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双语推荐:氧化钨

氧化钨是一种半导体光催化剂,可用于降解水中污染物。在用三氧化钨作为光催化剂处理亚甲基蓝模拟废水的反应中,通过单因素和正交实验,确定最佳处理条件为三氧化钨用量50mg、反应时间40min、H2O2用量4mL。并通过动力学研究,确定在不同三氧化钨光催化反应体系中的降解反应级数。
Tungsten trioxide was a semiconductor photocatalyst which could be used for degradation of pollutants in water. In the treatment of methylene blue simulation wastewater, tungsten oxide was applied as a photocatalyst, and through the single factor and orthogonal experiments, the optimal processing conditions were obtained:tungsten trioxide content 50mg, reaction time 40min, the dosage of H2O2 4mL. By the kinetics study, the degradation reaction order was determined in different tungsten oxide photocatalysis reaction system.

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以TaCl5和Na2 WO4为原料,采用水热法在170℃保温6h~48h合成钽掺杂球形氧化钨。利用XRD、SEM等手段对产物进行物相、形貌表征。研究表明:水热反应时间为6 h~48 h均能获得三斜晶型的氧化钨球,球体尺寸在200 nm~350 nm之间。对不同反应时间条件下合成的氧化钨球进行紫外-可见光的吸收光谱分析可知,随着反应时间的增加,获得钽掺杂氧化钨样品对光的吸收能力增强,平均禁带宽度为3.72 eV。
Global tungsten oxide doped with tantalum were synthesized by a facile hydrothermal method using TaCl5 and Na2 WO4 as raw materials at 170℃ for 6h ~48h. The samples of the products were characterized by XRD,SEM and IR. The results showed that the global tungsten oxide powders with the pure triclinic phase in the grain size range from 200 to 350 nm can be synthesized at 6 h~48 h at 170℃. The optical absorption preoperties of the samples were characterized by UV-VIS. As the reaction time increasing,the optical absorption of synthesized global tungsten oxide doped with addition of tantalum increased gradually,and the average band gap was 3. 72eV.

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概述近年微波及超声波在钨冶金生产工艺中的应用研究进展,简介其应用工艺和技术.主要从微波在钨冶金中应用:促进黑、白钨矿浸出;促进含钨化合物合成;烧结含钨化合物与热分解制备三氧化钨;超声波在钨冶金中应用:强化钨矿浸出及仲钨酸铵结晶;辅助制备含钨化合物;工业探伤应用等领域进行介绍.微波及超声波技术在钨冶金中应用将越来越广泛和深入.
The application processes with microwave and ultrasonic technology in tungsten metallurgy is introduced. The application of microwave in tungsten metallurgy includes the promotion of the ore leaching of scheelite and wolframite, as well as the synthesis of tungsten-containing compounds, the sintering of the tungsten -containing compounds and the thermal decomposition preparation of tungsten trioxide. The application of ultrasonic in metallurgy of tungsten contains the enforcement of the extraction of tungsten-containing compounds and crystallization of APT , assisted preparation of tungsten-containing compounds and industrial testing. The application of microwave and ultrasonic technology in tungsten metallurgy are becoming increasingly prevalent and far-reaching.

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以TaCl5、Na2WO4·2H2O及C6H6O12为原料,采用水热法在140℃~200℃保温48h合成钽掺杂球形氧化钨。利用XRD、SEM等手段对产物进行物相、形貌进行表征。研究表明:水热反应温度140℃~200℃为均能获得三斜晶型的氧化钨球,球体尺寸在2~3μm之间。对不同反应温度条件下合成的氧化钨球进行紫外-可见光的吸收光谱分析可知,平均禁带宽度为3.73e V,在170℃水热条件下获得样品对光的吸收性能最好。该样品在高温煅烧后,形貌发生较大的变化。
Global tungsten oxide doped with tantalum were synthesized by a facile hydrothermal method using TaCl5 , Na2 WO4 ? 2H2 O and C6 H12 O6 as raw materials at 140℃ ~200℃ for 48 h. The samples of the products were characterized by XRD and SEM. The results show that the global tungsten oxide powders with the pure triclinic phase in the grain size range from 2 to 3 μm can be synthesized at 48h at 140℃ ~200℃. The optical absorption preoperties of the samples were characterized by UV-Vis,global tungsten oxide doped with tantalum powder prepared at 170℃ had an optimal optical absorption,and the average band gap and the specific surface area was 3. 73 eV. Morphology of the product cannot remain is found after sintering at high temperature.

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采用空气(或氧气)氧化法处理WC-Co硬质合金废料时,钴和钨将形成难溶于水的化合物钨酸钴。针对湿法分解钨酸钴的问题,分别对Co-W-H2O体系和Co-W-C-H2O体系进行了热力学分析,获得了一系列平衡关系图。结果表明,钨酸钴在中性溶液中可稳定存在,采用酸分解或碱分解的方式,均可使钨酸钴分解,并实现钨和钴的分离。碳酸盐分解钨酸钴的热力学趋势较大,分解反应可在较低的碳酸盐过量系数下完成。此外,溶液pH值对碳酸盐分解钨酸钴具有较大的影响。
When treating scraps WC-Co hard metal with oxygen or air, cobalt tungstate insoluble in water forms in the oxidation products. Thermodynamic equilibriums of Co-W-H 2O system and Co-W-C-H2O system were studied respectively obtaining a series of equilibrium diagrams to investigate issues related to hydrometallurgical decomposition of cobalt tungstate. The results show that cobalt tungstate is relatively stable in neutral solution. Cobalt tungstate can be decomposed by acid or alkali under certain conditions. Tungsten and cobalt can be separated at the same time. In addition, the decomposition reaction of cobalt tungstate with carbonate can be accomplished at lower excess coefficient of carbonate due to its strong thermodynamic tendency. Solution PH value has a remarkable effect on the reaction.

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采用磷钨酸和硝酸铜为原料合成磷钨酸铜,以磷钨酸铜为催化剂,H2O2为氧化剂应用于模拟油氧化脱硫反应。考察了不同的氧化脱硫体系、反应温度、催化剂质量、H2O2的体积和反应时间对脱硫效果的影响。结果表明,H2O2/磷钨酸铜/十六烷基三甲基溴化铵(CTAB)体系具有最高的脱硫率,当反应的温度为40℃,催化剂的质量为0.01g,H2O2加入体积为0.5mL,反应的时间为1h,二苯并噻吩的脱除率为93%,催化剂循环使用5次后,脱硫率没有明显下降。
Cpper phosphotungstate was synthesize by phosphotungstic acid and nitric acid copper as raw materials .Oxidative desulfurization reaction of model oil was studied by copper phosphotungstate as catalyst and H2 O2 as oxidant .The experiment indicate various oxidative desulfurization system ,reaction temperature ,catalytic amount ,amount of hydrogen peroxide and reaction time influenced on oxidative desulfurization effect .The results show that a combined copper phosphotungstate ,CTAB and H2 O2 could lead to a good conversion of DBT .Reaction temperature was 40 ℃ ,catalytic amount was 0 .01 g ,volume of hydrogen peroxide was 0 .5 mL ,reaction time was 1 h ,which made conversion rate of dibenzothiophene up to 93% . The catalyst may was recycled five times and desulfurization effecience of mode oil isn''t decreased .

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云南某钨锡矿含钨0.323%,锡0.140%,二氧化硅63.13%,三氧化二铝17.44%,氧化钙2.92%,氧化镁2.44%,在矿石工艺矿物学及试验研究的基础上,采用一段磨至-0.5mm,针对不同的床型,开展水力分级,进行摇床粗选,混合精矿脱硫、除铁、常温浮选分离钨锡的选矿工艺,获得了钨精矿产率0.31%,钨品位71.06%,钨回收率67.69%,含锡0.56%;锡精矿产率0.12%,锡品位58.18%,锡回收率50.94%,含钨3.80%,锡富中矿产率0.21%,锡品位4.22%,锡回收率6.87%,含钨2.69%,综合锡回收率57.81%的技术指标。
Experiments were carried out on one wolfram and tin ore which obtains tin (0 .140% ) ,silica (63 .13% ) ,aluminum oxide (17 .44% ) ,calcium oxide (2 .92% ) ,magnesium oxide (2 .44% ) in Yunnan . Based on the study on ore mineralogy and experimental study ,the ore was milled to -0 .5mm ,the process was as follows :firstly hydraulic separation was taken according to different type of beds ,then desulfidation and deironing were carried out ,after that separation of wolfram and tin was carried out by flotation at ordinary temperature .Productivities of concentrates of wolfram and tin are 0 .31% with wolfram (71.06% ) ,tin (0 .56% ) and 0 .12% with tin (58 .18% ) ,wolfram (3 .80% ) respectively .The recoveries of wolfram and tin are 67 .69% and 50 .94% in concentrates .Meanwhile productivity of middling of tin is 0 .21 with tin (4 .22% ) ,wolfram (2 .69% ) .The recovery of tin is 6 .87% in middling .Comprehensive recovery of tin is 57 .81% .

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以钨酸钠和硝酸铜为原料,通过水热合成反应及550℃/1.5 h焙烧得到氧化钨铜复合粉体,氢气还原后获得W-20%Cu复合粉体,采用X射线衍射(XRD)、扫描电镜(SEM)和高分辨透射电镜(HTEM),对该复合粉体的组织与结构进行表征。结果表明:采用水热合成法制备氧化钨铜的前驱体时混合溶液应调整为碱性,最好将pH值控制在9,水热反应产物主要是由CuWO4·2H2O与Cu2WO4(OH)2组成的复合络合物;550℃温度下焙烧时水热合成产物完全分解为由WO3、CuO和CuWO4-x组成的复合氧化物,粒度在2~5μm之间,分布均匀;复合氧化物在700~900℃下氢气还原成为典型的铜包钨结构的钨铜复合粉体,呈规则球形,晶粒度在70 nm左右,钨铜分布均匀,两相一体,保留了溶液中分子级的混合状态。
The W-Cu oxide precursor composite powders were fabricated by hydrothermal synthesis method and 550 ℃/1.5 h calcination using sodium tungstate and copper nitrate as raw materials, and the W-20%Cu composite powders were obtained through hydrogen reduction. The microstructures of the prepared powders were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM) and high-resolution transmission electron microscopy (HTEM). The results show that the mixed solution should be adjusted for alkaline;pH value should be controlled at 9 when the W-Cu oxide precursor is prepared by hydrothermal synthesis method. The hydrolyzates are mainly consist of CuWO4·2H2O and Cu2WO4(OH)2, and can be completely decomposed into the oxide composite powders composed of WO3, CuO and CuWO4-x when calcinating at 550℃. The oxide composite powders particles distribute uniformly, and the particle size is about 2~5μm. Moreover, W-Cu composite powders can be reduced at 700~900℃. The mor
试样以硫磷混酸溶解后,加盐酸使铁转化为氯化铁,首先用SnCl_2预还原大部分Fe~(3+)为Fe~(2+),然后用TiCl。定量还原剩余的Fe~(3+)为Fe~(2+),以钨酸钠作指示剂还原终点,即当Fe3+定量还原为Fe~(2+)后,过量一滴TiCl_3溶液时,可使作为指示剂的钨酸钠中的六价钨(无色)还原成蓝色的五价钨化合物,故溶液呈显蓝色。过量的TiCl_3可在硫酸铜的催化下,借水中溶解氧及空气中的游离氧氧化使钨蓝色泽褪去,从而消除过量TiCl_3还原剂的影响。避免了国标法及经典法的无汞测铁分析方法用重铬酸钾氧化过量TiCl_3时易引入的误差。在硫磷混酸介质中,以二苯胺磺酸钠为指示剂,用重铬酸钾标准溶液滴定全铁量,取得了令人满意的结果。
With the sample dissolved with Sulfuric-phosphoric mixed acid,SnCl2 was used to pre-deoxi-dize the most of Fe3+ into Fe2+.Then with sodium tungstate as an indicator,TiCl3 was used to quantita-tively reduce the remaining Fe3+ to Fe2+,and the exces TiCl3 could be oxidized by the oxygen dissolved in solution and free oxygen in air,under the catalyzing of copper sulfate, making its tungsten-blue luster fade,to eliminate the effect of the superfluous reducing agent TICl3, thus avoiding errors liable to induc-ting when potassium dichromate was used to oxidize superfluous TiCl3 in the mercury-free iron-determina-tion analytical methods in the State Stsndards and Classic Methods.In medium of sulfur-phosphor mixed acid,with diphenylamine-sodiun-sulfonic acid as an indicator,the standard solution of potassium dichro-mate was used to titrate the total iron content,the result being satisfactory.

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以双氧水为氧化剂、磷钨酸?半焦(HPW?Sc)为催化剂、N-甲基吡咯烷酮为萃取剂、Span60为乳化剂,对以苯并噻吩(BT)、二苯并噻吩(DBT)、4,6-二甲基二苯并噻吩(4,6-DMDBT)为模型含硫化合物的模拟油进行氧化脱硫研究,考察磷钨酸负载量、氧化温度、氧化反应时间和模拟油中烯烃、芳烃和含氮化合物对含硫化合物脱除效果的影响。结果表明:催化剂的最佳磷钨酸负载量(w)为30%;在反应时间为60 min、反应温度为60℃、HPW?Sc2用量(w)为1.0%、Span60用量(w)为0.36%、n(H2 O2)?n(S)=3的条件下,DBT脱除率可达到99%,含硫化合物的氧化活性由大到小的顺序为 DBT>4,6-DMDBT>BT;模拟油中的苯可促进 DBT的脱除,而喹啉和环己烯则抑制DBT的脱除。
Oxidative desulfurization of benzothiophene(BT,DBT and 4,6-DMDBT)in simulated oil was investigated using hydrogen peroxide as oxidant,Span60 as emulsifier,N-methyl pyrrolidone as ex-tractant and phosphotungstic acid?semi-coke (HPW?Sc)as catalyst.The HPW?Sc catalysts were charac-terized by FT-IR.The effect of HPW loading amount,reaction temperature,reaction time,and aromat-ics,olefins and nitrogen compounds on desulfurization rate was studied.The results show that the sul-fur removal efficiency of DBT reaches above 99% using the catalyst with 30% HPW loading at the con-ditions of temperature of 60 ℃,reaction time of 60 min,amount of catalyst 1.0%,n(H2O2)?n(S)=3, amount of Span60 emulsifier 0.36%,and the oxidative activity of the model sulfur compounds follows the order of DBT>4,6-DMDBT>BT. The benzene in the test oil can promote DBT desulfurization, while quinoline and cyclohexene inhibit the removal of DBT.

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