CN102259896A - Method for extracting sodium thiocyanate from coking desulfurization waste liquid - Google Patents
Method for extracting sodium thiocyanate from coking desulfurization waste liquid Download PDFInfo
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Abstract
本发明为焦化厂脱硫废液提取硫氰酸钠的一种方法,其特征为:焦化脱硫废液加入2-6wt%活性炭,加热到70-90℃并保持搅拌1-2小时,过滤,滤液在密闭容器内加入硫酸至pH=3.5-4.5,加热到60-80℃并保持搅拌1-2小时,逸出的二氧化硫气体用导管引出并用稀氨水吸收,反应结束后过滤,滤液在密闭容器内加入与滤液中硫氰酸铵等物资的量的氢氧化钠和与滤液中硫酸铵等物质的量的氢氧化钙,加热到50-70℃并保持搅拌1-2小时,逸出的氨气用导管引出并用水吸收成稀氨水,反应结束后过滤,滤液蒸发结晶得到硫氰酸钠产品。The present invention is a method for extracting sodium thiocyanate from coking plant desulfurization waste liquid, which is characterized in that: coking desulfurization waste liquid is added with 2-6wt% activated carbon, heated to 70-90°C and kept stirring for 1-2 hours, filtered, and the filtrate Add sulfuric acid to the closed container to pH = 3.5-4.5, heat to 60-80°C and keep stirring for 1-2 hours, the escaped sulfur dioxide gas is drawn out with a catheter and absorbed with dilute ammonia water, filtered after the reaction, and the filtrate is in a closed container Add sodium hydroxide in the same amount as ammonium thiocyanate in the filtrate and calcium hydroxide in the same amount as ammonium sulfate in the filtrate, heat to 50-70°C and keep stirring for 1-2 hours, the released ammonia gas Lead out with a catheter and absorb it with water to form dilute ammonia water. After the reaction is completed, filter, and the filtrate is evaporated and crystallized to obtain sodium thiocyanate product.
Description
技术领域: Technical field:
本发明属于化工废水的回收处理领域,具体涉及到焦化脱硫废液提取硫氰酸钠的方法。The invention belongs to the field of recovery and treatment of chemical wastewater, and in particular relates to a method for extracting sodium thiocyanate from coking desulfurization waste liquid.
背景技术: Background technique:
目前,国内许多焦化厂采用HPF脱硫脱氰工艺,该工艺必须外排一部分脱硫废液并补充水分以保持较高的脱硫效率。焦化脱硫废液中含有大量的硫氰酸铵,是附加值很高的化工产品。从焦化脱硫废液中提取硫氰酸铵,是资源化处理脱硫废液切实可行的方法。At present, many domestic coking plants adopt the HPF desulfurization and decyanation process, which must discharge part of the desulfurization waste liquid and replenish water to maintain a high desulfurization efficiency. Coking desulfurization waste liquid contains a large amount of ammonium thiocyanate, which is a chemical product with high added value. Extracting ammonium thiocyanate from coking desulfurization waste liquid is a feasible method for resource treatment of desulfurization waste liquid.
目前国内从焦化脱硫废液中提取硫氰酸铵的主要方法是真空蒸馏浓缩,再分步结晶分别得到硫代硫酸铵和硫氰酸铵产品。这种方法所得到硫氰酸铵纯度较低,一般在70-90%之间,纯度很难达到95%以上。纯度较低的硫氰酸铵用途受限,价格低廉,经济效益较差。如何改进提盐方法,从焦化脱硫废液中提取高纯度的硫氰酸钠,具有十分重要的意义。At present, the main method of extracting ammonium thiocyanate from coking desulfurization waste liquid in China is vacuum distillation and concentration, followed by fractional crystallization to obtain ammonium thiosulfate and ammonium thiocyanate respectively. The ammonium thiocyanate purity obtained by this method is relatively low, generally between 70-90%, and the purity is difficult to reach more than 95%. The use of ammonium thiocyanate with lower purity is limited, the price is low, and the economic benefit is relatively poor. How to improve the salt extraction method and extract high-purity sodium thiocyanate from coking desulfurization waste liquid is of great significance.
发明内容 Contents of the invention
本发明以焦化脱硫废液为原料,提取纯度大于96%的硫氰酸钠产品。The invention uses coking desulfurization waste liquid as a raw material to extract sodium thiocyanate product with a purity greater than 96%.
本发明具体操作如下:焦化脱硫废液加入2-6wt%活性炭,加热到70-90℃并保持搅拌1-2小时,过滤,滤液在密闭容器内加入硫酸至pH=3.5-4.5,加热到60-80℃并保持搅拌1-2小时,逸出的二氧化硫气体用导管引出并用稀氨水吸收,反应结束后过滤,滤液在密闭容器内加入与滤液中硫氰酸铵等物资的量的氢氧化钠和与滤液中硫酸铵等物质的量的氢氧化钙,加热到50-70℃并保持搅拌1-2小时,逸出的氨气用导管引出并用水吸收成稀氨水,反应结束后过滤,滤液蒸发结晶得到硫氰酸钠产品。The specific operation of the present invention is as follows: add 2-6wt% activated carbon to the coking desulfurization waste liquid, heat to 70-90°C and keep stirring for 1-2 hours, filter, add sulfuric acid to the filtrate in a closed container to pH=3.5-4.5, heat to 60 Keep stirring at -80°C for 1-2 hours. The escaped sulfur dioxide gas is drawn out with a catheter and absorbed with dilute ammonia water. After the reaction is completed, filter it. Add sodium hydroxide in the amount of ammonium thiocyanate and other materials in the filtrate to the filtrate in a closed container. and calcium hydroxide in the amount of ammonium sulfate and other substances in the filtrate, heated to 50-70°C and kept stirring for 1-2 hours, the escaped ammonia gas was drawn out with a catheter and absorbed into dilute ammonia water, filtered after the reaction, and the filtrate Evaporation and crystallization to obtain sodium thiocyanate product.
具体实施方式 Detailed ways
实例1Example 1
取铜陵新亚星焦化有限公司所提供的焦化脱硫废液,经分析该废液主要成分为:NH4SCN 183g/L,(NH4)2S2O3 155g/L,(NH4)2SO4 47g/L,取该废液1升在烧杯中加入活性炭60g,加热到70℃并保持搅拌1小时,过滤;滤液在密闭容器内加入98%浓硫酸60mL至pH=3.5,加热到80℃并保持搅拌1小时,逸出的SO2气体用导管引出并用稀氨水吸收;反应结束后过滤,滤液在密闭容器内加入NaOH96g和Ca(OH)2 110g,加热到70℃并保持搅拌1小时,逸出的氨气用导管引出并用水吸收成稀氨水;反应结束后过滤,滤液蒸发结晶得到硫氰酸钠产品178g,纯度达到97%。Take the coking desulfurization waste liquid provided by Tongling Xinyaxing Coking Co., Ltd. After analysis, the main components of the waste liquid are: NH 4 SCN 183g/L, (NH 4 ) 2 S 2 O 3 155g/L, (NH 4 ) 2 SO 4 47g/L, take 1 liter of the waste liquid, add 60g of activated carbon to a beaker, heat to 70°C and keep stirring for 1 hour, filter; add 60mL of 98% concentrated sulfuric acid to the filtrate in a closed container until pH=3.5, heat to 80 ℃ and keep stirring for 1 hour, the escaped SO 2 gas is drawn out with a catheter and absorbed with dilute ammonia water; after the reaction is completed, filter, add NaOH 96g and Ca(OH) 2 110g to the filtrate in a closed container, heat to 70 ℃ and keep stirring for 1 hour , the escaping ammonia is drawn out with a conduit and absorbed into dilute ammonia water; after the reaction is finished, filter, and the filtrate is evaporated and crystallized to obtain 178g of sodium thiocyanate product, with a purity of 97%.
实例2Example 2
取山东省昌邑市华昊焦化有限公司所提供的焦化脱硫废液,经分析该废液主要成分为:NH4SCN 136g/L,(NH4)2S2O3 107g/L,(NH4)2SO4 31g/L,取该废液1升在烧杯中加入活性炭20g,加热到90℃并保持搅拌2小时,过滤;滤液在密闭容器内加入70%浓硫酸55mL至pH=4.5,加热60℃并保持搅拌2小时,逸出的SO2气体用导管引出并用稀氨水吸收;反应结束后过滤,滤液在密闭容器内加入NaOH 72g和Ca(OH)2 75g,加热到50℃并保持搅拌1小时,逸出的氨气用导管引出并用水吸收成稀氨水;反应结束后过滤,滤液蒸发结晶得到硫氰酸钠产品129g,纯度达到96%。Take the coking desulfurization waste liquid provided by Huahao Coking Co., Ltd. in Changyi City, Shandong Province. After analysis, the main components of the waste liquid are: NH 4 SCN 136g/L, (NH 4 ) 2 S 2 O 3 107g/L, (NH 4 ) 2 SO 4 31g/L, take 1 liter of the waste liquid, add 20g of activated carbon to a beaker, heat to 90°C and keep stirring for 2 hours, filter; add 55mL of 70% concentrated sulfuric acid to the filtrate in a closed container until pH = 4.5, heat 60°C and keep stirring for 2 hours, the escaped SO 2 gas is drawn out with a catheter and absorbed with dilute ammonia water; after the reaction is completed, filter, add 72g of NaOH and 75g of Ca(OH) 2 to the filtrate in a closed container, heat to 50°C and keep stirring After 1 hour, the released ammonia gas was drawn out with a catheter and absorbed into dilute ammonia water; after the reaction was completed, it was filtered, and the filtrate was evaporated and crystallized to obtain 129 g of sodium thiocyanate product, with a purity of 96%.
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102795644A (en) * | 2012-08-27 | 2012-11-28 | 安徽工业大学 | Method for recovering sodium thiocyanate from desulfurated waste liquid by modified ADA method |
CN103288286A (en) * | 2013-06-28 | 2013-09-11 | 陕西煤业化工技术研究院有限责任公司 | Catalytic oxidation treatment method for desulfurized waste liquid |
CN103395805A (en) * | 2013-07-18 | 2013-11-20 | 宜兴市燎原化工有限公司 | Method for preparing high-quality sodium thiocyanate from desulfurized and decyanated waste liquid of coke oven gas |
CN103420448A (en) * | 2013-08-22 | 2013-12-04 | 张家港燎原环保科技有限公司 | Thiosulfate removing method for coke oven gas desulfuration liquid waste using ion exchange resin |
CN103588340A (en) * | 2013-11-27 | 2014-02-19 | 安徽工业大学 | Method for treating sodium-alkali desulfurization waste liquid by causticization-acidification method |
CN104925830A (en) * | 2015-07-10 | 2015-09-23 | 安徽工业大学 | Chemical treatment method for extracting sodium thiocyanate from coked desulfurization waste solution |
CN105540613A (en) * | 2015-12-28 | 2016-05-04 | 河北诚信九天医药化工有限公司 | Method for preparing potassium thiocyanate combined-produced ammonia water by using coked waste liquor |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU530851A1 (en) * | 1974-12-13 | 1976-10-05 | Украинский научно-исследовательский углехимический институт | Method of producing rodsanate sodium |
CN1062884A (en) * | 1990-12-29 | 1992-07-22 | 湖南省农药工业公司 | Preparation process for high-content sodium rhodanide |
CN101966996A (en) * | 2010-09-30 | 2011-02-09 | 武汉科技大学 | Method for extracting NaSCN from thiocyanate-containing wastewater solution |
-
2011
- 2011-06-21 CN CN201110166190A patent/CN102259896A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU530851A1 (en) * | 1974-12-13 | 1976-10-05 | Украинский научно-исследовательский углехимический институт | Method of producing rodsanate sodium |
CN1062884A (en) * | 1990-12-29 | 1992-07-22 | 湖南省农药工业公司 | Preparation process for high-content sodium rhodanide |
CN101966996A (en) * | 2010-09-30 | 2011-02-09 | 武汉科技大学 | Method for extracting NaSCN from thiocyanate-containing wastewater solution |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102795644A (en) * | 2012-08-27 | 2012-11-28 | 安徽工业大学 | Method for recovering sodium thiocyanate from desulfurated waste liquid by modified ADA method |
CN102795644B (en) * | 2012-08-27 | 2015-10-21 | 安徽工业大学 | A kind of method reclaiming Sodium Thiocyanate 99 from modified ADA method desulfurization waste liquor |
CN103288286A (en) * | 2013-06-28 | 2013-09-11 | 陕西煤业化工技术研究院有限责任公司 | Catalytic oxidation treatment method for desulfurized waste liquid |
CN103288286B (en) * | 2013-06-28 | 2015-03-18 | 陕西煤业化工技术研究院有限责任公司 | Catalytic oxidation treatment method for desulfurized waste liquid |
CN103395805A (en) * | 2013-07-18 | 2013-11-20 | 宜兴市燎原化工有限公司 | Method for preparing high-quality sodium thiocyanate from desulfurized and decyanated waste liquid of coke oven gas |
CN103395805B (en) * | 2013-07-18 | 2016-03-30 | 江苏燎原环保科技股份有限公司 | The method of high-quality Sodium Thiocyanate 99 is prepared with coke-oven-gas desulfurization and decyanation waste liquid |
CN103420448A (en) * | 2013-08-22 | 2013-12-04 | 张家港燎原环保科技有限公司 | Thiosulfate removing method for coke oven gas desulfuration liquid waste using ion exchange resin |
CN103588340A (en) * | 2013-11-27 | 2014-02-19 | 安徽工业大学 | Method for treating sodium-alkali desulfurization waste liquid by causticization-acidification method |
CN103588340B (en) * | 2013-11-27 | 2014-12-24 | 安徽工业大学 | Method for treating sodium-alkali desulfurization waste liquid by causticization-acidification method |
CN104925830A (en) * | 2015-07-10 | 2015-09-23 | 安徽工业大学 | Chemical treatment method for extracting sodium thiocyanate from coked desulfurization waste solution |
CN104925830B (en) * | 2015-07-10 | 2016-10-05 | 安徽工业大学 | A chemical treatment method for extracting sodium thiocyanate from coking desulfurization waste liquid |
CN105540613A (en) * | 2015-12-28 | 2016-05-04 | 河北诚信九天医药化工有限公司 | Method for preparing potassium thiocyanate combined-produced ammonia water by using coked waste liquor |
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Application publication date: 20111130 |