Molecular sieve ion exchange method and application thereof

A technology of ion exchange and cation exchange membrane, which is applied in the field of clean and low-cost ion exchange of molecular sieves, which can solve the problems of high cost, high energy consumption, and excessive ammonium nitrogen wastewater, so as to prolong the service life and reduce energy consumption , The effect of shortening downtime

Active Publication Date: 2014-05-07
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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  • Molecular sieve ion exchange method and application thereof
  • Molecular sieve ion exchange method and application thereof
  • Molecular sieve ion exchange method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0084] (1) Weigh 8kg ZSM-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.

[0085] (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 ammonia water with a concentration of 30% by weight, 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 ...

Embodiment 2

[0093] (1) Weigh 50kg Beta molecular sieve (Na 2 The O content is 1.32% by weight, and the relative crystallinity is 95%) is added to 650 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.

[0094] (2) Combine the obtained 500kg filtrate with 2500g Na 2 SO 4 Mix well, obtain the aqueous solution that contains ion, be that the pH value of this aqueous solution is adjusted to 11 after the ammoniacal liquor of 30% by weight with concentration and filter, the liquid phase that will obtain is sent in the salt room storage tank of bipolar membrane electrodialyzer, At the same time, respectively add 100kg deionized water in the alkali chamber storage tank and the acid chamber storage tank of the bipolar membrane electrodialyzer, add 2% by weight Na of 20kg in the electrode chamber storage tank 2 SO 4 of aqueous solution. Turn on th...

Embodiment 3

[0106] (1) Weigh 10kgMCM-22 molecular sieve (Na 2 The O content is 2.95% by weight, and the relative crystallinity is 97%) is added to 230 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.

[0107] (2) Mix the obtained 300kg filtrate with 3000g NaCl uniformly to obtain an aqueous solution containing ions, adjust the pH value of the aqueous solution to 12 with ammonia water with a concentration of 30% by weight, and then filter, and send the obtained liquid phase into the bipolar In the salt chamber storage tank of the membrane electrodialyzer, add 100kg of deionized water respectively in the alkali chamber storage tank and the acid chamber storage tank of the bipolar membrane electrodialyzer at the same time, add 30kg of 3% by weight NaOH in the electrode chamber storage tank of aqueous solution. Turn on the circulating pu...

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Abstract

The invention provides a molecular sieve ion exchange method. The method comprises the following steps: conducting bipolar membrane electrodialysis on an aqueous solution containing ions in a bipolar membrane dialyzer to obtain an acid liquid, wherein the bipolar membrane dialyzer comprises a positive electrode, a negative electrode, bipolar membranes, a cation exchange membrane and an anion exchange membrane, and the bipolar membranes, the cation exchange membrane and the anion exchange membrane are located between the positive electrode and the negative electrode, and the cation exchange membrane and the anion exchange membrane are in pairs to separate the bipolar membranes in pairs, enabling the molecular sieve containing a template agent to be in contact with the acid liquid to conduct ion exchange so as to obtain a molecular sieve slurry subjected to the iron exchange; conducting solid liquid separation on the t molecular sieve slurry subjected to the iron exchange to obtain a solid phase and liquid phase; regulating the pH of the liquid phase to be more than 8, then conducting solid liquid separation to obtain a processing liquid, and circulating the processing liquid to the bipolar membrane electrodialysis step to conduct bipolar membrane electrodialysis. The method reduces the power consumption of a bipolar membrane electrodialysis device, and acquires higher ion exchange efficiency. The invention further provides application of an alkaline liquid prepared by the method and used in the preparation of the molecular sieve.

Description

technical field [0001] The invention relates to a molecular sieve ion exchange method and its application, in particular to a clean and low-cost ion exchange method for molecular sieves and its application. 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 s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/04B01D61/44
Inventor 罗一斌刘中清周丽娜舒兴田
Owner CHINA PETROLEUM & CHEM CORP
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