scholarly journals Nitrosamines and nitramines in Carbon Capture plants

2017 ◽  
Vol 28 (4) ◽  
pp. 43-50
Author(s):  
Tomasz Spietz ◽  
Szymon Dobras ◽  
Lucyna Więcław-Solny ◽  
Aleksander Krótki

Abstract The use of amine absorption in carbon capture technologies is related with the formation toxic and potentially carcinogenic amine degradation products such as nitrosamines and nitramines. These substances can be created within both the solvent and the atmosphere when air components (mainly NOx) and amines react with each other. These substances may pose environmental and health risks depending on the level and duration of the exposure. In this paper, formation and occurrence of nitrosamines and nitramines in carbon capture plants were described. Emission reducing technologies have been also mentioned. Furthermore, an overview of experimental data of emission of nitrosamines and other major degradation products has been pointed out.

1977 ◽  
Vol 38 (04) ◽  
pp. 0809-0822 ◽  
Author(s):  
Laurence A. Sherman

SummaryAlthough the site and manner of normal catabolism of most of the fibrinogen pool is uncertain, certain pathways have been defined for various fibrinogen derivatives. Several organs, including the kidneys and reticuloendothelial system (RES) have been directly implicated as catabolic sites for various fibrinogen derivatives. The catabolic sites are not the same for different derivatives. These differences in catabolism are probably in part related to biochemical differences between fibrinogen and its various derivatives. Fibrinogen itself may be catabolized in endothelial cells, although little experimental data is available. RES uptake of intact fibrinogen does not occur, and removal of sialic acid does not result in the rapid hepatic uptake seen with other desialop rote ins. In contrast, a variety of studies have shown that fibrin is taken up by the RES by at least 2 mechanisms. The first is phagocytosis of microparticulate fibrin. The second involves a RES cell membrane binding of soluble fibrin which remains soluble in the blood, when complexed to fibrinogen or degradation products. Fibrinogen degradation products alone may in part also be cleared in the RES. Fragments D and E appear to be catabolized in the kidney, although both the intrarenal site of catabolism and the means of cellular uptake is unknown. It is clear that normally there is no urinary excretion of D and E. Another fibrinogen derivative, low molecular weight clottable fraction 1–8, is derived in vivo from intact fibrinogen. 1–8 is found normally in the blood and has a shorter t ½ than fibrinogen although much longer than D and E. While originally thought to be the result of limited plasmin degradation, 1–8 may be the result of another type of proteolysis. The sites of both 1–8 formation and degradation are unknown. Catabolism via fibrin, 1–8, or D and E appears to be only a small percent of normal turnover, albeit of much greater significance in disease. The relationship of these pathways to the as yet unknown catabolic site for the bulk of normal fibrinogen remains to be determined.


2005 ◽  
Vol 347 (2) ◽  
pp. 234-243 ◽  
Author(s):  
Lijiang Song ◽  
John J. Morrison ◽  
Nigel P. Botting ◽  
Paul J. Thornalley

1975 ◽  
Vol 48 (2) ◽  
pp. 154-163 ◽  
Author(s):  
L. A. Wood ◽  
G. W. Bullman ◽  
F. L. Roth

Abstract The long-time creep of natural rubber cured with a conventional sulfur-accelerator recipe containing no filler can be conveniently shown near room temperature by a plot of ΔE/E1 with a double-abscissa scale, one marked in units of log t and the other in units of t. When experimental data from the present work and from previous studies reported in the literature are plotted in this manner it is noted that invariably the first scale yields a linear relation at short times and the second a linear relation at long times. The limiting linear relations just mentioned suggest the two-constant Equation (2), already proposed as a general creep equation for many materials. In the case of rubber the range of values of t investigated is from about 10 ms as studied by previous investigators to about 70 days in our work and other studies. Any significant deviations from the equation can be noted by inspection of the double-abscissa plot. We found that the equation furnished an excellent representation of almost all our experimental data up to the longest times. In one instance in our work and in a few other cases there was a prerupture increase of ΔE/E1 above the values given by the equation. This behavior can reduce somewhat the upper limit of validity of the general equation. The constants A and B can be evaluated from experimental observations of ΔE/E1 by solving two simultaneous equations obtained from the values at the longest time, at one minute, and at an intermediate time. In the present work, the constant A was essentially the same (about 2.4%/ (unit log t)) when the atmosphere surrounding the specimen was a vacuum, dry nitrogen, or dry air. The value was raised when the atmosphere was room air at 35% relative humidity and became about 4%/ (unit long t) when the air was saturated with water. The constant B was raised tenfold when the atmosphere was dry air instead of dry nitrogen. It was further increased by a factor of about 2, when the air was saturated. The value of B for the specimen in an atmosphere of stagnant room air was still greater than this by another factor of more than 2. It is possible that this atmosphere contained autocatalytic degradation products or other constituents which were removed when the air was bubbled through water or passed over CaCl2. The approximate boundaries of three different regions of time are determinable from the ratios A/B. In the first region, where t is less than 0.1(A/B), ΔE/E1 is approximately linear with log t. In the second region, where t is between 0.1(A/B) and 4.343 (A/B), ΔE/E1 is not linear with either log t or t. In the third region, where t is greater than 4.343 (A/B), ΔE/E1 is approximately linear with t. A fourth region of anomalous increase preceding rupture is sometimes found, especially when B is large.


2009 ◽  
Vol 64 (18) ◽  
pp. 4016-4023 ◽  
Author(s):  
Julianna A. Franco ◽  
David deMontigny ◽  
Sandra E. Kentish ◽  
Jilska M. Perera ◽  
Geoffrey W. Stevens

2013 ◽  
Vol 37 ◽  
pp. 759-768 ◽  
Author(s):  
Annette C. Rohr ◽  
Jacob D. McDonald ◽  
Dean Kracko ◽  
Melanie Doyle-Eisele ◽  
Stephanie L. Shaw ◽  
...  

2008 ◽  
Vol 57 (7) ◽  
pp. 1103-1110 ◽  
Author(s):  
E. Friedler ◽  
Z. Shwartzman ◽  
A. Ostfeld

This study analyses the reliability of an on-site MBR system for greywater treatment and reuse. To achieve this goal simulation was performed based on the IWA ASM1 model which was adapted to describe biological and physical mechanisms for MBR greywater treatment based systems. Model results were found to agree well with experimental data from an on site pilot greywater treatment plant, after which the calibrated model was used in a Monte Carlo mode for generating statistical data on the MBR system performance under different scenarios of failures and inflow loads variations. Effluents quality and their associated risks were successfully estimated.


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