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Method for producing ammonium sulfate by using high-ammonium-nitrogen sulfur-containing high-salinity wastewater

A high-salt wastewater, ammonium sulfate technology, applied in chemical instruments and methods, ammonia compounds, water pollutants, etc., can solve the problems of difficult treatment and high treatment costs, and achieve the effects of simple process, high yield and low cost

Active Publication Date: 2014-11-05
BEIJING CYCLE COLUMBUS ENVIRONMENTAL SCI & TECH
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The purpose of the present invention is to solve the existing problems of high ammonia nitrogen, sulfur-containing high-salt wastewater treatment difficulties and high treatment costs; thereby providing a method for refining high-purity ammonium sulfate using adsorption degreasing-low-cost catalytic oxidation of this type of wastewater The method adopts a heterogeneous catalyst, the conversion rate is high, the product ammonium sulfate is high in purity, and there is no high-salt and high-COD wastewater discharge

Method used

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  • Method for producing ammonium sulfate by using high-ammonium-nitrogen sulfur-containing high-salinity wastewater
  • Method for producing ammonium sulfate by using high-ammonium-nitrogen sulfur-containing high-salinity wastewater
  • Method for producing ammonium sulfate by using high-ammonium-nitrogen sulfur-containing high-salinity wastewater

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Embodiment 1

[0022] Refer to attached figure 1 , present embodiment is the method for producing ammonium sulfate with gaseous ammonia method desulfurization waste water, and concrete process is as follows:

[0023] 1) Catalytic oxidation: Take iron, vanadium and copper with a mass ratio of 1:1:3 to obtain the catalyst by roasting, and put the catalyst equivalent to 1% of the wastewater volume and the activated carbon equivalent to 0.1% of the wastewater volume at 95°C at the same time. In the wastewater, pure oxygen is used to aerate and stir for 720 minutes. During the aeration, the tar and other oils dissolved in the wastewater are adsorbed by activated carbon, and the following chemical reactions also occur:

[0024]

[0025] 2) Catalyst regeneration: The mixture after the reaction in step 1) is subjected to solid-liquid separation, wherein the solid contains activated carbon and catalyst, and is heated by air at 900°C for 600 minutes to obtain a mixture of activated carbon and catal...

Embodiment 2

[0030] Present embodiment is the method for producing ammonium sulfate with corn deep processing waste water, and concrete technology is as follows:

[0031] Take nickel, iron, chromium, titanium, and aluminum with a mass ratio of 1:1:2:5:1 to obtain a catalyst by roasting. At 10°C, the catalyst equivalent to 0.01% of the waste water, and the catalyst equivalent to 0.1% of the waste water Activated carbon is put into the wastewater at the same time, and air is used to aerate and stir for 10 minutes. During the aeration period, the dissolved corn oil in the wastewater is absorbed by the activated carbon, and all sulfur-containing ions are converted into sulfate radicals through a catalytic reaction.

[0032] The mixture after the catalytic oxidation reaction is subjected to solid-liquid separation, in which the solid contains activated carbon and the catalyst, and is heated at 200°C with air for 30 minutes to obtain a mixture of activated carbon and catalyst. Due to the low cata...

Embodiment 3

[0035] Present embodiment is the method for producing ammonium sulfate with chemical fertilizer production waste water, and concrete technology is as follows:

[0036] Take cobalt, manganese, cadmium, and rubidium with a mass ratio of 1:6:1:2 to obtain the catalyst by roasting, and put the catalyst equivalent to 0.3% of the wastewater volume and the activated carbon equivalent to 1% of the wastewater volume into the wastewater at the same time In the process, the air was aerated and stirred for 300 minutes, and all sulfur-containing ions were converted into sulfate radicals through a catalytic reaction during the aeration.

[0037] The mixture after the catalytic oxidation reaction is subjected to solid-liquid separation, wherein the solid contains activated carbon and catalyst, and is heated at 550°C for 240 minutes to obtain a mixture of activated carbon and catalyst. Due to this reaction condition, the activated carbon will only have a small amount of loss. After reaching a...

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Abstract

The invention relates to a method for preparing ammonium sulfate from high-ammonium-nitrogen sulfur-containing high-salinity wastewater. The method comprises the following steps of: mixing the wastewater with active carbon as well as a catalyst, then aerating by using air or pure oxygen at the temperature of 10-95 DEG C and reacting mixture for 10-720 minutes; performing solid-liquid separation on reacted slurry, wherein solid is mixture of the catalyst and the active carbon and can be continuously used after being regenerated, and the liquid is evaporated, concentrated, crystallized and dried to obtain an ammonium sulfate product; and concentrating and crystallizing mother liquor, returning to aerate, catalyze, oxidize and continuously purify the mother liquor to be used as a material. By adopting the method, the problem of pollution caused to environment by the high-ammonium-nitrogen sulfur-containing high-salinity wastewater is solved; meanwhile, the high-purity ammonium sulfate product is produced; and recycling of waste is realized.

Description

field of invention [0001] The invention relates to a process method for reusing high-salt and low-organic-matter wastewater, in particular to a method for preparing ammonium sulfate from wastewater containing high concentrations of ammonium and sulfur anions. Background technique [0002] In the production process of metallurgy, chemical industry, chemical fertilizer, food processing, electroplating and other industries, a large amount of high-salt wastewater is often produced, and its total salt concentration often reaches more than 10%. If it is discharged directly, it will cause potential harm to the environment. Therefore, it must be treated It governs. [0003] At present, the common treatment methods of high-salt wastewater reported in my country's patents mainly include: biodegradation method (CN200910191713.X, CN201010170494.X), separation and recovery method (CN200710167258.0), physical and chemical treatment method (CN200810119250.1, CN200610023287.5, CN20082008175...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01C1/245C02F9/04C02F1/28C02F1/72C02F101/18
Inventor 刘晨明曹宏斌李玉平林晓
Owner BEIJING CYCLE COLUMBUS ENVIRONMENTAL SCI & TECH