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A kind of ion exchange method

A technology of ion exchange and ion exchange column, which is applied in the field of ion exchange of solid substances containing exchangeable groups by ion exchange column, can solve the problems that the process cannot be completed at one time, large industrial waste water, etc., and reduce the cost of washing and regeneration frequency, reduce the frequency of clogging, and prolong the effect of the service life

Active Publication Date: 2016-08-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The existing molecular sieve desodination method is usually to exchange the sodium ion in the molecular sieve into NH with ammonium salt solution first. 4 + , and then roasted at high temperature, the NH 4 + Convert to H + , of course this process cannot be completed at one time, in order to get Na + Molecular sieve with low content, the ammonium exchange process needs to be repeated many times
This existing exchange method will produce a large amount of industrial wastewater, and among all the acidic ammonium-containing wastewater in the catalyst plant, the highest concentration of ammonia nitrogen is the exchange liquid and initial washing water produced by the molecular sieve ammonium exchange process, and its ammonia nitrogen content is higher than that of other ammonium-containing wastewater. More than several times of waste water (such as secondary washing water, tertiary washing water)

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0069] (1) 240 mL of ammonium-type styrene-based strongly acidic magnetic ion-exchange resin (commercially purchased from Nankai University Chemical Plant, with iron particles as the magnetic core, the content of which is 10% by weight, was loaded into a reactor with an inner diameter of 40 mm, The volume average particle diameter of the ion exchange resin was 720 μm, and the total exchange capacity was 1.8 mmol / mL), and an ion exchange column was obtained.

[0070] Three layers (6 per layer) of inductance coils are evenly arranged along the height direction of the ion exchange column. The inner diameter of each inductance coil is 40mm, the outer diameter is 65mm, the height is 70mm, and the number of turns is 370. The 6 inductance coils in each layer The coils are evenly arranged along the outer circumference of the ion exchange column, wherein the axis of the inductance coil is perpendicular to the axis of the ion exchange column, and the inductance coil is connected to a thr...

Embodiment 2

[0083] Adopt the same method as embodiment 1 to carry out ion exchange, the difference is that a glass tube (inner diameter is 10mm, length is 20mm, outer diameter is 12mm, and this glass tube is the same as ion exchange column) is arranged above the ion exchange resin bed layer. shaft, the distance between the lower end surface of the glass tube and the upper surface of the ion exchange resin bed is 5mm), and air is introduced into the glass tube through the gas channel at a gas inlet speed of 30mL / min, and then the slurry containing molecular sieve Pumped into the ion exchange column for ion exchange.

[0084] The sodium oxide content of each obtained molecular sieve sample is listed in Table 1. After the ion exchange, no deposited ion exchange resin was observed on the upper surface of the ion exchange resin bed in the ion exchange column, and the mass change rate of the solid matter in the ion exchange column before and after ion exchange was 4.9%.

Embodiment 3

[0086] Ion exchange was carried out in the same manner as in Example 1, except that 1 g of NaCl was added to the dispersion as an ion exchange initiator.

[0087] The sodium oxide content of each obtained molecular sieve sample is listed in Table 1. After the ion exchange, the thickness of the molecular sieve deposited on the upper surface of the ion exchange resin bed in the ion exchange column was 1mm, and the mass change rate of the solid matter in the ion exchange column before and after ion exchange was 5.1%.

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Abstract

The invention provides an ion exchange method. According to the method, a slurry comprising a solid substance with exchangeable groups flows through an ion exchange column filled with an ion exchange resin bed layer, such that the exchangeable groups in the solid substance is subjected to ion exchange with ion exchange groups in the ion exchange resin in the ion exchange resin bed layer; and solid-substance-containing slurry flowing out from the ion exchange column is collected. At least part of the ion exchange resin is magnetic ion exchange resin. Also, when the slurry flows through the ion exchange column, the ion exchange column is positioned in a transversal rotation magnetic field. With the method provided by the invention, after ion exchange, no or substantially no molecular sieve is adhered to the surface of the ion exchange resin, such that ion exchange column service period can be effectively prolonged, and washing and regeneration frequencies can be reduced. Under a same condition of ion exchange, with the method provided by the invention, higher ion exchange efficiency can be achieved.

Description

technical field [0001] The invention relates to an ion exchange method, more specifically, relates to a method for ion exchange of solid substances containing exchangeable groups by using an ion exchange column. Background technique [0002] Molecular sieves are widely used in the field of petrochemical industry. At present, the methods of industrially synthesizing molecular sieves are all in alkaline solution, so the synthesized molecular sieves are all sodium type. The largest catalyst in the oil refining industry is catalytic cracking catalyst, which mostly uses Y-type molecular sieve as the active component. When Y-type molecular sieve is artificially synthesized, it is in the stable NaY form. The sodium ion completely neutralizes the negative charge center in the zeolite molecular sieve, resulting in Sodium molecular sieves do not have acid centers. Therefore, sodium molecular sieves have almost no activity in the carbon ion reaction. If they are used as catalytic crac...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J47/06C01B39/02B01J29/04
CPCB01J47/06
Inventor 张翊刘中清罗一斌宗保宁
Owner CHINA PETROLEUM & CHEM CORP
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