A method of ion-exchanging solid substances containing exchangeable ions

A technology of ion exchange and solid matter, applied in the field of ion exchange, can solve the problems of excessive ammonium nitrogen wastewater, complicated operation, low efficiency, etc., and achieve the effects of reducing overall energy consumption, high ion exchange efficiency, and reducing the number of times

Active Publication Date: 2016-05-25
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 of the ammonium exchange method is that the original powder of the molecular sieve needs to be exchanged with ammonium to make an NH4 molecular sieve, and then roasted to convert it into a hydrogen molecular sieve. However, due to the limitation of the chemical balance, NH4+ cannot completely replace the 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 method of ion-exchanging solid substances containing exchangeable ions
  • A method of ion-exchanging solid substances containing exchangeable ions
  • A method of ion-exchanging solid substances containing exchangeable ions

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 800gNa 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 200gNa 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 o...

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 500gNa 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 a...

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Abstract

The invention provides an ion exchange method for a solid substance with exchangeable ions, which includes the following steps: bipolar membrane electrodialysis: performing bipolar membrane electrodialysis to a water solution with ions, so as to obtain an acid liquor; ion exchange: performing ion exchanging to the contacted solid substance with exchangeable ions and the acid liquor, wherein ions capable of forming a water insoluble substance with OH<-> are contained in the exchangeable ions in the solid substance; solid-liquid separation: performing solid-liquid separation to slurry of the solid substance subjected to ion exchange, so as to obtain the solid phase and the liquid phase; performing solid-liquid separation after the pH value of the liquid phase is adjusted above 8 and obtaining a conditioning fluid; circulating the conditioning fluid to the step of bipolar membrane electrodialysis, substituting at least part of the water solution with ions with the conditioning fluid for bipolar membrane electrodialysis. In the method provided by the invention, power consumption for bipolar membrane electrodialysis is low, and higher ion exchange efficiency is obtained through the method.

Description

technical field [0001] The invention relates to a method for performing ion exchange on a solid substance containing exchangeable ions, in particular to a method for performing ion exchange on a solid substance containing exchangeable ions in a clean and low-cost manner. 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 th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D61/44
Inventor 刘中清周丽娜罗一斌舒兴田
Owner CHINA PETROLEUM & CHEM CORP
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