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A method for comprehensive recovery and utilization of waste rare earth type Y molecular sieve catalyst

A molecular sieve and catalyst technology, which is applied in the field of waste catalytic cracking catalyst recycling, to achieve the effects of shortening reaction time, reducing emissions, and reducing the difficulty of subsequent environmental protection treatment

Active Publication Date: 2018-03-13
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The present invention aims at the deficiencies in the current technology of recovering rare earth and other useful elements from waste rare earth type Y molecular sieve catalysts, and develops a two-step low-acid dissolution treatment method for waste rare earth type Y molecular sieve catalysts. The acid-dissolved molecular sieve still contains vanadium , nickel and other heavy metals can be doped into the selective catalytic reduction (SCR) catalyst for flue gas denitrification, and the aluminum-containing solution after rare earth recovery can be used as a raw material for polyaluminum chloride

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] The waste rare earth type Y molecular sieve catalyst adopts the waste balancer discharged from a catalytic cracking unit. The mixed rare earth content is 4.6%, the silicon-to-aluminum ratio of the waste molecular sieve is 3.4, and the carbon deposit of the molecular sieve is 0.35%. .

[0042] Take 50g of the waste rare earth type Y molecular sieve catalyst, put it into a container containing 2 liters of a mixed solution of hydrochloric acid and oxalic acid (2g oxalic acid dissolved in hydrochloric acid) with a pH of 1.3, and stir at 70°C for 3 hours to separate the solid and liquid phases. The rare earth is separated from the liquid phase by the oxalic acid precipitation method, and the separated solution is recycled for use after adjusting the pH value; the solid phase is again put into a 1.0 liter mixed solution of hydrochloric acid and oxalic acid with a pH of 0.7 (1g oxalic acid dissolved in hydrochloric acid) Add 1.0 g of oxalic acid to the container and stir at 70°C ...

Embodiment 2

[0049] The waste rare earth type Y molecular sieve catalyst adopts the waste balancer discharged from a catalytic cracking unit. The mixed rare earth content is 4.6%, the silicon-to-aluminum ratio of the waste molecular sieve is 3.4, and the carbon deposit of the molecular sieve is 0.35%. .

[0050] Take 50g of the waste rare earth type Y molecular sieve catalyst, put it into a container containing 2 liters of a mixed solution of hydrochloric acid and oxalic acid (2g oxalic acid dissolved in hydrochloric acid) with a pH of 1.6, and stir at a constant temperature of 80°C for 3 hours to separate the solid and liquid phases. The rare earths are separated from the liquid phase by the oxalic acid precipitation method, and the separated solution is recycled after adjusting the pH value; the solid phase is again put into a mixed solution containing 1.0 liter of hydrochloric acid and oxalic acid with a pH of 0.9 (1g oxalic acid dissolved in hydrochloric acid) Add 1.0 g of oxalic acid to ...

Embodiment 3

[0057] The waste rare earth type Y molecular sieve catalyst used is the same as in Example 1.

[0058] Take 50 g of waste rare earth type Y molecular sieve catalyst, put it into a container containing 1.5 liters of a mixed solution of hydrochloric acid and oxalic acid (3 g oxalic acid dissolved in hydrochloric acid) with a pH of 1.5, and stir at a constant temperature of 50°C for 2 hours to separate the solid and liquid phases. The rare earth is separated from the liquid phase by the oxalic acid precipitation method, and the separated solution is recycled after adjusting the pH value; the solid phase is again put into a mixed solution containing 1 liter of hydrochloric acid and oxalic acid with a pH of 0.8 (2g oxalic acid dissolved in hydrochloric acid) In the container, stir at a constant temperature of 50°C for 1.0 hour to separate the solid and liquid phases. The liquid phase is separated by the oxalic acid precipitation method to separate the rare earths, and the separated so...

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Abstract

The invention relates to a comprehensive recycling method of a waste rare-earth type Y-type molecular sieve catalyst. The comprehensive recycling method includes the following steps that firstly, the waste catalyst is stirred in a mixed acid solution with low acidity, so that most of rare earth is separated from a parent solution; secondly, the solid catalyst separated out is subjected to secondary stirring treatment in a mixed acid solution with high acidity, so that enough rare earth is separated from the parent solution, and since a molecular sieve of the parent solution is subjected to two times of acid leaching, the heavy metal content loss of a slag sample is small, and subsequent utilization is easy to implement; and finally, the solid molecular sieve slag sample is ground to be ultra-fine powder, and the ultra-fine powder is blended to the preparation of an SCR catalyst so as to replace part of titanium dioxide, so that the emission of heavy metal is reduced, the intensity of formed catalysts is increased, and meanwhile the denitration activity is not be reduced too much. An acid-containing solution is used as the parent solution for preparing polymer aluminum chloride after the rare earth is separated out, and the turbidity reducing effect of products is not affected, and is superior to the turbidity reducing effect of industrial polymer aluminum chloride.

Description

Technical field [0001] The invention relates to a method for recycling waste catalytic cracking catalysts, in particular to a method for recycling rare earth, aluminum and molecular sieve seeds in waste rare earth type Y molecular sieves. The invention belongs to the field of comprehensive utilization of rare earth catalysts. Background technique [0002] At present, rare earths are widely used in the field of catalysts. The domestic consumption of rare earths in the petrochemical field alone accounts for more than 10% of the total consumption of rare earths. Rare earth Y molecular sieves have been widely used in catalytic cracking since the 1960s, and this trend has been transferred to other molecular sieve catalysts. Nowadays, with the increasing shortage of resources, the recovery of rare earth components from the preparation process of petrochemical catalysts or catalyst waste has very good social and economic benefits. [0003] CN200510046121 proposes a method for dissolving ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/00C22B59/00B01J29/78
CPCY02P10/20
Inventor 巫树锋刘发强李常青贾媛媛刘光利杨岳江岩何琳梁宝锋王军张媛李扬李晶蕊荣树茂文善雄
Owner PETROCHINA CO LTD