽,支撑杆连接在布水多孔板和封头之间,可拆卸挡水板安装在设备本体封头进水口下方。本实用新型采用大直径的柱状结构,设备处理水量大幅提高,大大降低水流扰动,保证了树脂层的稳定;从而提高出水水质。

A filter for condensate polishing, including a housing, a water distribution device and a water outlet device, the housing is a columnar structure, the diameter of the housing is 3200mm to 4200mm, and the height of the cylinder is 2000mm to 3500mm; The shell is welded by two equal-diameter curved heads and a cylindrical cylinder; the water distribution device is composed of a detachable water baffle, a peripheral ring plate, a support rod, a water distribution perforated plate, and a water distribution perforated plate There is a water distribution cap on the top, the support rod is connected between the water distribution porous plate and the head, and the detachable water baffle is installed under the water inlet of the head of the equipment body. The utility model adopts a large-diameter columnar structure, which can greatly increase the amount of water treated by the equipment, greatly reduce the disturbance of the water flow, and ensure the stability of the resin layer; thereby improving the quality of the effluent.

Description

一种核电凝结水精处理用过滤器A filter for nuclear power condensate polishing

技术领域technical field

本实用新型涉及一种核电二回路超大离子交换设备即凝结水精处理用过滤器,特别适用于核电站凝结水精处理系统,属于工业水处理领域。The utility model relates to an ultra-large ion exchange device of a nuclear power secondary circuit, that is, a filter for condensate fine treatment, which is especially suitable for a nuclear power plant condensate fine treatment system and belongs to the field of industrial water treatment.

背景技术Background technique

目前,根据国家节能环保政策,大力发展核电和火力发电厂大容量高参数机组取代小型机组是发展趋势。2003年以来,火电新建机组多为600MW、1000MW超临界及超超临界参数机组,核电站新建机组也多为1000MW参数机组,因而对凝结水量和水汽品质要求也愈来愈高。若采用直径较小的离子交换设备,则需要增加设备数量,同时相应增加了系统管道、阀门等部件,使整个系统占地面积增大,同时增加了系统自动控制的难度,给系统安全、稳定运行带来风险。且设备数量增多,导致树脂填料体外再生频繁,增大了体外再生系统设备的工作压力,而由于再生耗时固定且必须,严重时有可能导致失效树脂来不及再生,影响系统连续运行。现有的球形过滤设备,因其本身结构问题,进水通过布水板时由于设备空间渐大,使水流延弧面向四周扩散,不能形成柱形下向流,易使设备运行中水流分布不均匀,易产生偏流、紊流,水流扰动树脂填料。另外,传统柱形过滤设备柱形高度小于2000mm,水垫层高度小于600mm,使水流得不到足够缓冲,易搅动树脂填料,使出水质量和周期制水量降低,系统的运行成本较高等问题。At present, according to the national energy conservation and environmental protection policy, it is a development trend to vigorously develop large-capacity and high-parameter units in nuclear power and thermal power plants to replace small units. Since 2003, most of the newly-built thermal power units are 600MW, 1000MW supercritical and ultra-supercritical units, and most of the new nuclear power plant units are 1000MW units, so the requirements for condensate volume and water vapor quality are getting higher and higher. If ion exchange equipment with a smaller diameter is used, the number of equipment needs to be increased, and at the same time, system pipes, valves and other components are correspondingly increased, which increases the area occupied by the entire system and increases the difficulty of automatic control of the system, making the system safe and stable. Running carries risks. Moreover, the increase in the number of equipment leads to frequent in vitro regeneration of resin fillers, which increases the working pressure of the in vitro regeneration system equipment. However, due to the fixed and necessary regeneration time, in severe cases, it may cause the failed resin to be regenerated too late, affecting the continuous operation of the system. The existing spherical filter equipment, due to its own structural problems, when the water enters through the water distribution plate, due to the increasing space of the equipment, the water flows along the arc and spreads around, and cannot form a columnar downward flow, which easily causes the water flow distribution during the operation of the equipment to be uneven. Uniform, easy to produce bias flow, turbulent flow, water flow disturbance resin filler. In addition, the columnar height of the traditional columnar filtration equipment is less than 2000mm, and the height of the water cushion is less than 600mm, so that the water flow cannot be sufficiently buffered, the resin filler is easily stirred, the quality of the effluent and the amount of periodic water production are reduced, and the operating cost of the system is relatively high.

实用新型内容Utility model content

本实用新型的目的在于,提供一种核电二回路超大离子交换设备即核电凝结水精处理用过滤器,其设备直径增大,处理水量大幅提高,减少了设备数量,降低系统自动控制的难度,节约了系统的占地面积;柱状筒体使进水形成均匀柱状下向流,它可以确保布水均匀;设备高度增加,提高水垫层高度,即使水流得到足够缓冲,避免偏流、紊流,进而避免树脂填料扰动,又使水流在设备中停留时间增长,可以提高出水质量和周期制水量,延长设备树脂填料的使用寿命,降低系统的运行成本。The purpose of this utility model is to provide a nuclear power secondary circuit ultra-large ion exchange equipment, that is, a filter for nuclear power condensate polishing treatment. The diameter of the equipment is increased, the amount of treated water is greatly increased, the number of equipment is reduced, and the difficulty of automatic control of the system is reduced. The floor area of the system is saved; the columnar cylinder makes the water flow form a uniform columnar downward flow, which can ensure uniform water distribution; the height of the equipment is increased to increase the height of the water cushion, even if the water flow is sufficiently buffered, to avoid bias and turbulent flow, Furthermore, the disturbance of the resin filler is avoided, and the residence time of the water flow in the equipment is increased, which can improve the quality of the effluent water and the amount of periodic water production, prolong the service life of the resin filler of the equipment, and reduce the operating cost of the system.

本实用新型的技术方案:一种核电凝结水精处理用过滤器,包括壳体、布水装置和出水装置,所述的壳体为柱状结构,壳体的直径为3200mm至4200mm,柱体高度为2000mm至3500mm;所述的壳体由两个等径曲面封头和一个柱形筒体焊接而成;所述的布水装置由可拆卸的挡水板、外围圈板、支撑杆、布水多孔板、布水多孔板上设有布水水帽,支撑杆连接在布水多孔板和封头之间,可拆卸挡水板安装在设备本体封头进水口下方。The technical solution of the utility model: a filter for nuclear power condensate polishing, including a shell, a water distribution device and a water outlet device, the shell is a columnar structure, the diameter of the shell is 3200mm to 4200mm, and the height of the column is 2000mm to 3500mm; the shell is welded by two isometric curved heads and a cylindrical cylinder; the water distribution device consists of a detachable water baffle, a peripheral ring plate, The water distribution perforated plate and the water distribution perforated plate are provided with water distribution caps, the support rod is connected between the water distribution perforated plate and the head, and the detachable water baffle is installed under the water inlet of the head of the equipment body.

前述的凝结水精处理用过滤器中,所述的布水多孔板是由一块圆形平板开孔而成,含一块自带均匀分布水帽的椭圆形内人孔板安装在圆形平板的开孔上。椭圆形内人孔板可拆卸,便于布水多孔板上部检修。In the aforementioned filter for condensate polishing, the water distribution perforated plate is made of a circular plate with holes, and an oval inner manhole plate with an evenly distributed water cap is installed on the circular plate. on the opening. The oval inner manhole plate is detachable, which is convenient for the upper maintenance of the water distribution perforated plate.

前述的凝结水精处理用过滤器中,所述的壳体的内壁与布水多孔板边缘连接方式为焊接方式。In the aforementioned filter for condensate polishing, the inner wall of the housing and the edge of the water distribution porous plate are connected by welding.

前述的凝结水精处理用过滤器中,所述出水装置由出水多孔板、出水多孔板上均匀分布出水水帽、支撑柱和出水挡板组成,支撑柱连接在出水多孔板和封头之间,出水多孔板和支撑柱焊接而成,且出水挡板焊接在出水口上方。In the aforementioned filter for condensate polishing, the water outlet device is composed of a water outlet porous plate, a water outlet cap evenly distributed on the water outlet porous plate, a support column and a water outlet baffle, and the support column is connected between the water outlet porous plate and the head , the water outlet porous plate and the support column are welded, and the water outlet baffle is welded above the water outlet.

前述的凝结水精处理用过滤器中,所述出水装置的出水多孔板边缘与壳体焊接。In the aforementioned filter for condensate polishing, the edge of the water outlet porous plate of the water outlet device is welded to the shell.

本实用新型有益效果:与现有技术相比,本实用新型采用一种核电二回路超大离子交换(过滤)设备,本实用新型采用大直径的柱状结构,设备处理水量大幅提高,减少系统设备和进口自动阀门、配套仪器仪表、管道数量,减少占地空间、降低系统投入成本;其布水装置可采用可拆卸挡板+圈板、多孔板+水帽二级布水装置;出水装置使用出水多孔板+出水水帽+出水口挡板集水装置形式。因设备直径增大,处理水量大幅提高,减少了设备数量,降低系统自动控制的难度,节约了系统的占地面积;柱状筒体使进水形成均匀柱状下向流,它可以确保布水均匀;设备高度增加,提高水垫层高度,使水流得到足够缓冲,避免偏流、紊流,避免树脂填料扰动,同时柱状筒体增高(过滤器柱体高度超过常规2000mm,使水垫层高度增加,大大减小进水的水流冲击,确保树脂层水流平稳,流速有所降低),使水流在设备中停留时间增长,可以提高出水质量和周期制水量,延长设备树脂填料的使用寿命,降低系统的运行成本;设备下部出水装置取消了不锈钢夹套封头,降低了设备制造成本。增长水流与离子交换剂的接触时间,进水形成均匀柱状流动,大大降低水流扰动,保证了树脂层的稳定;从而提高出水水质;出水装置使用出水多孔板+出水水帽+出水口挡板集水装置形式,可以提高出水质量和周期制水量,延长设备中离子交换剂的使用寿命,降低系统的运行成本。Beneficial effects of the utility model: Compared with the prior art, the utility model adopts a super large ion exchange (filter) equipment for the secondary circuit of nuclear power. The utility model adopts a columnar structure with a large diameter, and the amount of water treated by the equipment is greatly improved, reducing system equipment and Imported automatic valves, supporting instruments and meters, and the number of pipelines reduce floor space and system input costs; the water distribution device can use detachable baffle + ring plate, perforated plate + water cap secondary water distribution device; the water outlet device uses water outlet Porous plate + water outlet cap + water outlet baffle water collection device form. Due to the increase of the diameter of the equipment, the amount of treated water is greatly increased, the number of equipment is reduced, the difficulty of automatic control of the system is reduced, and the floor area of the system is saved; the columnar cylinder makes the influent water form a uniform columnar downward flow, which can ensure uniform water distribution ; Increase the height of the equipment, increase the height of the water cushion, so that the water flow can be sufficiently buffered, avoid bias flow, turbulent flow, and avoid disturbance of the resin filler. Greatly reduce the water flow impact of the incoming water, ensure that the water flow in the resin layer is stable, and the flow velocity is reduced), so that the residence time of the water flow in the equipment increases, which can improve the quality of the effluent water and the amount of periodic water production, prolong the service life of the equipment resin filler, and reduce the system. Operating cost; the water outlet device at the bottom of the equipment cancels the stainless steel jacketed head, which reduces the manufacturing cost of the equipment. Increase the contact time between the water flow and the ion exchanger, and the incoming water forms a uniform columnar flow, which greatly reduces the disturbance of the water flow and ensures the stability of the resin layer; thereby improving the water quality of the effluent; the water outlet device uses a water outlet porous plate + water outlet cap + outlet baffle set The water device form can improve the quality of effluent water and the amount of periodic water production, prolong the service life of the ion exchanger in the equipment, and reduce the operating cost of the system.

附图说明Description of drawings

图1是本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;

图2是本实用新型的布水板的结构示意图。Fig. 2 is a schematic structural view of the water distribution plate of the present invention.

附图中的标记为:1-壳体、2-布水装置、3-出水装置、4-可拆卸挡水板、5-外围圈板、6-布水多孔板、7-布水水帽、8-支撑杆、9-挡水板吊杆、10-上部人孔、11-椭圆形内人孔板、12-出水多孔板、13-出水水帽、14-支撑柱、15-下部人孔、16-出水挡板、17-窥视镜。The marks in the drawings are: 1-housing, 2-water distribution device, 3-water outlet device, 4-removable water baffle, 5-peripheral ring plate, 6-water distribution porous plate, 7-water distribution cap , 8-support rod, 9-water retaining plate suspender, 10-upper manhole, 11-elliptic inner manhole plate, 12-outlet perforated plate, 13-outlet water cap, 14-support column, 15-lower manhole hole, 16-water outlet baffle, 17-peep mirror.

具体实施方式Detailed ways

下面结合附图和实施例对本实用新型作进一步的说明。Below in conjunction with accompanying drawing and embodiment the utility model is described further.

本实用新型的实施方式:一种核电二回路超大离子交换设备,结构如图1所示;包括壳体1、布水装置2和出水装置3,所述的壳体1主体为柱状结构,壳体1的直径为3200mm至4200mm,典型设计3400mm;柱体高度为2000mm至3500mm,典型设计2400mm。Embodiment of the present utility model: a super large ion exchange equipment for the secondary circuit of nuclear power, the structure is shown in Figure 1; it includes a housing 1, a water distribution device 2 and a water outlet device 3, the main body of the housing 1 is a columnar structure, and the housing The diameter of the body 1 is 3200mm to 4200mm, with a typical design of 3400mm; the height of the cylinder is 2000mm to 3500mm, with a typical design of 2400mm.

所述的壳体1由两个等径曲面封头和一个柱形筒体焊接而成。The shell 1 is welded by two isometric curved heads and a cylindrical barrel.

所述的布水装置2由可拆卸挡水板、外围圈板、布水多孔板、布水板上的布水水帽和支撑杆组成,可拆卸挡水板安装在设备本体封头进水口下方。The water distribution device 2 is composed of a detachable water baffle, a peripheral ring plate, a water distribution porous plate, a water distribution cap on the water distribution plate and a support rod, and the detachable water baffle is installed at the water inlet of the head of the equipment body below.

所述的布水多孔板6,结构如图2所示;一块圆形平板10开孔而成,含一组自带水帽的椭圆形内人孔板11安装其上,自带水帽的椭圆形内人孔板根据人孔直径调整,范围为长轴直径400mm至500mm,短轴直径400mm,典型设计长轴直径480mm,短轴直径400mm。The structure of the water distribution perforated plate 6 is as shown in Figure 2; a circular plate 10 is perforated and formed, and a group of oval inner manhole plates 11 with a water cap are installed on it, and a water cap with a water cap is installed on it. The elliptical inner manhole plate is adjusted according to the diameter of the manhole, ranging from 400mm to 500mm in the major axis diameter and 400mm in the minor axis diameter. The typical design major axis diameter is 480mm and the minor axis diameter is 400mm.

所述的壳体1的内壁与布水多孔板6连接为焊接方式,自带水帽的椭圆形内人孔板11为紧固件连接。The inner wall of the housing 1 is connected to the water distribution perforated plate 6 by welding, and the oval inner manhole plate 11 with its own water cap is connected by fasteners.

所述出水装置3由出水多孔板12、出水多孔板上出水水帽13、支撑柱14和出水挡板16组成,出水多孔板12和支撑柱14焊接而成,出水挡板16焊接在出水口上方。The water outlet device 3 is composed of a water outlet porous plate 12, a water outlet cap 13 on the water outlet porous plate, a support column 14 and a water outlet baffle 16. The water outlet porous plate 12 and the support column 14 are welded, and the water outlet baffle 16 is welded on the water outlet above.

所述出水装置3通过出水多孔板12与壳体1焊接。The water outlet device 3 is welded to the housing 1 through the water outlet perforated plate 12 .

壳体1开有上部人孔10、下部人孔15共两个人孔,孔径400mm至500mm;下部为出水装置3,为弧形板;The casing 1 is provided with two manholes, the upper manhole 10 and the lower manhole 15, with a diameter of 400mm to 500mm; the lower part is the water outlet device 3, which is an arc-shaped plate;

布水水帽7为圆柱型,间隙为0.4~1.0mm,高度从40~80mm,直径为50~90mm;The water distribution cap 7 is cylindrical, with a gap of 0.4-1.0 mm, a height of 40-80 mm, and a diameter of 50-90 mm;

出水水帽13为圆柱型,间隙为0.2~0.3mm,高度从40~80mm,直径为50~90mm;The outlet water cap 13 is cylindrical, with a gap of 0.2-0.3 mm, a height of 40-80 mm, and a diameter of 50-90 mm;

设备下方为出水口,规格为DN350mm;Below the equipment is the water outlet, the specification is DN350mm;

设备上、下部进、出脂口:DN50mm至DN150mm;The inlet and outlet of the upper and lower parts of the equipment: DN50mm to DN150mm;

在设备壳体部分设计有窥视镜DN100mm。DN为公称直径,mm为毫米。A peep mirror DN100mm is designed in the equipment housing part. DN is the nominal diameter, mm is millimeter.

Claims (5)

1. a nuclear power condensate polishing treatment strainer, is characterized in that comprising housing, water-distributing device and discharging device, and described housing is columnar structure, and the diameter of housing is 3200mm to 4200mm, and height of column is 2000mm to 3500mm; Described housing is welded by two isometrical head surfaces and a column-shaped barrel; Described water-distributing device is provided with water distribution water cap by dismountable water eliminator, peripheral girth sheets, support bar, water distribution porous plate, water distribution porous plate, support bar is connected between water distribution porous plate and end socket, and detachable water eliminator is arranged on below apparatus body end socket water-in.
2. nuclear power condensate polishing treatment strainer according to claim 1, it is characterized in that described water distribution porous plate is formed by one piece of circular flat-plate pore-opening, and be provided with one piece carry be uniformly distributed water cap ellipse in manhole plate be arranged in circular dull and stereotyped perforate.
3. nuclear power condensate polishing treatment strainer according to claim 1, is characterized in that the inwall of described housing and water distribution porous plate edge conjunction mode are welded construction.
4. nuclear power condensate polishing treatment strainer according to claim 1, it is characterized in that described discharging device forms by water outlet porous plate, water outlet porous plate being uniformly distributed water outlet water cap, pillar stiffener and water outlet baffle plate, pillar stiffener is connected between water outlet porous plate and end socket, water outlet porous plate and pillar stiffener are welded, and water outlet baffle plate is welded on above water outlet.
5. nuclear power condensate polishing treatment strainer according to claim 4, is characterized in that water outlet porous plate edge and the case weld of described discharging device.
CN201420618797.7U 2014-10-23 2014-10-23 A kind of nuclear power condensate polishing treatment strainer Expired - Lifetime CN204111377U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420618797.7U CN204111377U (en) 2014-10-23 2014-10-23 A kind of nuclear power condensate polishing treatment strainer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420618797.7U CN204111377U (en) 2014-10-23 2014-10-23 A kind of nuclear power condensate polishing treatment strainer

Publications (1)

Publication Number Publication Date
CN204111377U true CN204111377U (en) 2015-01-21

Family

ID=52328712

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420618797.7U Expired - Lifetime CN204111377U (en) 2014-10-23 2014-10-23 A kind of nuclear power condensate polishing treatment strainer

Country Status (1)

Country Link
CN (1) CN204111377U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106277184A (en) * 2015-05-12 2017-01-04 中广核工程有限公司 High flow rate is pressed ion-exchange unit
CN107240431A (en) * 2017-06-30 2017-10-10 青岛同兴环保设备有限公司 A kind of nuclear waste disposal filter screen
CN107684757A (en) * 2017-08-28 2018-02-13 宜兴市建华成套环保有限公司 A kind of double case gravity valveless filters

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106277184A (en) * 2015-05-12 2017-01-04 中广核工程有限公司 High flow rate is pressed ion-exchange unit
CN107240431A (en) * 2017-06-30 2017-10-10 青岛同兴环保设备有限公司 A kind of nuclear waste disposal filter screen
CN107684757A (en) * 2017-08-28 2018-02-13 宜兴市建华成套环保有限公司 A kind of double case gravity valveless filters

Similar Documents

Publication Publication Date Title
CN201037120Y (en) Condensation water refined processing high-speed mixing bed
CN204111377U (en) A kind of nuclear power condensate polishing treatment strainer
CN202983425U (en) Filter pipe used for high-temperature gas-solid separation and filter of filter pipe
CN104556266B (en) A kind of strengthening waterpower cavitation process device
CN204022554U (en) Internal-external double circulation anaerobic reactor
CN103785188A (en) Liquid flash separator
CN102001727A (en) Ion exchange equipment
CN207469205U (en) A kind of reciprocal flow pattern river suspended particulate substance collection device
CN207404937U (en) A kind of new UASB water distributors
CN205199479U (en) Air distributor reaches reactor including it
CN201353445Y (en) Spider web water distribution device
CN105971691A (en) Automobile exhaust filtering device
CN205241341U (en) Water distribution device with water distribution head
CN210117264U (en) A walnut shell filter with balanced water distribution function
CN103083978A (en) Recoil type pipeline filter
CN204173981U (en) A kind of circular UASB water-distributing device
CN107758830A (en) The reactor of dismountable wet oxidation processing waste water
CN101792188A (en) High flow-rate medium pressure resin bed
CN205760138U (en) Expanding-type dirt separator
CN203803197U (en) Large-diameter film laminating filter
CN207253827U (en) A kind of double flow rate water filtering cap
CN211552531U (en) High-efficient heat exchanger is used in base oil production
CN206184016U (en) Does whirl inlet tube structure reach tower tray formula flash distillation that contains it heat transfer integration equipment
JP5682418B2 (en) Desalter
CN112516656A (en) Front filter dome-shaped porous plate water outlet device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20150121