A method for the recovery of nickel and energy substances from nickel hyperaccumulator plants

A super-enrichment plant and nickel-rich technology, applied in the field of solid waste recycling, can solve problems such as high operating costs, recovery of pyrolysis oil and pyrolysis gas, waste of resources, etc., and achieve high-value recovery and high recovery efficiency , to avoid the effect of wasting

Active Publication Date: 2021-03-26
SUN YAT SEN UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the cost of this method is relatively high, and only nickel can be recovered by this method, and a large amount of biomass energy of the hyperaccumulator itself is completely wasted, and a large amount of toxic and harmful gases will be produced during the incineration process
[0004] In addition, the patent CN106987722A pyrolyzes the hyperaccumulated plant harvest, and the pyrolytic charcoal produced by pyrolysis is leached with the leaching solution to extract heavy metals, and then enters the fluidized bed together with the pyrolysis oil to generate gasification gas, but the pyrolysis produces The pyrolysis gas has not been well treated and recovered, resulting in waste of resources and environmental pollution
Patent CN106984628A uses pyrolysis, purification, electrochemical deposition, leaching and other methods to recover gas, bio-oil and metals after pyrolysis of hyperaccumulated plant harvests, but the process is complicated and the operating cost is high, so it is difficult to produce more great economic value
Patent CN109987973A adopts the method of incineration to burn Osmanthus superaccumulative plant harvest into ash and prepare ash and rare earth micro-fertilizer. However, a large amount of toxic and harmful gases will be produced during the incineration process. In order to obtain proper treatment, incineration is also a The waste of the biomass resources of Osmanthus persicae itself has insufficient environmental and economic benefits.
Patent CN109794262A adopts pyrolysis method to burn cadmium hyperaccumulated plant harvests into cadmium-containing biochar, and uses sulfidation reaction to prepare cadmium-containing biochar into carbon-loaded cadmium sulfide photocatalytic material, but does not produce cadmium sulfide in the pyrolysis process. Pyrolysis oil and pyrolysis gas are recycled, resulting in a waste of resources. At the same time, exposure of pyrolysis oil gas to the environment will cause environmental pollution, which in turn will cause harm to the human body

Method used

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  • A method for the recovery of nickel and energy substances from nickel hyperaccumulator plants
  • A method for the recovery of nickel and energy substances from nickel hyperaccumulator plants

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] Embodiment 1 A kind of method that utilizes vacuum pyrolysis staged condensation device to reclaim energy substance from nickel hyperaccumulation plant Brassica japonica (Alysumsbertooonii)

[0054] 1. Vacuum pyrolysis segmental condensation device

[0055] The structure of the vacuum pyrolysis segmental condensation device is as follows: figure 1 As shown, it includes three parts: vacuum pyrolysis condensation system 5 , vacuum pumping system 26 and pyrolysis gas collection system 14 . Vacuum pyrolysis condensation system 5 is divided into inlet valve 1 and outlet valve 9, and a corundum tube 7 is placed in the vacuum pyrolysis condensation assembly 2. The first temperature zone in the tube is the pyrolysis zone, and a corundum crucible-4 is placed to hold Put the super-enrichment plant harvest 3, and control the temperature of the first temperature zone by controlling the silicon molybdenum rod thermocouple heating element 15 through the temperature regulator 18; the...

Embodiment 2

[0062] Example 2 Recovery of nickel and energy substances from nickel hyperaccumulator plant Brassica japonica (Alysums bertooonii)

[0063] (1) Drying 40 g of the harvested plant of the nickel hyperaccumulator Brassettina sativa, and crushing the dried plant in a shear crusher to obtain a uniform nickel hyperaccumulator harvested powder.

[0064] (2) The above-mentioned nickel hyperaccumulated plant powder is subjected to pyrolysis and condensation treatment using a vacuum pyrolysis staged condensation device. Set the vacuum degree of the first pyrolysis zone to 10Pa, the final pyrolysis temperature to 600°C, the heating rate to 30°C / min, and the retention time to 30min. Set the condensation temperature of the second condensation zone to 160°C, and set the condensation temperature of the third condensation zone to 60°C.

[0065] (3) Collect the pyrolysis products of the above-mentioned nickel hyperaccumulation plant harvests to obtain 27.67 g of mixed hydrocarbon pyrolysis o...

Embodiment 3

[0070] Embodiment 3 A kind of method that reclaims nickel and energy source material from nickel hyperaccumulator plant

[0071] (1) Drying 40 g of the harvested plant of the nickel hyperaccumulator Brassettina sativa, and crushing the dried plant in a shear crusher to obtain a uniform nickel hyperaccumulator harvested powder.

[0072] (2) The above-mentioned nickel hyperaccumulated plant powder is subjected to pyrolysis and condensation treatment using a vacuum pyrolysis staged condensation device. Set the vacuum degree of the first pyrolysis zone to 100Pa, the final pyrolysis temperature to 500°C, the heating rate to 20°C / min, and the retention time to 40min. Set the condensation temperature of the second condensation zone to 180°C, and set the condensation temperature of the third condensation zone to 80°C.

[0073] (3) Collect the pyrolysis products of the above-mentioned nickel hyperaccumulation plant harvests to obtain 24.14 g of mixed hydrocarbon pyrolysis oil and pyro...

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Abstract

The invention discloses a method of recovering nickel and energy substances from nickel hyperaccumulators. The method combines mechanical crushing, vacuum pyrolysis segmented condensation, heavy metalleaching and chemical precipitation. In the method, the energy substances, such as pyrolysis oil and pyrolysis gas, are recovered through a vacuum pyrolysis segmented condensation technology; pyrolysis residues are leached by adopting a mixed solution of hydrochloric acid and nitric acid; and nickel elements in a leaching solution precipitate in a form of nickel carbonate by adopting a sodium carbonate precipitant, and finally, a nickel carbonate solid is filtered and recovered. By adopting the method, high-value resource recovery of the nickel hyperaccumulator harvests is realized, biomassesof the nickel hyperaccumulators are converted to the energy substances, the nickel elements rich in the plants are recovered, and harms to the environment caused by exposure of the nickel hyperaccumulators to the environment is avoided; and the method is simple in whole process and high in recovery efficiency as well as has remarkable economic and environmental benefits.

Description

technical field [0001] The invention relates to the technical field of solid waste recycling, in particular to a method for recovering nickel and energy substances from nickel hyperaccumulation plants. Background technique [0002] Soil is the foundation of human survival, and most of the substances needed for human survival come from soil. However, since the industrial revolution, a large amount of soil has been polluted, which seriously threatens human life. Heavy metal pollution is particularly prominent in soil pollution. Since heavy metals cannot be decomposed by microorganisms in the soil, they are easy to accumulate in the soil, seriously endangering the health of humans and soil animals and plants. Heavy metal nickel is one of the eight heavy metals in soil pollution. Excessive nickel soil pollution can retard plant growth and cause plant necrosis. Long-term exposure of the human body to nickel will cause skin ulcers and even induce cancer. Therefore, some methods h...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/00C22B23/00
CPCC22B7/007C22B23/0423C22B23/0438C22B23/0461Y02P10/20
Inventor 仇荣亮秦保家刘文深汤叶涛何尔凯阮菊俊
Owner SUN YAT SEN UNIV
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