2009
DOI: 10.1016/j.chemosphere.2009.08.023
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Treatment of Chromite Ore Processing Residue by pyrolysis with rice straw

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Cited by 30 publications
(7 citation statements)
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“…14 In previous research, a new technology for treatment of COPR was investigated. 15,16 In this process, COPR was initially mixed with rice straw and subsequently pyrolyzed at low temperatures. The Cr(VI) in COPR could be reduced into Cr(III) in less than 10 min of reaction time combined with low energy consumption of 43 kg of standard coal per ton of COPR.…”
Section: ■ Introductionmentioning
confidence: 99%
“…14 In previous research, a new technology for treatment of COPR was investigated. 15,16 In this process, COPR was initially mixed with rice straw and subsequently pyrolyzed at low temperatures. The Cr(VI) in COPR could be reduced into Cr(III) in less than 10 min of reaction time combined with low energy consumption of 43 kg of standard coal per ton of COPR.…”
Section: ■ Introductionmentioning
confidence: 99%
“…11− 14 The current low-temperature pyrolysis reduction technology has achieved a pyrolysis reduction rate of 80−90%. 13,14 However, considering the high initial Cr(VI) concentration (∼10 000 mg/kg), there is still a large quantity of Cr(VI) (exceed 1000 mg/kg) that is not reduced. This will always result in a frequent reoccurrence of Cr(VI) in the remediated chromium slag, 15 also called the reyellowing phenomenon, causing a severe secondary threat to the ecosystem and to public health.…”
Section: Introductionmentioning
confidence: 99%
“…In order to remediate Cr­(VI), various methods are applied, such as electro-dialysis, chelate, phytoremediation, and microbial remediation. Most of these are expensive or have low removal efficiency . Therefore, the low-temperature pyrolysis reduction of Cr­(VI) to nontoxic Cr­(III) by biomass has been generally considered satisfactory for chromium slag treatment. The current low-temperature pyrolysis reduction technology has achieved a pyrolysis reduction rate of 80–90%. , However, considering the high initial Cr­(VI) concentration (∼10 000 mg/kg), there is still a large quantity of Cr­(VI) (exceed 1000 mg/kg) that is not reduced. This will always result in a frequent reoccurrence of Cr­(VI) in the remediated chromium slag, also called the reyellowing phenomenon, causing a severe secondary threat to the ecosystem and to public health. , Therefore, to avoid serious secondary pollution, realizing a highly reduction efficiency of Cr­(VI) near 100% is urgently needed.…”
Section: Introductionmentioning
confidence: 99%
“…Most of these methods aim to reduce the hexavalent chromium (Cr(VI)) to trivalent chromium (Cr(III)) and to keep it in the mineral phase through ensuing treatments. 25 However, there have been some problems and limitations for these methods, including the large amount of the reducing agent used, high cost, 17 , 26 and the increased volume of residue after detoxification. 27 , 28 Besides, the components of the detoxified slag become more complicated because of the introduction of additional substances that make the subsequent resource utilization of the valuable elements difficult.…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, the COPR must be treated carefully. At present, the treatment of COPR focuses on environmentally friendly treatment by chemical reduction, hydrolysis, , electro-repair, stabilization/immobilization, , micro-organisms, biomass repair methods, , etc. Most of these methods aim to reduce the hexavalent chromium (Cr­(VI)) to trivalent chromium (Cr­(III)) and to keep it in the mineral phase through ensuing treatments .…”
Section: Introductionmentioning
confidence: 99%