Method for degradation of high salinity organic wastewater and synchronous preparation of iron oxide
A technology for organic wastewater with high salt content, applied in the fields of iron oxide, chemical instruments and methods, iron oxide/iron hydroxide, etc., which can solve the problems of sludge generation and low utilization rate of oxidant
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Embodiment 1
[0030] This embodiment provides a method for degrading high-salt organic wastewater and synchronously preparing iron oxide. The high-salt organic wastewater is selected from the industrial wastewater produced in the acid oxidation stage of DSD production, which contains NaSO 4 The content is about 10wt%, and the total organic carbon (TOC) is 9438mg / L. Take 200 mL of waste water and place it in a stirred reactor, add 0.5 g of iron oxide red catalyst, the oxidant is H 2 o 2 , and then take 30wt% H 2 o 2 30mL and 3.7mol / L ferrous chloride 75mL were simultaneously added to the reactor with a peristaltic pump, the pH of the reaction solution was controlled at 5.0-5.5 with lye, and the degradation reaction was carried out. After degradation, the TOC was 669mg / L, and the degradation efficiency 92.9%. The COD of the water sample was 76 mg / L after the salt was evaporated. The coloring power of the iron oxide red product produced by the reflux transformation of the filter cake iro...
Embodiment 2
[0032] This embodiment provides a method for degrading high-salt organic wastewater and synchronously preparing iron oxide. The high-salt organic wastewater is selected from the industrial wastewater produced in the acid oxidation stage of DSD production, which contains NaSO 4 The content is about 10wt%, and the total organic carbon (TOC) is 9438mg / L. Take 200 mL of waste water and place it in a stirred reactor, add 0.5 g of iron oxide red catalyst, and the oxidant is Na 2 S 2 o 8 , and then respectively take 130g Na 2 S 2 o 8 150 mL of aqueous solution and 3.7mol / L ferrous chloride, and the peristaltic pump was added to the reactor synchronously. The pH value of the reaction solution was controlled at 5.0-5.5 with alkali, and the degradation reaction was carried out. After degradation, the TOC was 366mg / L, and the degradation efficiency It was 91.3%. After distilling off the salt, the COD of the water sample is 49mg / L. Iron oxide red produced by reflux conversion of fi...
Embodiment 3
[0034] This embodiment provides a method for degrading high-salt organic wastewater and synchronously preparing iron oxide. The high-salt organic wastewater is selected from the industrial wastewater produced in the acid oxidation stage of DSD production, which contains NaSO 4 The content is about 10wt%, and the total organic carbon (TOC) is 9438mg / L. Take 200 mL of waste water and place it in a stirred reactor, add 0.5 g of iron oxide red catalyst, and the oxidizing agent is O 2, take 105mL of 3.7mol / L ferrous chloride, and add it into the reactor with a peristaltic pump. The pH value of the reaction solution is controlled at 5.0-5.5 with alkali, and the degradation reaction is carried out. After degradation, the TOC is 519mg / L, and the degradation efficiency is 96 %. After distilling off the salt, the COD of the water sample is 64mg / L. Iron oxide red produced by reflux conversion of the filter cake iron oxide has a coloring power of 99% (511 nm), and the product has good p...
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