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D301FC macroporous anion exchange resin

NegotiableUpdate on 05/06
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Overview

D301FC macroporous anion exchange resin wastewater decolorization resin uses saturated saline solution, which is approximately twice the volume of the treated resin. Soak the resin in a saline solution for 18-20 hours, then drain the saline solution and rinse with clean water to ensure that the discharged water does not turn yellow; Next, use a 2% -4% NaOH solution with the same amount as above, soak in it for 2-4 hours (or clean with a small flow rate), drain the alkaline solution, and rinse the resin until the discharged water is close to neutral; Afterwards, use a 5% HCl solution with the same amount as above, soak for 4-8 hours, drain the acid solution, and drift with clean water until neutral for later use

Product Details

Professional 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
After grinding, the percentage of spherical particles is ≥ ..95
Transformation expansion rate% ≤ 35.3535
Resin appearance: milky white or light yellow opaque spherical particles
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 anion exchange resin wastewater decolorization resin
1. Ion exchange resin contains a certain amount of moisture and should not be stored outdoors. During storage and transportation, it should be kept moist to avoid air drying and dehydration, which may cause the resin to break. If the resin is dehydrated during storage, it should be soaked in concentrated saline water (10%) first and gradually diluted. It should not be directly placed in water to avoid rapid swelling and breakage of the resin.
2. In winter storage and transportation, it is necessary to maintain a temperature environment of 5-40 ℃ to avoid overcooling or overheating, which may affect quality. If there is no insulation equipment in winter, the resin can be stored in salt water, and the concentration of salt water can be determined according to the temperature.
3. In industrial products of ion exchange resins, there are often a few low polymers and monomers that have not participated in the reaction, as well as inorganic impurities such as iron, lead, copper, etc. When the resin comes into contact with water, acid, alkali or other solutions, the above substances will be transferred into the solution, affecting the quality of the effluent. Therefore, it is necessary to pre treat the new resin before use. Generally, water is used to make the resin fully swollen. Then, the inorganic impurities (mainly iron compounds) in between can be removed with 4-5% dilute hydrochloric acid, and the organic impurities can be removed with 2-4% dilute * solution, washed to near neutrality. If used in pharmaceutical preparation, it must be soaked in ethanol for treatment.
4. In the application of resins, it is necessary to avoid contact with metal (such as iron, copper, etc.) oil stains, organic molecular microorganisms, strong oxidants, etc., in order to prevent ion exchange from decreasing or even losing function. Therefore, the resin needs to be activated irregularly according to the situation. The activation method can be determined according to the pollution situation and conditions. Generally, cation resins are prone to Fe pollution during softening and can be soaked in hydrochloric acid and gradually diluted. Anion resins are prone to organic pollution and can be soaked or rinsed in a mixed solution of 10% NaCl+2-5% NaOH. If necessary, 1% hydrogen peroxide solution can be soaked for a few minutes. Other methods can also be used, such as acid-base replacement treatment, bleaching treatment, alcohol treatment, and various other methods.
5. Pre treatment of new resins: Industrial products of ion exchange resins often contain a small number of oligomers and monomers that have not participated in the reaction, as well as inorganic impurities such as iron, lead, and copper. When resin comes into contact with water, acid, alkali, or other solutions, these substances will transfer into the solution, affecting the quality of the effluent. Therefore, it is necessary to pre treat the new resin before use. Generally, the resin is first swollen with water, and then the inorganic impurities (mainly iron compounds) in between can be removed with 4-5% dilute hydrochloric acid. Organic impurities can be removed with 2-4% dilute * solution and washed until near neutrality.
The purification method of graphene oxide includes the following steps: ion exchange purification: sequentially passing the graphene oxide solution through cation exchange resin and anion exchange resin; The cation exchange resin is a hydrogen type cation exchange resin, and the anion exchange resin is a hydroxide type anion exchange resin. The purification method provided by the present invention has the advantages of simple operation and high purification efficiency. The content of each metal impurity in the purified graphene oxide is less than 10ppm; In addition, the used ion exchange resin can be reused through regeneration, which is energy-saving and environmentally friendly.