A kind of molecular sieve ion exchange method

A technology of ion exchange and molecular sieve, which is applied in the field of clean and low-cost ion exchange of molecular sieves, can solve the problems of excessive ammonium nitrogen wastewater, complicated operation, low efficiency, etc., and achieve reduced overall energy consumption, high ion exchange efficiency, The effect of reducing the number of times

Active Publication Date: 2015-10-28
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the common problem with the ammonium exchange method is that the raw molecular sieve powder needs to be exchanged with ammonium to produce NH 4 Type molecular sieves can be transformed into hydrogen type molecular sieves by roasting again. However, due to the limitation of chemical balance, NH 4 + Cannot completely replace Na at one time + , to get low Na 2 Molecular sieve with O content, the ammonium exchange process needs to be repeated many times, resulting in a large amount of ammonium nitrogen waste water exceeding the standard
In order to meet the national standard that the discharge of ammonium nitrogen is less than 15mg / L, wastewater needs to be treated, but the process of treating the wastewater not only consumes a lot of energy but also costs a lot
In addition, the conventional ammonium ion exchange method needs to repeatedly adjust the acidity and alkalinity of the environment, the operation is complicated and the efficiency is low

Method used

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  • A kind of molecular sieve ion exchange method
  • A kind of molecular sieve ion exchange method
  • A kind of molecular sieve ion exchange method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0079] (1) Weigh 10kg REUSY molecular sieve (Na 2 The O content is 4.96% by weight, and the relative crystallinity is 58%) is added into 130 kg of deionized water, and stirred evenly to obtain a slurry. The slurry is filtered to obtain a filtrate and a filter cake, and the weight ratio of molecular sieve to water in the filter cake is 1:3.

[0080] (2) Combine the obtained 100kg filtrate with 800g Na 2 SO 4 Mix evenly to obtain an ion-containing aqueous solution, adjust the pH value of the aqueous solution to 12.5 with a concentration of 17% by weight ammonia water, and then carry out solid-liquid separation, and send the obtained liquid phase into the salt chamber storage tank of the bipolar membrane electrodialyzer At the same time, 50kg of deionized water was added to the acid chamber storage tank and the alkali chamber storage tank of the bipolar membrane electrodialyzer at the same time, and 20kg of 2% by weight Na was added to the electrode chamber storage tank. 2 SO ...

Embodiment 2

[0096] (1) Weigh 10kgNaY molecular sieve (NaY 2 The O content is 13.0% by weight, and the relative crystallinity is 85%) is added into 80 kg of deionized water, and stirred evenly to obtain a slurry. The slurry is filtered to obtain a filtrate and a filter cake, wherein the weight ratio of molecular sieve to water in the filter cake is 1:3.

[0097] (2) Combine the obtained 50kg filtrate with 200g Na 2 SO 4 Mix evenly to obtain an ion-containing aqueous solution, adjust the pH value of the aqueous solution to 9 with a concentration of 20% by weight ammonia water, and then carry out solid-liquid separation, and send the obtained liquid phase into the salt chamber storage tank of the bipolar membrane electrodialyzer At the same time, 80kg of deionized water was added to the acid chamber storage tank and the alkali chamber storage tank of the bipolar membrane electrodialyzer at the same time, and 20kg of 3% by weight Na was added to the electrode chamber storage tank. 2 SO 4 ...

Embodiment 3

[0104] (1) Weigh 8kgZSM-5 molecular sieve (Na 2 The O content is 1.2% by weight, and the relative crystallinity is 95%) is added into 100 kg of deionized water, and stirred evenly to obtain a slurry. The slurry is filtered to obtain a filtrate and a filter cake, and the weight ratio of molecular sieve to water in the filter cake is 1:3.

[0105] (2) Combine the obtained 76kg filtrate with 500g Na 2 SO 4 Mix evenly to obtain an ion-containing aqueous solution, adjust the pH value of the aqueous solution to 12 with a concentration of 30% by weight ammonia water, and then carry out solid-liquid separation, and send the obtained liquid phase into the salt chamber storage tank of the bipolar membrane electrodialyzer At the same time, 50kg of deionized water was added to the alkali chamber storage tank and the acid chamber storage tank of the bipolar membrane electrodialyzer at the same time, and 20kg of 3% by weight Na was added to the electrode chamber storage tank. 2 SO 4 of ...

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Abstract

The invention provides a molecular sieve ion exchange method. The method comprises the following steps: a bipolar membrane electrodialysis step comprising conducting bipolar membrane electrodialysis on an aqueous solution containing ions to obtain an acid liquid; an ion exchange step comprising enabling a molecular sieve and the acid liquid to be in contact with each other to implement ion exchange so as to obtain a molecular sieve slurry subjected to the iron exchange; a solid liquid separation step comprising conducting the solid liquid separation on the molecular sieve slurry subjected to the iron exchange to obtain a liquid phase and a solid phase, and conducting solid liquid separation after the pH of the liquid phase is regulated to be more than 8 to obtain a processing liquid; a step of circulating the processing liquid to the bipolar membrane electrodialysis step to replace at least part of the aqueous solution containing ions, and then conducting bipolar membrane electrodialysis to obtain an alkaline liquid and an acid liquid. In the method provided by the invention, the power consumption of the bipolar membrane electrodialysis step is low. In addition, the method can acquire higher ion exchange efficiency.

Description

technical field [0001] The invention relates to a molecular sieve ion exchange method, in particular to a clean and low-cost ion exchange method for molecular sieves. Background technique [0002] According to the data of the Ministry of Water Resources in 2005, 78% of the river sections flowing through cities in the country are no longer suitable for drinking water sources, and 50% of urban groundwater is polluted. Water pollution will not only directly affect industrial and agricultural production, but also cause serious harm to human health. In order to achieve the sustainable development of the country and the harmonious coexistence between man and nature, the country has formulated the national standard GB8978-1996 for industrial sewage discharge, which stipulates that the primary discharge standard of ammonium nitrogen in the petrochemical industry is 15mg / L, and the secondary discharge standard is 50mg / L. [0003] Molecular sieves have structural characteristics su...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/02
Inventor 周丽娜刘中清罗一斌舒兴田
Owner CHINA PETROLEUM & CHEM CORP
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