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D301FC macroporous weakly basic anion exchange resin news report

NegotiableUpdate on 05/06
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Overview

D301FC macroporous weakly basic anion exchange resin news report: The new resin often contains solvents, substances that have not participated in polymerization reactions, and a small amount of low polymer, and may also adsorb heavy metal ions such as iron, aluminum, and copper. When the resin comes into contact with water, acid, alkali, or other solutions, the soluble impurities mentioned above will be transferred into the solution, contaminating the effluent quality in the early stages of use. So, the new resin needs to be pre treated before being put into operation.

Product Details

D301FC macroporous weakly basic anion exchange resin news reportProfessional production: anion and cation exchange resin, macroporous adsorption resin, softened water resin, mixed bed MB resin, 18 megaohm ultra pure water polishing resin, wire cutting slow wire resin, sewage decolorization resin, electroplating wastewater nickel and chromium removal resin, iron, copper, phosphorus, boron, and heavy metal removal resin, acid recovery resin, chelating resin, food grade resin, alum extraction resin, gold absorption resin, silver extraction resin, strong acid, strong alkali, weak acid, weak alkali. There are dozens of models in four categories: 001 x7、001x8、732、717、201x7、201x4、D001、D201、D301、D113、D101、H103、D403、D408 wait


One Product Name: D301 Large Pore Weakly Basic Styrene Anion Exchange Resin Supply

Detailed information:

2、 Corresponding foreign brands

United States: Amberlite IRA-93; Germany: LewaitMP-60 Japan: DiaionWA-30

3、 Execution standard: DL519-93 SH2605.09-1997 HG/T2165-91 Q/JH 105-2002

四、理化性能.

indicator name

D301

Full exchange capacity mmol/g ≥

4.8

Strong functional group capacity mmol/g ≥

1.0

Volume exchange capacity mmol/ml ≥

1.4

Moisture content%

48-58

Wet visual density g/ml

0.65-0.72

Wet true density g/ml

1.03-1.06

Particle size%

(0.315-1.25mm)≥95

Effective particle size mm

0.40-0.70

≥0.5

0.35-0.50

Uniformity coefficient ≤

1.60

..1.60

1.40

Grinding ball rate% ≥

...95

Transformation expansion rate% ≤

35

.35

35

Resin appearance

Milky white or light yellow opaque spherical particles

Factory type free amine

Factory type: free amine type. Appearance: Milky white or light yellow opaque spherical particles. ......

5、 Operational reference indicators ..

1. PH range: 1-9

2. Operating temperature: OH type 40 ℃ Cl type 100 ℃ ...

3. Industrial resin layer height: 1.0-3.0m

4. Regeneration solution concentration: NaOH 2-4%

5. Regeneration solution dosage: (by calculation)

NaOH (industrial) 40-70 Kg/m3

6. Flow rate of regeneration solution: 4-6 m/h

7. Regeneration contact time: 30-50 minutes

8. Flow rate for washing: 15-25 m/h

9. Washing time: about 30 minutes

10. Operating flow rate: 15-25 m/h

11. Work exchange capacity: ≥ 1000mol/m3

6、 Usage: Mainly used for the preparation of pure water and high-purity water, used as a pre bed or double bed in combination with strong alkali anion resin, which can significantly improve the economic efficiency of operation. This product is also used for the treatment and recycling of electroplating and chromium containing wastewater.






D301FC macroporous weakly basic anion exchange resin news report

During the use of resin particles, there are changes such as transfer, friction, expansion, and contraction. After long-term use, there will be a small amount of loss and breakage, so the resin should have high mechanical strength and wear resistance. Generally, resins with low cross-linking are more prone to breakage, but the durability of the resin is mainly determined by the uniformity and strength of the cross-linking structure. Such as macroporous resin, those with high crosslinking degree have stable structure and can withstand repeated regeneration.
This article describes the method of preparing macroporous cation exchange resin. The macroporous cation exchange resin is in the form of particles (such as beads), which contain hydrophilic, cross-linked (methyl) acrylic polymer materials. In addition, the present invention describes a method for purifying positively charged materials using the macroporous cation exchange resin, a method for preparing a chromatographic column comprising the macroporous cation exchange resin, a method for preparing a filter element comprising the macroporous cation exchange resin, and a method for preparing a porous composite material comprising the macroporous cation exchange resin