Hydroxylamine

About: Hydroxylamine is a research topic. Over the lifetime, 6481 publications have been published within this topic receiving 115772 citations. The topic is also known as: nitrinous acid & aminol.

The anaerobic oxidation of ammonium

Abstract: From recent research it has become clear that at least two different possibilities for anaerobic ammonium oxidation exist in nature. 'Aerobic' ammonium oxidizers like Nitrosomonas eutropha were observed to reduce nitrite or nitrogen dioxide with hydroxylamine or ammonium as electron donor under anoxic conditions. The maximum rate for anaerobic ammonium oxidation was about 2 nmol NH4+ min-1 (mg protein)-1 using nitrogen dioxide as electron acceptor. This reaction, which may involve NO as an intermediate, is thought to generate energy sufficient for survival under anoxic conditions, but not for growth. A novel obligately anaerobic ammonium oxidation (Anammox) process was recently discovered in a denitrifying pilot plant reactor. From this system, a highly enriched microbial community with one dominating peculiar autotrophic organism was obtained. With nitrite as electron acceptor a maximum specific oxidation rate of 55 nmol NH4+ min-1 (mg protein)-1 was determined. Although this reaction is 25-fold faster than in Nitrosomonas, it allowed growth at a rate of only 0.003 h-1 (doubling time 11 days). 15N labeling studies showed that hydroxylamine and hydrazine were important intermediates in this new process. A novel type of hydroxylamine oxidoreductase containing an unusual P468 cytochrome has been purified from the Anammox culture. Microsensor studies have shown that at the oxic/anoxic interface of many ecosystems nitrite and ammonia occur in the absence of oxygen. In addition, the number of reports on unaccounted high nitrogen losses in wastewater treatment is gradually increasing, indicating that anaerobic ammonium oxidation may be more widespread than previously assumed. The recently developed nitrification systems in which oxidation of nitrite to nitrate is prevented form an ideal partner for the Anammox process. The combination of these partial nitrification and Anammox processes remains a challenge for future application in the removal of ammonium from wastewater with high ammonium concentrations.

Stimulation of guanylate cyclase by sodium nitroprusside, nitroglycerin and nitric oxide in various tissue preparations and comparison to the effects of sodium azide and hydroxylamine.

Abstract: Sodium nitroprusside, nitroglycerin, sodium azide and hydroxylamine increased guanylate cyclase activity in particulate and/or soluble preparations from various tissues. While sodium nitroprusside increased guanylate cyclase activity in most of the preparations examined, the effects of sodium azide, hydroxylamine and nitroglycerin were tissue specific. Nitroglycerin and hydroxylamine were also less potent. Neither the protein activator factor nor catalase which is required for sodium azide effects altered the stimulatory effect of sodium nitroprusside. In the presence of sodium azide, sodium nitroprusside or hydroxylamine, magnesium ion was as effective as manganese ion as a sole cation cofactor for guanylate cyclase. With soluble guanylate cyclase from rat liver and bovine tracheal smooth muscle the concentrations of sodium nitroprusside that gave half-maximal stimulation with Mn2+ were 0.1 mM and 0.01 mM, respectively. Effective concentrations were slightly less with Mg2+ as a sole cation cofactor. The ability of these agents to increase cyclic GMP levels in intact tissues is probably due to their effects on guanylate cyclase activity. While the precise mechanism of guanylate cyclase activation by these agents is not known, activation may be due to the formation of nitric oxide or another reactive material since nitric oxide also increased guanylate cyclase activity.

Ammonium removal by the oxygen-limited autotrophic nitrification-denitrification system

Abstract: The present lab-scale research reveals the potential of implementation of an oxygen-limited autotrophic nitrification-denitrification (OLAND) system with normal nitrifying sludge as the biocatalyst for the removal of nitrogen from nitrogen-rich wastewater in one step. In a sequential batch reactor, synthetic wastewater containing 1 g of NH4+-N liter−1 and minerals was treated. Oxygen supply to the reactor was double-controlled with a pH controller and a timer. At a volumetric loading rate (Bv) of 0.13 g of NH4+-N liter−1 day−1, about 22% of the fed NH4+-N was converted to NO2−-N or NO3−-N, 38% remained as NH4+-N, and the other 40% was removed mainly as N2. The specific removal rate of nitrogen was on the order of 50 mg of N liter−1 day−1, corresponding to 16 mg of N g of volatile suspended solids−1 day−1. The microorganisms which catalyzed the OLAND process are assumed to be normal nitrifiers dominated by ammonium oxidizers. The loss of nitrogen in the OLAND system is presumed to occur via the oxidation of NH4+ to N2 with NO2− as the electron acceptor. Hydroxylamine stimulated the removal of NH4+ and NO2−. Hydroxylamine oxidoreductase (HAO) or an HAO-related enzyme might be responsible for the loss of nitrogen.