Magnesium sulfate heptahydrate was made from salt lake magnesium chloride and sulfuric acid, then anhydrous magnesium sulfate was obtained from magnesium sulfate heptahydrate by dehydration, and finally high-purity ma...
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Magnesium sulfate heptahydrate was made from salt lake magnesium chloride and sulfuric acid, then anhydrous magnesium sulfate was obtained from magnesium sulfate heptahydrate by dehydration, and finally high-purity magnesia was prepared from anhydrous magnesium sulfate by natural gas reduction pyrolysis. The effects of pyrolysis temperature, pyrolysis time, particle size, and gas flow rate on the conversion rate of magnesium sulfate were investigated by single factor experiment. These experimental parameters were optimized by orthogonal experiment. The reduction pyrolysis product was analyzed and characterized by X-ray diffraction (XRD) and scanning electron microscopy (SEM). The optimal experimental parameters are as follows: the pyrolysis temperature is 1000°C, the pyrolysis time is 30 min, the particle size of anhydrous magnesium sulfate is 75 μm, and the flow rate of natural gas is 25 mL·min-1. The pyrolysis temperature is the main factor which influences the conversion rate. Under the optimal condition, the conversion rate of magnesium sulfate reaches 99.27%, and the purity of magnesia is 99.5%. The unimolecular MgO features well-distributed particle size, porous and fluffy surfaces, and high specific surface area.
Calcium oxide (CaO) was prepared by directly pyrolyzing the precursor called calcium carbonate (CaCO3), which was synthesized by solid-state ball milling reaction between NH4HCO3 and CaSO4·2H2O, the byproduct gen...
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Calcium oxide (CaO) was prepared by directly pyrolyzing the precursor called calcium carbonate (CaCO3), which was synthesized by solid-state ball milling reaction between NH4HCO3 and CaSO4·2H2O, the byproduct generated during the preparation of MnSO4. The effects of NH4HCO3-to- CaSO4·2H2O molar ratio, milling time, and ball-to-feed mass ratio on the conversion of CaSO4-2H2O were investigated respectively. The product was analyzed by X-ray diffraction and chemical analytical method. The reaction mechanism was also discussed. When the NH4HCO3-to-CaSO4-2H2O molar ratio is 3.5:1, the milling time is 40 min, and the ball-to-feed mass ratio is 5:1, the conversion rate of CaSO4-2H2O reaches 99.8%. Calcium oxide, whose purity is 99.2%, can be prepared by pyrolyzing the precursor at 1000°C for 1 h. The effectiveness of the solid-state reaction is improved by refining the reactant size, increasing the contact area, and providing necessary energy during the ball-milling process at ambient temperature.
Novel cobalt Fischer-Tropsch synthesis (FTS) catalysts were prepared from natural halloysite nanotubes (HNT) by double-solvent and wet- impregnation methods, and characterized by TEM, XRD, TPR and N2 adsorption-de...
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Novel cobalt Fischer-Tropsch synthesis (FTS) catalysts were prepared from natural halloysite nanotubes (HNT) by double-solvent and wet- impregnation methods, and characterized by TEM, XRD, TPR and N2 adsorption-desorption. Comparing with the catalyst prepared by wet- impregnation method, the catalyst prepared by double-solvent method reduces Co3O4 particle migration and agglomeration due to size-induced effect, thus showing higher catalytic activity for Fischer-Tropsch synthesis.
Residence time distribution (RTD) in twin-screw extruder is an important parameter for polymer processing. This work developed an improved apparatus for inline measurement of RTD in twin-screw extruder (TSE). The appa...
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ISBN:
(纸本)9781622760831
Residence time distribution (RTD) in twin-screw extruder is an important parameter for polymer processing. This work developed an improved apparatus for inline measurement of RTD in twin-screw extruder (TSE). The apparatus possessed many important advantages over those reported in the literatures. An important characteristic of the improved apparatus is to provide the possibility of calculating the local RTD because it allowed to simultaneously measuring RTDs at any two different locations of an extruder. Another significant application is to construct emulsification curves of polymer blend process in TSE by combining the concept of compatibilizer-tracer so that makes it possible for selecting most appropriate compatibilizers under real industrial polymer blending conditions as well as scaling up and optimizing blending processes.
Thermal decomposition kinetics of magnesite were investigated using non-isothermal TG-DSC technique at heating rate (β) of 15, 20, 25, 35, and 40 K min-1. The method combined Friedman equation and Kissinger equation ...
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Different shaped bismuth subcarbonate ((BiO)2CO3) nanostructures including irregular nanoplates, relatively uniform nanoplates and nanocubes were prepared and characterized by powder X-ray diffraction (XRD), scanning ...
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In this work, a series of NiMo/γ-Al 2 O 3 catalysts is prepared by one-pot method with controlled precipitation of AlCl 3 ·6H 2 O, (NH 4 ) 6 Mo 7 O 24 ·4H 2 O and NiCO 3 ·2Ni(OH) 2 ·4H 2 O using u...
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In this work, a series of NiMo/γ-Al 2 O 3 catalysts is prepared by one-pot method with controlled precipitation of AlCl 3 ·6H 2 O, (NH 4 ) 6 Mo 7 O 24 ·4H 2 O and NiCO 3 ·2Ni(OH) 2 ·4H 2 O using urea and ammonium carbonate as additives. The molar ratio of urea to Al varied from 4.1 to 17.2 and the influence of this parameter on the surface and structural properties of the catalysts and HDM activity was studied. HDM of Ni-TPP was carried out in a batch reactor. The catalysts were characterized by BET, XRD, H 2 -TPR, DRS, XPS, EDS, FT-IR, TG–DTA and NH 3 -TPD. The results show that urea employed as additive not only improves the solubility of Mo and Ni salt, but also adjusts the hydroxyl concentration and facilitates the formation of molybdate and polymolybdate. The existence of residual chlorine may improve the dispersion of the particles containing Ni and Mo on the surface of porous Al 2 O 3 , enhance hydrogen spillover and the acidity of the catalyst. HDM activity varied with the amount of urea to a maximum at urea/Al of 12.3 with activity of 98%. The highest activity occurred at this ratio is mainly due to better porosity, well dispersed active particles, increased octahedral molybdenum/nickel oxides and proper acidity.
[ Objective ] This study aimed to extract antibacterial peptides from mussel. [ Method ] Blue mussels were used as raw materials for direct extraction of antibacterial peptides by using O. 5 % acetic acid, and the ant...
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[ Objective ] This study aimed to extract antibacterial peptides from mussel. [ Method ] Blue mussels were used as raw materials for direct extraction of antibacterial peptides by using O. 5 % acetic acid, and the antibacterial peptides were isolated and purified by Sephacryl S-100 polyacrylamide gel chromatography. The fractions were collected for measurement of antibacterial activity and minimum inhibitory concentration for a variety of bacterial species by filter paper diffusion assay. Molecular weight of the antibacterial peptides was determined by SDS-PAGE. Variation of antibacterial activity of antibacterial peptides was measured at 100 ~C under conditions of different processing time and different pH. [ Result] The O. 5% acetic acid was used for crude extraction of antibacterial peptides as extrac- tion solution and led to relatively high extraction efficiency. By using Sephacryl S-100, the antibacterial peptides could be purified as a single substance. The isola- ted and purified antibacterial peptides of mussel had relatively strong antibacterial properties with molecular weight of 5 908, showing heat-resistance acid-alkaline resistance. [ Conclusion] This study laid the theoretical foundation for large-scale production of antibacterial peotides.
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