CN203200058U - Swirl ion exchanger - Google Patents
Swirl ion exchanger Download PDFInfo
- Publication number
- CN203200058U CN203200058U CN 201320214487 CN201320214487U CN203200058U CN 203200058 U CN203200058 U CN 203200058U CN 201320214487 CN201320214487 CN 201320214487 CN 201320214487 U CN201320214487 U CN 201320214487U CN 203200058 U CN203200058 U CN 203200058U
- Authority
- CN
- China
- Prior art keywords
- resin
- water
- ion
- exchanger
- ion exchanger
- 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 - Fee Related
Links
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model relates to a swirl ion exchanger. An inlet of filtering raw water is an inlet of the ion exchanger, and an outlet at the other end is located in a chamber at the bottom in the ion exchanger; a flow guide pore plate is fixed on the tank wall at the upper part of the chamber; a filtering pore plate is arranged at the upper part of the flow guide pore plate; the upper part of the filtering pore plate is filled with a resin layer; a flow guide spiral channel is formed in a tank body; a water outlet pipe is communicated with the tank body and fixed at the upper part of the tank body; an outlet filter screen is arranged at a water inlet of the water outlet pipe; the ion exchanger fills resin through a filling port and performs the resin discharge work through a resin discharge port; and a water outlet is an external discharge port which is only used for discharging redundant water in the exchanger when the ion exchanger adds resin. According to the swirl ion exchanger provided by the utility model, through the flow guide pore plate and the flow guide spiral channel, the filtering medium entering the resin layer passes through always in a selection and remaining state, thus the path of the filtering medium is prolonged, the contact time is increased, and the resin layer is indirectly heightened.
Description
Technical field: the utility model relates to a kind of cyclone-type ion-exchanger.
Background technology
In order to remove the impurity of water intermediate ion attitude, most methods that adopt are ion exchange techniques now.This method can must be more thorough with the Impurity removal of water intermediate ion attitude, thereby can make very pure water, so in the place that power station and related production need to be used pure water, it is an indispensable step of necessity.Ion-exchange in operational process, successively exchange with the displacement state under carry out, and lost efficacy layer and protective layer are the chemical reaction that ion-exchange can not occur again in operational process.Therefore, the factor that affects ion-exchange operation also affects work period, the utilization ratio of resin in ion-exchange and the economical operation of whole ion exchange system of resin in the ion exchange system.Concerning ion exchange system, some factor is fixed, as use the performance (comprising the own quality of its particle diameter, exchange capacity, selectivity and product etc.) of resin, the structure of interchanger and the height of resin layer, other factors then be change in the operational process such as operation flow velocity, influent quality, water temperature etc.The resin layer height is one of important factor that affects ion-exchanger operation and regeneration.The resin layer effect of altitude utilization ratio and the operating capacity of resin.Resin layer divides can be divided into lost efficacy layer, working lining and protective layer.Working lining is thicker, and its occupied ratio in total floor height is just larger.When reaching the inefficacy terminal point, the exchange capacity of unemployed resin is larger in the interchanger, and average inefficacy degree and the operating capacity of resin also decrease.Suitable increase resin layer height is conducive to improve the exchange capacity of effluent quality and resin work for this reason.Along with the height increase of resin layer, flow resistance and power consumption also can increase considerably but simultaneously.
The operation flow velocity also is one of important factor that affects the ion-exchanger operation.The flow velocity of water affects the carrying out of ion exchange reaction from two aspects, wherein be the mass transfer velocity that the water intermediate ion penetrates the outer liquid film of resin, and another one is the reaction times of ion and resin.In flow process, because the ion content in the solution is low, the principal element that determines permutoid reaction is the speed of film diffusion.Flow velocity is low, and the time of the outer liquid film thickening of resin ion penetration liquid film increases, and affects exchange velocity, is unfavorable for the carrying out of permutoid reaction.Although too high operation flow velocity is thinning of liquid film, has shortened the duration of contact of water and resin, it is incomplete that permutoid reaction is carried out, and can cause the reduction of effluent quality deterioration and resin operating capacity.The operation flow velocity is crossed the low phenomenon that easily causes current that bias current occurs in the cross section of resin layer, affects the performance of the exchange capacity of resin, because partial penetration causes effluent quality to worsen and operating capacity reduces.Too high flow velocity can cause the increase of flow resistance, has increased the breakage rate of power consumption and resin.
Present stage, the ion-exchanger equipment of main flow mainly was divided into fixed bed and floating bed, because the use of the innovation fixed bed of technology being replaced gradually by floating bed slowly, although floating bed have the fast stable effluent quality of flow velocity operating performance its still have certain defect.Do not cause such as the resin utilization ratio is high that whole exchange capacity is low, the cycle of operation is short, water production in periodic mode is regenerated the problems such as comparatively high consumption less.
Summary of the invention: the purpose of this utility model provides a kind of usage quantity of saving regenerator, prolongs the cyclone-type ion-exchanger of the regeneration period of deionization equipment.The technical solution of the utility model is: a kind of cyclone-type ion-exchanger, the entrance that filters former water is ion-exchanger entrance (1), the other end outlet is arranged in the chamber (2) of parallel operation bottom, fixing water conservancy diversion orifice plate (4) on the tank skin on chamber (2) top, water conservancy diversion orifice plate (4) top is orifice filter (5), resin layer (6) is loaded on orifice filter (5) top, water conservancy diversion helical channel (3) is installed in tank body, rising pipe (9) is communicated with tank body and is fixed on tank body top, rising pipe (9) water-in is with outlet filter screen (8), ion-exchanger is loaded resin by filler (12), carry out resin discharging and draw off work by unloading resin mouth (11), water port (10) is discharged the outside drain mouth that superfluous water is Appointments should be governeded by qualifications in the interchanger for ion-exchanger when adding resin.
The utility model water conservancy diversion orifice plate and water conservancy diversion helical channel make the filtration medium that enters resin layer keep passing through of the state of selecting and remain always, prolong the path that filtration medium is passed by thereby reach, and increase duration of contact and the covert resin layer height that increases.
The utility model principle is as follows:
Filtration medium enters in the interchanger by ion-exchanger entrance 1, at chamber 2 interior formation water subfills, enters water conservancy diversion orifice plate 4 and forms eddy flow.Enter resin layer 6 through orifice filter 5, filtration medium still continues to guarantee that by the water conservancy diversion helical channel 3 on the tank skin filtration medium remains attitude with eddy flow by resin layer, until water outlet is crossed until flow out ion exchange systems from ion-exchanger outlet 9 from outlet filter screen logical 8 by resin layer the time.
By the water (flow) direction that enters ion-exchanger is carried out water conservancy diversion, change its intrinsic flow direction, make water enter resin layer in the mode of eddy flow.Like this in same flow rate regime, enter resin layer in the mode of eddy flow, prolong the distance that water passes by from resin layer and the time lengthening that water is contacted with resin layer.Thereby improve the effective rate of utilization of level resin layer, be that the use of ion-exchanger is more economical, more efficient.
Description of drawings:
Fig. 1 the utility model structural representation
Embodiment:
The utility model as shown in Figure 1 is a kind of cyclone-type ion-exchanger, the entrance that filters former water is ion-exchanger entrance 1, the other end outlet is arranged in the chamber 2 of parallel operation bottom, fixing water conservancy diversion orifice plate 4 on the tank skin on chamber 2 tops, water conservancy diversion orifice plate 4 tops are orifice filter 5, resin layer 6 is loaded on orifice filter 5 tops, water conservancy diversion helical channel 3 is installed in tank body, rising pipe 9 is communicated with tank body and is fixed on tank body top, rising pipe 9 water-ins are with outlet filter screen 8, ion-exchanger is loaded resin by filler 12, carry out resin discharging and draw off work by unloading resin mouth 11, water port 10 is discharged the outside drain mouth that superfluous water is Appointments should be governeded by qualifications in the interchanger for ion-exchanger when adding resin.
The whirlwind-type ion-exchanger is a kind of design concept that is different from original conventional ion switching equipment structure.Operate by the flow direction to the filtration medium that enters ion-exchange unit, the operating path of filtration medium in ion-exchange unit prolonged, prolonged the duration of contact of itself and ion exchange resin, allow finally resin operating capacity in the ion-exchanger increases, the utilization ratio of resin promotes.Thereby can more save the usage quantity of regenerator and the regeneration period of prolongation deionization equipment, the economy of ion-exchange unit is further promoted.
Claims (1)
1. cyclone-type ion-exchanger, it is characterized in that: the entrance that filters former water is ion-exchanger entrance (1), the other end outlet is arranged in the chamber (2) of parallel operation bottom, fixing water conservancy diversion orifice plate (4) on the tank skin on chamber (2) top, water conservancy diversion orifice plate (4) top is orifice filter (5), resin layer (6) is loaded on orifice filter (5) top, water conservancy diversion helical channel (3) is installed in tank body, rising pipe (9) is communicated with tank body and is fixed on tank body top, rising pipe (9) water-in is with outlet filter screen (8), ion-exchanger is loaded resin by filler (12), carry out resin discharging and draw off work by unloading resin mouth (11), water port (10) is discharged the outside drain mouth that superfluous water is Appointments should be governeded by qualifications in the interchanger for ion-exchanger when adding resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320214487 CN203200058U (en) | 2013-04-25 | 2013-04-25 | Swirl ion exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320214487 CN203200058U (en) | 2013-04-25 | 2013-04-25 | Swirl ion exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203200058U true CN203200058U (en) | 2013-09-18 |
Family
ID=49144188
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320214487 Expired - Fee Related CN203200058U (en) | 2013-04-25 | 2013-04-25 | Swirl ion exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203200058U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103193293A (en) * | 2013-04-25 | 2013-07-10 | 高朋云 | Rotational flow type ion exchanger |
-
2013
- 2013-04-25 CN CN 201320214487 patent/CN203200058U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103193293A (en) * | 2013-04-25 | 2013-07-10 | 高朋云 | Rotational flow type ion exchanger |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204198512U (en) | Tertiary filter | |
| CN104003478A (en) | Extracorporeal upflow regeneration process for ion exchange resin | |
| CN203200058U (en) | Swirl ion exchanger | |
| CN103193293A (en) | Rotational flow type ion exchanger | |
| CN103127753A (en) | Quick sand filter | |
| CN202164187U (en) | Device for recycling electroplating rinsing water | |
| CN102225788B (en) | Magnetic-acoustic field synergistically enhanced sponge iron water deoxygenizing component | |
| CN203508043U (en) | Ion exchange unit | |
| CN104003477A (en) | External regeneration reverse-flow ion exchange system and application method thereof | |
| JP5672333B2 (en) | Operation method of regenerative ion exchanger | |
| CN203123981U (en) | Ion exchange device | |
| CN203174060U (en) | Integrated oil-gas field natural gas desulfurization device | |
| CN104415585A (en) | Filter for chemical industry | |
| CN102615367A (en) | Wire cutting water tank with filtering system | |
| CN210522001U (en) | Integrated high-efficiency water purifying equipment | |
| CN202700369U (en) | Dynamic separation device for cyclohexanone ammoximation catalysts | |
| CN103058315B (en) | Tower-type adsorption reactor and system and method thereof for removing heavy metal ions in water | |
| CN201823399U (en) | Cooling liquid solid particle purifying device for numerical-control boring miller or machining center | |
| CN204325021U (en) | Dyeing and printing sewage treatment unit | |
| CN201304336Y (en) | Countercurrent regeneration controller of fixed bed ion exchanger | |
| CN205473036U (en) | Circulating industrial waste water purifier | |
| CN203123639U (en) | Active sand filtering tank | |
| CN204125210U (en) | A kind of integrated water supply disc tube reverse osmosis (dt-ro) device | |
| CN203803337U (en) | Improved desulfurizing and absorbing tower of demister flushing water system | |
| CN103432785B (en) | Lateral flow rapid filter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200925 Address after: 150025 Heilongjiang Harbin Limin Development Zone Nanjing Road South, Shenyang Avenue East metropolis new phase 1, building B2 1-4 floor 106. Patentee after: Harbin Antai Lida Technology Development Co.,Ltd. Address before: Yilan County, Yu Gong Xiang Yong Quan Cun, Harbin city Heilongjiang province 154800 Cong Jia Tun Patentee before: Gao Pengyun |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130918 Termination date: 20210425 |