Method for predicting particulate breakthrough time for non-regenerative ion exchange resin device and method for managing non-regenerative ion exchange resin device
An ion exchange resin, breakthrough time technology, applied in ion exchange water/sewage treatment, measurement device, non-polluting water treatment, etc., can solve the problem of difficult ion exchange capacity, and achieve the effect of preventing leakage
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
no. 1 approach
[0038]
[0039] figure 1 An ultrapure water production device to which the method for predicting the particle breakthrough time of the non-regenerative ion exchange resin device in this embodiment can be applied is shown. exist figure 1 Among them, the ultrapure water manufacturing device 1 is an ultrapure water manufacturing device 1 composed of a pretreatment system 2, a primary pure water device 3 and a secondary pure water device (subsystem) 4 for processing primary pure water. Water, tap water, well water, etc.) W is used for manufacture.
[0040]Suspended substances or colloidal substances in the raw water W are removed in the pretreatment system 2 composed of coagulation, pressurized flotation (sedimentation), filtration (membrane filtration) devices, and the like. In addition, high-molecular organic substances, hydrophobic organic substances, and the like can be removed in this process.
[0041] The primary pure water manufacturing device 3 is equipped with a firs...
no. 2 approach
[0066] Next, a method of predicting the particle breakthrough time of the non-regenerative ion exchange resin device according to the second embodiment of the present invention will be described.
[0067] In the aforementioned first embodiment, the small resin column is installed in parallel with the non-regenerative ion exchange resin 25, but this embodiment is a method of installing the small resin column independently of the non-regenerative ion exchange resin 25 and performing an accelerated test. .
[0068] In this embodiment, the same device as that in the first embodiment described above can be applied as the ultrapure water production device. In addition, the same device can also be applied to the non-regenerative ion exchange resin device 25 which is the object of predicting the breakthrough time of fine particles. In addition, the same column can also be used as a small resin column.
[0069]
[0070] A method of predicting the breakthrough time of fine particles i...
Embodiment 1
[0084] exist figure 1 In the ultrapure water production apparatus shown, in order to predict the breakthrough time of the non-regenerative ion exchange resin 25, an accelerated test was performed with one small resin column.
[0085]
[0087] Resin layer height: 1000mm.
[0088] Water SV: 39 / h.
[0089] Water LV: 39m / h.
[0090] The number of particles in the treated water (feed water): about 100 / mL (>0.05μm).
[0091]
[0093] Resin layer height: 500mm.
[0094] Water SV: 78 / h.
[0095] Water LV: 39m / h.
[0096] The number of particles in the simulated treated water: about 3000 / mL (>0.05μm).
[0097] The simulated water to be treated was passed through the small resin column, and the results of continuous measurement of the number of treated water particles in the small resin column are shown in Figure 4 . In addition, when the number of particles in the treated water is more than 1% (≥ about 30 par...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


