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chlorine dioxide相关的网络例句

查询词典 chlorine dioxide

与 chlorine dioxide 相关的网络例句 [注:此内容来源于网络,仅供参考]

Methods Quantitative disinfection experiments for an electrolyzed-oxidizing water with effective chlorine content of 2 mg/L and some disinfectants such as trichloro-isocyanuric acid,sodium hypochlorite and chlorine dioxide were carried out.

结果酸性电位水在1 min内的杀菌效果相当于含40 mg/L有效氯的三氯异氰尿酸或次氯酸钠及含30 mg/L有效氯的二氧化氯;随着消毒时间的延长,含氯消毒剂与酸性电位水杀菌效果的差别逐渐缩小,含20 mg/L有效氯的含氯消毒剂消毒5 min的消毒效果与酸性电位水相当。

The research result is as follow: The higher removal efficiency oncoliform in the seawater can be achieved by using chlorine dioxide as disinfectantthan sodium hypochlorite under the same dosage and reaction time, the removalefficiency of coliform can be achieved about 97.89% by using sodium hypochloritewith dosage of 3.0mg/L, and it can be achieved about 99.94% by chlorine dioxideunder the same dosage.

结果为:二氧化氯对海水中大肠菌群的去除率较次氯酸钠高,3.0 mg/L的次氯酸钠对海水中大肠菌群的去除率为97.89%,而相同浓度的二氧化氯对海水中大肠菌群的去除率则高达99.94%。

Under the condition of weak base, chlorine dioxide can oxidize cyanide into no poisonous cyanate, carbon dioxide and nitrogen.

在弱碱性条件下,二氧化氯消毒剂将氰化物氧化成无毒的氰酸盐、二氧化碳和氮气。

The advantage of supercritical carbon dioxide used as an environmental medium in polymerization and reactions in supercritical carbon dioxide are described. It includes homogeneous free radical polymerizations, precipitation free radical polymerizations, dispersion free radical polymerizations, emulsion and inverse emulsion free radical polymerizations, cationic polymerizations, ring-opening polymerization, melt-phase condensation polymerizations, sol-gel polymerizations, polymer blend synthesis, catalytic chain transfer polymerizations, oxidative coupling polymerization, nitroxide-mediated radical dispersion, atom-transfer radical polymerization, reversible addition-fragmentation chain transfer polymerization, electrochemical polymerization, simultaneous one-pot combination of enzymatic and chemical polymerization, copolymerization of carbon dioxide used as monomer.

评述了ScCO2作为聚合反应介质的优点,以及在ScCO2中可进行的聚合反应类型,包括均相聚合、沉淀聚合、分散聚合、乳液及反相乳液聚合、阳离子聚合、开环聚合、熔融态缩聚、溶液-凝胶聚合、聚合物混合合成、链催化转移聚合、氧化-偶合反应聚合、氮氧自由基可控活性聚合、原子转移自由基聚合、可逆加成-断裂链转移、电化学聚合、原子转移聚合与酶催化开环聚合两种活性聚合在ScCO2中同时聚合、二氧化碳作为原料共聚合等。

The disadvantage of ammonia and carbon dioxide- cyanamide method is the operation condition of this technology has very high request. Our team compares urea-cyanamide method with ammonia and carbon dioxide- cyanamide method, and then we get the conclusion: urea-cyanamide method is better than ammonia and carbon dioxide- cyanamide method.

为了比较两种新工艺的优劣,本课题组将两种工艺所得的收率,对环境的影响,催化剂,工艺条件,原料成本进行了比较,得出尿素-氰胺法优于氨气、二氧化碳-氰胺法的结论。

The device for separating and recovering the carbon dioxide from the flue gas by dry process consists of a powder grinding device, a powder feeding device, a fluidized bed, a cyclone separator and a regeneration device, wherein, a flue gas inlet is arranged at the bottom of the fluidized bed, the powder grinding device is communicated with the lower part of the fluidized bed by the powder feeding device, the upper part of the fluidized bed is communicated with the upper part of the cyclone separator by a pipe I, the top of the cyclone separator is provided with an outlet pipe for the flue gas containing low-concentration carbon dioxide, the bottom of the cyclone separator is communicated with the upper part of the regeneration device by a pipe II, the bottom of the regeneration device is communicated with the bottom of the fluidized bed by a pipe III, and the top of the regeneration device is provided with an outlet pipe for the flue gas containing high-concentration carbon dioxide.

本发明提供一种干法分离和回收烟气中二氧化碳的装置和方法,无需分离前对烟气进行降温,而直接在高温下进行二氧化碳的吸收分离,从而避免降温过程中的能量损失;器中干法分离和回收烟气中二氧化碳的装置,由磨粉装置、给粉装置、流化床、旋风分离器和再生装置组成,所述流化床底部有烟气入口,所述磨粉装置通过给粉装置与流化床下部连通,流化床的上部通过管道I与旋风分离器的上部相连通,旋风分离器的顶部有低二氧化碳浓度烟气出口管道,旋风分离器底部经过管道II与再生装置的上部连通,再生装置的底部通过管道III与流化床的底部相连通,再生装置顶部设有高浓度二氧化碳烟气出口管道。

Composition of suspension will chang from titanium monoxide to titanium dioxide during standstill procedure. Experimental results show that the proposed method can successfully prepare the anatase phase of titanium dioxide .In the photocatalysis experiment, the prepared titanium dioxide nanofluid absorbs the Ultraviolet when light wavelength was 360 to 380 nm. Adsorption experimental results show that the efficiency of absorbing methylene blue using TiO2 is higher than that for TiO2 (Degussa P-25) or ZnO. Depigmentation of methylene blue experimental using TiO2 can depigmentize methylene blue reach 100% in 60 min.

悬浮液所含之奈米颗粒在静置过程中,成份方面会由似一氧化钛转变为二氧化钛;在结晶组成方面,所制备之二氧化钛颗粒之结晶组成为锐钛矿结构;在光催化方面,所制备之奈米二氧化钛悬浮液在光波长360nm~380nm时产生吸收紫外光现象,在吸附实验中本制程所制备的二氧化钛颗粒的吸附效果优於商用的二氧化钛及氧化锌,在亚甲基蓝的脱色实验中本制程所制备的二氧化钛颗粒能在60分钟内达到脱色率100%。

Manganese dioxide is a familiar katalyst of oxidation reaction,there are five kinds of crystal configuration of manganese dioxide that have known, and different kinds of crystal configuration of manganese dioxide have the different catalysis and natural life.

二氧化锰是一种常见的氧化反应催化剂,现在已知二氧化锰有5种不同的晶型结构,不同晶型结构的二氧化锰的催化功能及寿命也不相同。

The invention relates to a middle-density pulp hydrogen dioxide dual-tower blanch method, which comprises:(1) washing and concentrating the pulp;(2) adding NaOH in 0.5-1.5%, sodium silicate in 0.5-3%, bitter salt in 0.05-0.5% and barium dioxide in 1.0-2.5%,, and adding slurry to 70-100Deg. C;(3) 1# blanch tower blanches, while the temperature is 70-100Deg. C, and the reaction time is 30-90mins;(4) 2# blanch tower blanches, while adds barium dioxide in 0.5-1.5% and some blanch agent, while keeps the temperature in 70-100Deg. C and the reaction time is 30-90mins;(5) adding water, and washing to attain blanch slurry.

本发明公开一种中浓纸浆过氧化氢双塔漂白方法,包括(1)纸浆洗涤浓缩;(2)加入绝干浆重量的0.5~1.5%NaOH、0.5~3%硅酸钠、0.05~0.5%硫酸镁和1.0~2.5%过氧化氢等,将纸浆加热至70~100℃;(3)1#漂白塔漂白:温度为70~100℃,反应时间为30~90分钟;42#漂白塔漂白:补加0.5~1.5%的过氧化氢及适量漂白助剂,保持温度70~100℃,反应30~90分钟;(5)加水稀释、经洗涤后得漂白浆。

The present dissertation deals with:(1) Exploring the feasibility of the CO〓 methanation and the conversion CH〓/H〓 into C〓 hydrocarbons under plasma with catalyst at ambient temperature and atmosphere.(2) Designing a reactor and preparing some catalysts suited for the conversion of carbon dioxide via the cooperation effect of plasma and catalysts.(3) Optimizing reaction conditions of conversion carbon dioxide to C〓 hydrocarbons in the proposed process.(4) Studying the reaction mechanism of conversion carbon dioxide to C〓 hydrocarbons under plasma by using in situ OES technology.(5) By the results of characterizing coked catalysts, exploring the reasons that result in the coking of catalyst and the paths for decreasing the deposit in the catalyst under plasma.(6) Analyzing the energy efficiency of the plasma catalysis and exploring the paths for improving the energy efficiency.

论文的主要研究工作包括:(1)探索脉冲电晕等离子体与催化剂共同作用CO〓/H〓甲烷化和由CH〓/H〓合成C〓烃反应的可行性;(2)研制等离子体催化CO〓转化的反应器和适配的催化剂;(3)优化等离子体催化CO〓转化制C〓烃反应的工艺条件和电参数;(4)利用原子发射光谱原位技术对等离子体反应的诊断结果,对等离子体催化CO〓转化制C〓烃反应的机理进行推断;(5)通过对积碳催化剂的表征结果,分析积碳的类型及其成因,并探讨减少积碳的途径;(6)通过对等离子体催化CO〓转化制C〓烃反应能量效率的分析,探讨提高等离子体催化反应能量效率的途径。

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