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Method for recovering palladium from barium sulfate carrier invalid palladium catalyst

A palladium catalyst and barium sulfate technology, which is applied in the field of comprehensive recycling of precious metal secondary resources, can solve the problems of short process flow and achieve the effects of short process flow, low production cost and simple operation

Active Publication Date: 2019-09-13
GUIYAN RESOURCE YIMEN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The object of the present invention is to overcome above-mentioned deficiencies in the prior art, provide a kind of process flow short, production cost is low, simple to operate, the method that the recovery rate of palladium is high from barium sulfate carrier invalidation palladium catalyst reclaims palladium, solves the problem from barium sulfate The problem of improving the recovery rate of palladium when recovering palladium in the palladium catalyst with carrier failure

Method used

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  • Method for recovering palladium from barium sulfate carrier invalid palladium catalyst

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Embodiment 1

[0028] Such as figure 1 Shown, the method for recovering palladium from barium sulfate carrier invalidation palladium catalyst, carries out successively according to the following steps:

[0029] A. Oxidation roasting: Put 200 g of the barium sulfate carrier invalid palladium catalyst into a 500 ml porcelain bowl and roast at a high temperature in a muffle furnace, the roasting temperature is 800° C., and the roasting time is 2 hours;

[0030] B. Ball mill mixing: the barium sulfate carrier invalid palladium catalyst after roasting is ground into particles with a particle size of 200 mesh with a ball mill, and the particles after grinding are mixed evenly with sodium carbonate and anti-dispersing agent according to the mass ratio of 20:60:1;

[0031] C. High-temperature calcination: put the mixed material into a 1500ml porcelain bowl and use a muffle furnace for high-temperature calcination. The high-temperature calcination temperature is 900°C, and the calcination time is 2 h...

Embodiment 2

[0038] The method for recovering palladium from barium sulfate carrier invalidation palladium catalyst, carries out successively according to the following steps:

[0039] A. Oxidation roasting: Put 500 g of barium sulfate carrier invalid palladium catalyst into a 500 ml porcelain bowl and roast at a high temperature in a muffle furnace, the roasting temperature is 700° C., and the roasting time is 4 hours;

[0040] B. Ball milling mixture: the barium sulfate carrier invalid palladium catalyst after roasting is ground into particles with a particle size of 120 mesh with a ball mill, and the particles after grinding are mixed evenly with sodium carbonate and anti-dispersing agent according to the mass ratio of 40:160:3;

[0041] C. High-temperature calcination: put the mixed material into a 1500ml porcelain bowl and use a muffle furnace for high-temperature calcination. The high-temperature calcination temperature is 800° C., and the calcination time is 3 hours;

[0042] D. Wat...

Embodiment 3

[0048] The method for recovering palladium from barium sulfate carrier invalidation palladium catalyst, carries out successively according to the following steps:

[0049] A. Oxidation roasting: Put 500 g of barium sulfate carrier invalid palladium catalyst into a 500 ml porcelain bowl and roast at a high temperature in a muffle furnace, the roasting temperature is 600° C., and the roasting time is 6 hours;

[0050] B. Ball mill mixing: the barium sulfate carrier invalid palladium catalyst after roasting is ground into particles with a particle size of 40 meshes with a ball mill, and the particles after grinding are mixed evenly with sodium carbonate and anti-dispersing agent according to the mass ratio of 10:50:1;

[0051] C. High-temperature calcination: put the mixed material into a 1500ml porcelain bowl and use a muffle furnace for high-temperature calcination. The high-temperature calcination temperature is 900°C, and the calcination time is 2 hours;

[0052] D. Water sol...

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Abstract

The invention relates to the field of precious metal secondary resource comprehensive recycling, in particular to a method for recovering palladium from an ineffective barium sulfate carrier palladium catalyst. The method for recovering palladium from the ineffective barium sulfate carrier palladium catalyst comprises the following sequential steps of A, oxidizing roasting; B, ball-milling material mixing; C, high-temperature calcination; D, dissolution in water; E, hydrochloric acid decomposition; and F, filtering and drying. The method for recovering palladium from the ineffective barium sulfate carrier palladium catalyst has the advantages of being short in technological process, low in production cost and high in palladium recovery rate, and easy top operate.

Description

technical field [0001] The invention relates to the field of comprehensive recovery and utilization of precious metal secondary resources, in particular to a method for recovering palladium from an invalid palladium catalyst supported by barium sulfate. Background technique [0002] The palladium catalyst with barium sulfate as the carrier is mainly used in the fields of pharmaceuticals and fine chemicals. It has good catalytic performance for catalytic hydrogenolysis reactions, such as hydrogenolysis of acid chlorides to produce aldehydes. The content of palladium in commonly used catalysts is 1%, 5%, 10% %, etc., the content of palladium is relatively high, and the spent catalyst has a high recovery value. [0003] Barium sulfate is relatively stable in nature, and palladium is usually recovered from spent catalysts by directly dissolving palladium. Due to the large specific surface area and strong adsorption capacity of the barium sulfate carrier, the dissolved palladium...

Claims

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Application Information

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IPC IPC(8): C22B11/00
Inventor 王欢赵雨贺小塘郭俊梅熊庆丰李勇吴喜龙刘文张选冬
Owner GUIYAN RESOURCE YIMEN