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根据Na2SO4 - H2O2 - NaCl加合物生产工艺和控制要求,结合生产实践,从工艺路线、设备选型、工艺控制等方面进行了探讨.提出了Na2SO4 - H2O2 - NaCl加合物工业化生产技术优化方案. 相似文献
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根据Na2s04-H2O2-NaGl加合物生产工艺和控制要求,结合生产实践,从工艺路线、设备选型、工艺控制等方面进行了探讨。提出了Na2SO4-H202-NaCl加合物工业化生产技术优化方案。 相似文献
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极端嗜盐绿色杜氏藻是世界上迄今发现的最耐盐的真核光合生物,藻体内含有植物蛋白、脂肪酸、多糖、叶绿素、甘油等多种营养成分和生物活性物质,具有开发天然保健品或生物药品的应用前景、文章依据人工海水理论和方法,研究了水体Na+/Mg2+、Cl-/SO2-4比值对极端嗜盐绿色杜氏藻生长的影响,从而探讨适合该藻类生长的化学环境. 相似文献
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通过定量研究磨木木素色团在Na2SO3处理及H2o2漂白中的发色效果,揭示木素在CTMP化学预处理及漂白过程中的发色行为.研究发现,邻醌和邻酚金属螯合物是Na2SO3处理及H2O2漂白木素的主要颜色来源,共轭羰基对木素颜色不构成主要影响;限制金属离子的引入,可有效地提高CTMP浆的漂白性能. 相似文献
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木素在Na2SO3处理及H2O2漂白中的发色行为 总被引:1,自引:0,他引:1
通过定量研究磨木木素色团在Na2SO3处理及H2O2漂白中的发色效果,揭示木素在CTMP化学预处理及漂白过程中的发色行为。研究发现,邻醌和邻酚金属螯合物是Na2SO3处理及H2O2漂白木素的主要颜色来源。共轭羰基对木素颜色不构成主要影响;限制金属离子的引入,可有效地提高CTMP浆的漂白性能。 相似文献
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以Na2SiO3为活性物质,以纳米Fe3O4为磁核制备磁性固体碱催化剂Na2O·SiO2/Fe3O4,通过正交实验,得到催化剂的最佳制备条件为:硅与铁的摩尔比2.5,晶化时间2h,煅烧温度350℃,煅烧时间2.5h,并通过震动样品磁强计(VSM)对催化剂的磁性进行表征。结果表明,所制备的催化剂Na2O·SiO2/Fe3O4具有较好的磁性和顺磁性,抗水性能优于传统均相碱催化剂;将其应用于棉籽油酯交换反应制备脂肪酸甲酯的最优工艺参数为:醇油摩尔比7:1,催化剂加入量5%,反应温度65℃,反应时间1h,搅拌速度400r/min,在此条件下,催化棉籽油酯交换反应转化率为99.6%,连续使用11次后活性仍在90%以上。 相似文献
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Induction of pitting corrosion on stainless steel (grades 304 and 316) used in dairy industry by biofilms of common sporeformers 下载免费PDF全文
This study hypothesised that there may be induction of pitting corrosion or microbially‐induced corrosion on stainless steel (SS) dairy‐processing surfaces by biofilms of common milk sporeformers such as Bacillus sporothermodurans and Geobacillus stearothermophilus. Scanning electron microscopy (SEM) and micrographs generated from energy‐dispersive spectroscopy were used to observe pitting corrosion and to find the elemental composition and distribution on the control and pitted surfaces. From SEM images and energy‐dispersive spectroscopy micrographs, it was observed that pitting corrosion on SS could be induced by biofilms of both B. sporothermodurans and G. stearothermophilus. 相似文献
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对Φ10.70mm0Cr17Ni4Cu4Nb(SUS630)马氏体沉淀硬化型不锈钢丝冷变形过程中易出现拉拔断裂、拉拔后自裂以及冷变形困难进行工艺分析和探讨,指出钢丝表面状态不佳是影响拉拔的主要原因。通过细晶表面处理技术,拉拔时选择道次压缩率8%~12%,使钢丝表面处于压应力状态;盘条热处理采用(1040±10)℃保温1h加上(630±10)℃保温4h时效,中间去应力退火采用(640±10)℃保温2~4h,成品前去应力退火采用(630±10)℃保温4h时效,生产出的Φ10.70mm直条钢丝平均抗拉强度1030MPa,延伸率16.4%,硬度HRC值为31,满足GB/T1220—2007要求,用户使用反映良好。 相似文献
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In a laboratory-based test series, seven experiments along a simulated Pacific hydrotherm at 152 degrees W, 40 degrees N were carried out to measure the rise velocities of liquefied CO2 droplets under (clathrate) hydrate forming conditions. The impact of a hydrate skin on the rising behavior was investigated by comparing the results with those from outside the field of hydrate stability at matching buoyancy. A thermostatted high-pressure tank was used to establish conditions along the natural oceanic hydrotherm. Under P-/T-conditions allowing hydrate formation, the majority of the droplets quickly developed a skin of CO2 hydrate upon contact with seawater. Rise rates of these droplets support the parametrization by Chen et al. (Tellus 2003, 55B, 723-730), which is based on empirical equations developed to match momentum of hydrate covered, deformed droplets. Our data do not support other parametrizations recently suggested in the literature. In the experiments from 5.7 MPa, 4.8 oC to 11.9 MPa, 2.8 degrees C positive and negative deviations from predicted rise rates occurred, which we propose were caused by lacking hydrate formation and reflect intact droplet surface mobility and droplet shape oscillations, respectively. This interpretation is supported by rise rates measured at P-/T-conditions outside the hydrate stability field atthe same liquid CO2-seawater density difference (delta rho) matching the rise rates of the deviating data within the stability field. The results also show that droplets without a hydrate skin ascend up to 50% faster than equally buoyant droplets with a hydrate skin. This feature has a significant impact on the vertical pattern of dissolution of liquid CO2 released into the ocean. The experiments and data presented considerably reduce the uncertainty of the parametrization of CO2 droplet rise velocity, which in the past emerged partly from their scarcity and contradictions in constraints of earlier experiments. 相似文献
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In coastal areas, strong complexation of copper generally reduces its toxicity; our ability to monitor and regulate copper as a toxin therefore depends on our understanding of the sources and sinks of the copper-binding ligands. Terrestrial humic substances (HS) are well-recognized contributors to weak ligand concentrations in aquatic systems. In this work, we show that HS are likely contributors to both stronger and weaker ligand classes controlling copper speciation in coastal areas receiving typical inputs of terrestrial organic matter. We used competitive ligand exchange adsorptive cathodic stripping voltammetry (CLE-ACSV), with the added ligands benzoylacetone and salicylaldoxime, to examine copper binding by terrestrial HS in a seawater matrix, at HS and copper concentrations typical of coastal waters. Copper titration data of 1 mg/L Suwannee River humic acid (SRHA) in seawater could be modeled using conditional stability constants of 10(12.0) and 10(10.0) and total ligand concentrations of 10.4 and 199 nM for a stronger and weaker ligand, respectively. Similar results were obtained for Suwannee River fulvic acid (SRFA). Strong copper binding by SRFA in seawater was weaker than previously reported for a freshwater at similar pH, possibly indicating effects of Ca and Mg competition or ionic strength. Nevertheless,the concentrations and binding strengths of copper ligands we observed are comparable to the range reported in previous coastal speciation studies. In addition, we show that the weaker copper ligands cause internal calibration techniques to significantly underestimate the sensitivity of ACSV in the presence of HS concentrations typical of coastal waters. To address this issue, we demonstrate the use of "overload titrations", using a high enough concentration of added ligand to outcompete all natural ligands as an alternative calibration technique for analysis of coastal samples. 相似文献
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研究了以非离子型微乳液乳化剂-OP/n-C4H9OH/n-C7H16/H2O为介质,Ni(Ⅱ)与1-(2-吡啶偶氮)-2-萘酚(PAN)的显色反应,在pH值8.58~10.70范围内,配合物的最大吸收波长为570nm,回归方程:A=0.0313c-0.0066(c/μg·25mL-1),相关系数r=0.9996,表观摩尔吸光系数为4.56×104L/mol·cm,Ni(Ⅱ)浓度在0.2μg/25mL~25μg/25mL范围内服从比尔定律,检出限0.2μg/25mL,相对标准偏差(RSD%)在0.014%~0.64%之间,加标回收率在95.00%~110.9%之间。该法用于合成样和不锈钢餐具浸泡液中镍的测定,结果令人满意。 相似文献
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1 前言目前国内生产食用盐普遍采用两种生产方法 ,其一是真空蒸发结晶工艺 ,其二是利用原盐进行粉碎、洗涤、干燥的生产工艺 ,简称粉洗干工艺。在粉洗干生产工艺中粉碎机是关键设备 ,目前粉碎机使用最多和效果最好的是对辊式粉碎机、其优点是两粉碎磨辊间隙可以调节 ,使得粉碎盐粒度可以调节 ,能够适应市场对多品种的要求。粉碎磨辊拆卸方便 ,并可以经过多次拉丝反复使用 ,确保生产的经济性。2 不锈钢粉碎磨辊的开发研制对辊式粉碎机粉碎磨辊绝大多数采用双层复合式离心铸造 ,内层为灰口铸铁或球墨铸铁 ,外层为硬质合金铸铁 ,主要成分是镍… 相似文献