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含硫废水循环利用法合成二烯丙基二硫醚的新工艺
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作者 邱滔 彭全舟 吕新宇 《精细石油化工》 CAS CSCD 北大核心 2010年第2期35-37,共3页
实验以PEG-400(聚乙二醇-400)为相转移催化剂,Na_2S_2与3-氯丙烯为原料合成了二烯丙基二硫醚。考察了相转移催化剂类型、相转移催化剂的量、原料配比、反应温度和反应时间等因素对反应的影响。最佳工艺条件为:n(Na_2S_2):n(3-氯丙烯)=0.... 实验以PEG-400(聚乙二醇-400)为相转移催化剂,Na_2S_2与3-氯丙烯为原料合成了二烯丙基二硫醚。考察了相转移催化剂类型、相转移催化剂的量、原料配比、反应温度和反应时间等因素对反应的影响。最佳工艺条件为:n(Na_2S_2):n(3-氯丙烯)=0.6:1,m(Na_2S_2):m(PEG-400)=105.6:1,反应温度50℃,反应时间1 h,二烯丙基二硫醚收率可达80.2%。含硫废水循环利用3次不影响产率。 展开更多
关键词 二硫化二钠 3-氯丙烯 聚乙 烯丙基硫醚 含硫废水 循环利用
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相转移催化法合成二烯丙基二硫的研究 被引量:5
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作者 魏冰 《精细化工》 EI CAS CSCD 北大核心 2000年第9期556-557,共2页
用四丁基溴化铵做相转移催化剂 ,2 0℃下 ,在 0 5h内将 17 6mL烯丙基溴滴加到二硫化二钠溶液中 ,然后回流反应 1h ,合成了二烯丙基二硫 ,产率达到 87 7% (二烯丙基二硫的质量分数为 97 2 % ) ,并且对其结构进行了红外光谱和核磁共振分析。
关键词 烯丙基 烯丙基溴 二硫化二钠 相转移催化
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Dyestuff wastewater treatment by combined SDS-CuO/TiO_2 photocatalysis and sequencing batch reactor 被引量:2
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作者 徐璇 吉芳英 +3 位作者 范子红 何莉 胡学斌 张琨 《Journal of Central South University》 SCIE EI CAS 2012年第6期1685-1692,共8页
Combined technology of SDS-CuO/TiO2 photocatalysis and sequencing batch reactor (SBR) were applied to treating dyestuff wastewater. Photocatalysis was carried out in a spiral up-flow type reactor as pre-treatment. S... Combined technology of SDS-CuO/TiO2 photocatalysis and sequencing batch reactor (SBR) were applied to treating dyestuff wastewater. Photocatalysis was carried out in a spiral up-flow type reactor as pre-treatment. SDS-CuO/TiO2 photocatalyst was prepared by modification of nano-TiO2 using CuO and sodium dodecyl sulfate (SDS). Results show that the SDS-CuO/TiO2 photocatalyst contains two kinds of crystals, including TiO2 and CuO. The band gap of this photocatalyst is 1.56 eV, indicating that it can be excited by visible light (2〈794.87 nm). And characterization also shows that there are alkyl groups on its surface. It takes 40 rain to improve the biodegradability of dyestuff wastewater. Five-day biochemical oxygen demand (BODs) and dehydrogenase activity (DHA) of wastewater reach the maximum value when dissolved oxygen is higher than 2.97 mg/L. SBR reactor was used to treat this biodegradability improved wastewater. Chemical oxygen demand (COD) and colority decline to 72 mg/L and 20 times, respectively, when the sludge loading is 0.179 kg(COD)/[kg(MLSS)'d], dissolved oxygen is 4.09 mg/L and aeration time is 10 h. 展开更多
关键词 BIODEGRADABILITY PHOTOCATALYSIS sequencing batch reactor dyestuffwastewater
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Oxidative Desulfurization of Diesel Fuel with Hydrogen Peroxide Using Na_2WO_4 as Catalyst 被引量:1
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作者 Sun Xin Long Jun +1 位作者 Xu Benjing Xie Chaogang (Research Institute of Petroleum Processing, SINOPEC, Beijing 100083) 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2009年第1期45-50,共6页
Oxidative desulfurization was performed on Na2WO4 catalyst in the presence of hydrogen peroxide and acetic acid under mild reaction conditions (atmospheric pressure and temperature range of 293--343 K). Different or... Oxidative desulfurization was performed on Na2WO4 catalyst in the presence of hydrogen peroxide and acetic acid under mild reaction conditions (atmospheric pressure and temperature range of 293--343 K). Different organic compounds including benzothiophene (BT), dibenzothiophene (DBT), 4, 6-dimethyl dibenzothiophene (4, 6-DMDBT) were used to investigate the reactivity of this catalyst, and the effect of various parameters, such as temperature, solvents and the amount of oxidant reagent used in oxidative desulfurization reaction, was also examined. The results showed that the Na2WO4- H202 system was very effective for oxidative desulfurization, and the oxidation of BT, DBT and 4, 6-DMDBT was influenced by different parameters. 展开更多
关键词 oxidative desulfurization DIBENZOTHIOPHENE Na2WO4 hydrogen peroxide
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