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Selective separation recovery technology of heavy metal in electroplating sludge containing chromium

A selective and heavy metal technology, applied in the direction of improving process efficiency, can solve the problems of large consumption of acid and alkali and various precipitants, lack of convenience for separation and recovery, poor selective separation effect, etc., and achieve considerable economic benefits, Realize the effects of harmlessness and low requirements for industrial equipment

Active Publication Date: 2019-05-17
FUZHOU UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Chinese patent document CN101643243B discloses a resource utilization method of electroplating sludge, which is purified and recovered metal ions after acid leaching. Since the leaching solution after acid leaching contains a variety of metal ions, the selective separation effect is poor, and the subsequent separation process Complex, high consumption of acid-base and various precipitants
However, this method requires additional seed crystals, and the resulting product has poor magnetic properties, and is still lacking in the convenience of separation and recovery.

Method used

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  • Selective separation recovery technology of heavy metal in electroplating sludge containing chromium

Examples

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Embodiment 1

[0037]A process for selective separation and recovery of heavy metals in chromium-containing electroplating sludge, comprising the following steps:

[0038] (1) Mix 10g of electroplating sludge with 1g of ferric hydroxide and 2g of sodium carbonate, and place it in a muffle furnace for calcination at 550°C for 1.5 hours to obtain roasted sludge; the electroplating sludge is extracted from field sampling, and its elemental composition is mainly Cr(5.5%), Fe(7.8%), Ni(5.6%), Cu(6%), Zn(4.2%), Ca(10.2%), measured by ICP;

[0039] (2) Put the roasted sludge into a hydrothermal kettle, add 100mL of sodium hydroxide with a concentration of 5mol / L, and conduct a hydrothermal mineralization reaction at 180°C for 4 hours to obtain hydrothermal sludge;

[0040] (3) Separate the hydrothermal sludge by applying an external magnetic field. After separation, a 100mL solution containing Cr(VI) and Zn(II) (Zn concentration is 4.2g / L, Cr concentration is 4.5g / L) and a magnetic Hydrothermal re...

Embodiment 2

[0044] A process for selective separation and recovery of heavy metals in chromium-containing electroplating sludge, comprising the following steps:

[0045] (1) Take 20g of electroplating sludge (the electroplating sludge is extracted from field sampling, and the elemental composition determined by ICP is mainly Cr(6%), Fe(7.2%), Ni(5.5%), Cu(5.5%), Zn (4.3%), Ca (10.5%)) were mixed with 2.5g iron oxide and 5g sodium carbonate, and placed in a muffle furnace for calcination at 500°C for 2 hours to obtain roasted sludge;

[0046] (2) Put the roasted sludge into a hydrothermal kettle, add 200mL of potassium hydroxide with a concentration of 5mol / L, and conduct a hydrothermal mineralization reaction at 200°C for 3 hours to obtain hydrothermal sludge;

[0047] (3) Separate the hydrothermal sludge by applying an external magnetic field, and obtain a 200mL solution containing Cr(VI) and Zn(II) after separation (Zn concentration is 4.3g / L, Cr concentration is 4.3g / L) and a magnetic ...

Embodiment 3

[0051] A process for selective separation and recovery of heavy metals in chromium-containing electroplating sludge, comprising the following steps:

[0052] (1) Take 15g of electroplating sludge (the electroplating sludge is extracted from field sampling, and the element composition determined by ICP is mainly Cr(5.8%), Fe(7.3%), Ni(5.6%), Cu(5.6%), Zn(4.1%), Ca(10%)) were mixed with 2.0g iron oxide and 3g sodium carbonate, and placed in a muffle furnace for calcination at 400°C for 2 hours to obtain roasted sludge;

[0053] (2) Put the roasted sludge into a hydrothermal kettle, add 150mL of potassium hydroxide with a concentration of 5mol / L, and conduct a hydrothermal mineralization reaction at 190°C for 10 hours to obtain hydrothermal sludge;

[0054] (3) Separate the hydrothermal sludge by applying an external magnetic field, and obtain a solution containing Cr(VI) and Zn(II) after separation—150mL (Zn concentration is 4.3g / L, Cr concentration is 4.5g / L) and a magnetic Hy...

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Abstract

The invention relates to a selective separation recovery technology of heavy metal in electroplating sludge containing chromium. The selective separation recovery technology of the heavy metal in theelectroplating sludge containing the chromium specifically comprises the steps that (1) the sludge containing the chromium and carbonate are subjected to mix roasting under a certain temperature, andiron sources are supplemented appropriately; (2) hydrothermal reaction is carried out on a solid obtained in the step (1) and an alkaline mineralizing agent; (3) after solid-liquid separation is carried out on turbid liquid obtained in the step (2) by using magnetic force, a diluted acid solution (pH is 3.5-5.0) is added into the solid for calcium removal, and concentration and crystallization arecarried out for recovering the chromium after liquid dezincification; and (4) after the magnetic separation of the turbid liquid in the step (3) is carried out, mixed reaction is carried out on the solid and a concentrated acid solution (pH is 2-3.5); and after the magnetic separation of the obtained turbid liquid is carried out, the solid is a nickel ferrite product, and copper is recovered in aliquid mode. According to the selective separation recovery technology of the heavy metal in the electroplating sludge containing the chromium, doping regulation and control of metal elements in thesludge in spinel class materials (M (II) N (III) 2O4 (M=Ni, Cu, Zn, Ca; N=Cr, Fe, Al)) is realized through comprehensive regulation and control of the roasting temperature and a hydrothermal mineralizing agent, so that the selective separation recovery technology of the heavy metal is realized. Meanwhile, after the sludge is subjected to a roasting / hydrothermal combined technology, the solid has higher magnetic force, and the difficulty of solid-liquid separation in the technology is reduced.

Description

technical field [0001] The invention relates to a selective separation and recovery process for heavy metals in chromium-containing electroplating sludge, and belongs to the field of solid waste disposal and resource utilization. Background technique [0002] Electroplating sludge refers to heavy metal-containing sludge waste generated after electroplating sewage treatment, and is included in the seventeenth category of hazardous waste in the national hazardous waste list. At present, wastewater treatment plants mainly use chemical reduction, flocculation and precipitation treatment for chromium-containing electroplating wastewater, that is, using a reducing agent (such as ferrous sulfate) to first reduce Cr(VI) to Cr(Ⅲ), and then adding a precipitant (such as quicklime) to reduce Cr(VI) to Cr(Ⅲ). Cr(Ⅲ) was removed from wastewater in the form of Cr-OOH precipitation. In addition to Cr(III), the obtained electroplating sludge often contains iron oxyhydroxides. At the same t...

Claims

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Application Information

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IPC IPC(8): C22B7/00C22B1/02C22B34/32C22B15/00C22B23/00
CPCY02P10/20
Inventor 王永净林仕宏吴佳硕翁许骋姚虹
Owner FUZHOU UNIV
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