scholarly journals The Effect of Oxygen and Reduced Nickel on the Catalytic Action of Hydrogen Bromide in the Isomerization of Isostilbene into Stilbene

1937 ◽  
Vol 12 (11) ◽  
pp. 507-509 ◽  
Author(s):  
Yoshiyuki Urushibara ◽  
Osamu Simamura
Keyword(s):  
Hydrogen Bromide ◽  
Catalytic Action ◽  
Effect Of Oxygen

Radiolysis of aqueous 2,2,2-tribromoethanol solutions

1970 ◽  
Vol 48 (16) ◽  
pp. 2542-2548 ◽  
Author(s):  
V. G. Sorensen ◽  
V. M. Bhale ◽  
K. J. McCallum ◽  
R. J. Woods
Keyword(s):  
Carbon Dioxide ◽  
Dose Rate ◽  
Glycolic Acid ◽  
Hydrogen Bromide ◽  
Photochemical Decomposition ◽  
Bromide Ion ◽  
Presence And Absence ◽  
Effect Of Oxygen

Hydrogen bromide, glycolic acid, and carbon dioxide have been identified as products of the γ-radiolysis of aqueous 2,2,2-tribromoethanol solutions. The effect of oxygen, tribromoethanol concentration, and dose rate upon the yields of bromide ion and acid have been determined, and partial radiolysis mechanisms are proposed for reaction in the presence and absence of oxygen. Dibromoacetaldehyde, reported to be a product of the photochemical decomposition of tribromoethanol solutions, was not detected in the radiolysis experiments or in tribromoethanol solutions exposed to sunlight.

Radical reactions of p-nitrobenzylidene halides with aci-nitronate ions

1978 ◽  
Vol 31 (11) ◽  
pp. 2477 ◽  
Author(s):  
DJ Freeman ◽  
RK Norris ◽  
SK Woolfenden
Keyword(s):  
Nitrous Acid ◽  
Catalytic Effect ◽  
Lithium Salt ◽  
Phase Transfer ◽  
Hydrogen Bromide ◽  
Radical Reactions ◽  
Radical Process ◽  
Tetrabutylammonium Salt ◽  
Effect Of Oxygen ◽  
Radical Processes

The radical SRN1 and subsequent ERC1 reactions of p-nitrobenzylidene dibromide (2b) and bromide chloride (2c) with the lithium salt (1a) and the tetrabutylammonium salt (1b) (under phase-transfer conditions) of 2-nitropropane are discussed and compared with the reactions of the dichloride (2a). The SRN1 and ERC1 sequence occurs in rapid succession in the reaction of (2b), in contrast to the reactions of (2a) and (2c) which give isolable amounts of the SRN1 product, p-NO2C6H4CH(Cl)-CMe2NO2 (3a). The monobromide p-NO2C6H4CH(Br)CMe2NO2 (3b) cannot be detected in the SRN1-ERC1 sequence leading from (2b) to β,β-dimethyl-p-nitrostyrene (5). The ERC1 reaction of the monobromide (3b) is also studied and shown to take place more slowly than the combined SRN1-ERC1 sequence for (2b). ��� The phase-transfer technique is shown to be a convenient method for the preparation of C-alkylated derivatives like (3a), but not (3b), in both-the o- and p-nitrobenzylic systems. The dibromide p- NO2C6H4CH(Br)CMe2Br (7) was shown to undergo competitive ERC1 and E2(H) reactions with (1a) to give the styrene (5) and p-NO2C6H4C(Br)=CMe2 (8) respectively. Iodide ion reacts with (7) to give the styrene (5) by an E2(Br) mechanism at a rate which is several orders of magnitude slower than the radical process. Alkoxide ions gave E2(H) reactions on dibromide (7) and monochloride (3a) with elimination of the elements of hydrogen bromide and nitrous acid respectively. The catalytic effect of white light, the inhibitive effect of oxygen and p-dinitrobenzene, and the effect of concentration on the radical processes are discussed.

A TEM study of the effect of oxygen on nanocavity formation and precipitation in rapid - solidified Fe-16Ni-9Cr stainless steels

1994 ◽  
Vol 52 ◽  
pp. 700-701
Author(s):  
S. Wisutmethangoon ◽  
T. F. Kelly ◽  
J.E. Flinn
Keyword(s):  
Stainless Steels ◽  
High Mobility ◽  
Hot Extrusion ◽  
Extrusion Ratio ◽  
Gas Atomization ◽  
Cavity Formation ◽  
Nucleation Sites ◽  
Heat Treated ◽  
Different Types ◽  
Effect Of Oxygen

Vacancies are introduced into the crystal phase during quenching of rapid solidified materials. Cavity formation occurs because of the coalescence of the vacancies into a cluster. However, because of the high mobility of vacancies at high temperature, most of them will diffuse back into the liquid phase, and some will be lost to defects such as dislocations. Oxygen is known to stabilize cavities by decreasing the surface energy through a chemisorption process. These stabilized cavities, furthermore, act as effective nucleation sites for precipitates to form during aging. Four different types of powders with different oxygen contents were prepared by gas atomization processing. The atomized powders were then consolidated by hot extrusion at 900 °C with an extrusion ratio 10,5:1. After consolidation, specimens were heat treated at 1000 °C for 1 hr followed by water quenching. Finally, the specimens were aged at 600 °C for about 800 hrs. TEM samples were prepared from the gripends of tensile specimens of both unaged and aged alloys.

Application of pure, thermostable, alkali-tolerant xylanase in bleaching of oxygen-delignified pine kraft pulp

TAPPI Journal ◽  
2015 ◽  
Vol 14 (11) ◽  
pp. 689-694
Author(s):  
QINGZHI MA ◽  
QI WANG ◽  
CHU WANG ◽  
NIANJIE FENG ◽  
HUAMIN ZHAI
Keyword(s):  
Intrinsic Viscosity ◽  
Chlorine Dioxide ◽  
High Purity ◽  
Kraft Pulp ◽  
Alkaline Media ◽  
Industrial Scale ◽  
Elemental Chlorine ◽  
Effect Of Oxygen ◽  
Alkaline Tolerant ◽  
Ecf Bleaching

The effect of oxygen (O2)-delignified pine kraft pulp pretreatment by high-purity, thermostable, and alkaline-tolerant xylanases on elemental chlorine free (ECF) bleaching of O2-delignification kraft pulp was studied. The study found that xylanase pretreatment preserved the intrinsic viscosity and yield of O2-delignified pulp while causing about 7% of delignification with high delignification selectivity. The xylanases with high purity, higher thermostability (75°C~80°C) in highly alkaline media (pH 8.0~9.5) could be applied on an industrial scale. Pulp pretreatment by the high-purity, thermostable, and alkaline tolerant xylanases could improve pulp brightness or reduce the chlorine dioxide (ClO2) consumption. In a D0ED1D2 bleaching sequence using the same amount of ClO2, the xylanase-pretreated pulp obtained a higher brightness (88.2% vs. 89.7% ISO) at the enzyme dose of 2 U/g pulp; or for the same brightness as control (88.2% ISO), the ClO2 dosage in the D0 stage was reduced by 27%, which represents a 16% savings in total ClO2 used for bleaching.

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