Effect of ammonia, ammonia‐water, and sulfuric acid on the HO 2  + HO 2  → H 2 O 2  + 3O 2 reaction in troposphere: Competition between stepwise and one‐step mechanisms

2020 ◽  
Vol 120 (23) ◽  
Author(s):  
Mingjie Wen ◽  
Xiru Cao ◽  
Yongqi Zhang ◽  
Meng Liang ◽  
Tianlei Zhang ◽  
...  
Keyword(s):  
2020 ◽  
Author(s):  
Jacob Rodriguez ◽  
Heemal Dhanjee ◽  
Stephen L. Buchwald

<div> <p>Amphiphilic ligands are valued for their ability to facilitate organometallic reactions in the presence of water. The regioselective sulfonation of a series of commercially available biaryl monophosphines to generate amphiphilic ligands is presented. In this one-step protocol, the temperature and addition of fuming sulfuric acid were carefully controlled to arrive at sulfonated biaryl monophosphine ligands in high yields with >95% regioselectivity without the need for chromatographic purification.</p> </div>


2008 ◽  
Vol 73 (6) ◽  
pp. 2450-2453 ◽  
Author(s):  
Gui-Rong Qu ◽  
Bo Ren ◽  
Hong-Ying Niu ◽  
Zhi-Jie Mao ◽  
Hai-Ming Guo

2011 ◽  
Vol 52 (46) ◽  
pp. 6103-6107 ◽  
Author(s):  
Sridhar Madabhushi ◽  
Narsaiah Chinthala ◽  
Venkata Sairam Vangipuram ◽  
Kondal Reddy Godala ◽  
Raveendra Jillella ◽  
...  

2007 ◽  
Vol 118 (1-2) ◽  
pp. 129-133 ◽  
Author(s):  
Kuiyi You ◽  
Bohua Wu ◽  
Liqiu Mao ◽  
Dulin Yin ◽  
Pingle Liu ◽  
...  

2013 ◽  
Vol 803 ◽  
pp. 9-12
Author(s):  
Zhen Xiu Wu ◽  
Zhao Hui Sun ◽  
Wen Long Chen ◽  
Guang Chao Du

The exploratory experiments of precipitating vanadium which simulated the process conditions in a vanadium plant with the indexes of vanadium loss and the cost were tested with industrial sulfuric acid and flue-gas sulfuric acid in laboratory, respectively. The technology optimizations were studied by selecting the experimental group with the lowest vanadium loss and cost. The results indicate that the vanadium loss and cost are the lowest by one-step vanadium precipitation with flue-gas sulfuric acid, and the optimum processes are as follows: the pH of solution is adjusted to 2.2 after adding the vanadium precipitation agent; the precipitation is proceeded 1 hour at 99°C or 100°C. The vanadium loss and cost per 1000 kg V2O3 are respectively 3.06 kg and 763.18 yuan by the optimum processes, which are much less than the processes with industrial sulfuric acid.


2007 ◽  
Vol 154 (9) ◽  
pp. K74 ◽  
Author(s):  
R. Hellin Rico ◽  
B. Du Bois ◽  
A. Witvrouw ◽  
C. Van Hoof ◽  
J.-P. Celis

2002 ◽  
Vol 116 (10) ◽  
pp. 4221-4227 ◽  
Author(s):  
I. Napari ◽  
M. Noppel ◽  
H. Vehkamäki ◽  
M. Kulmala

ChemInform ◽  
2012 ◽  
Vol 43 (9) ◽  
pp. no-no
Author(s):  
Madabhushi Sridhar ◽  
Chinthala Narsaiah ◽  
Vangipuram Venkata Sairam ◽  
Godala Kondal Reddy ◽  
Jillella Raveendra ◽  
...  

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