Pyrophoric material such as iron sulfide is frequently found in refinery equipment. When the equipment is opened to the atmosphere for maintenance, an exothermic reaction can take place that may cause injury to personnel and catastrophic damage to equipment. A process used to treat pyrophoric material uses sodium nitrite injected into a gaseous carrier stream to oxidize iron sulfides to elemental sulfur and iron oxides. The sodium nitrite solution may be buffered to a pH of about 9 with disodium phosphate or monosodium phosphate. A chemical additive that provides a quantitative measure of reaction completion may be added to the treatment solution.

Provided herein are pharmaceutically acceptable sodium nitrite and pharmaceutical compositions thereof. Also provided herein are methods for determining the total non-volatile organic carbon in a sodium nitrite-containing sample. Further provided herein are methods for producing pharmaceutically acceptable sodium nitrite. Still further provided herein are methods of treatment comprising the administration of pharmaceutically acceptable sodium nitrite.

Provided herein are pharmaceutically acceptable sodium nitrite and pharmaceutical compositions thereof. Also provided herein are methods for determining the total non-volatile organic carbon in a sodium nitrite-containing sample. Further provided herein are methods for producing pharmaceutically acceptable sodium nitrite. Still further provided herein are methods of treatment comprising the administration of pharmaceutically acceptable sodium nitrite.

Provided herein are pharmaceutically acceptable sodium nitrite and pharmaceutical compositions thereof. Also provided herein are methods for determining the total non-volatile organic carbon in a sodium nitrite-containing sample. Further provided herein are methods for producing pharmaceutically acceptable sodium nitrite. Still further provided herein are methods of treatment comprising the administration of pharmaceutically acceptable sodium nitrite.

Provided herein are pharmaceutically acceptable sodium nitrite and pharmaceutical compositions thereof. Also provided herein are methods for determining the total non-volatile organic carbon in a sodium nitrite-containing sample. Further provided herein are methods for producing pharmaceutically acceptable sodium nitrite. Still further provided herein are methods of treatment comprising the administration of pharmaceutically acceptable sodium nitrite.

An atomizing method comprises providing an atomizer including a mist generator and a plasma producer. The plasma producer includes a tube of dielectric material, an external electrode on an outside surface of the tube of dielectric material, an internal electrode on an inside surface of the tube of dielectric material, and a high-frequency power supply for applying a high-frequency voltage between the external electrode and the internal electrode. Mist from the mist generator is plasma-activated while passing through the tube of dielectric material and emitted from an end of the tube of dielectric material. The external electrode and the internal electrode are located such that location of the external electrode and location of the internal electrode does not overlap or merely partially overlap in the longitudinal direction of the tube of dielectric material. Peroxynitrous acid is continuously generated by generating hydrogen peroxide and nitrous acid using plasma-activated water mist.

The present disclosure relates to a system adapted to convert gaseous nitrous acid into gaseous nitric oxide. The system includes a catalytic converter and a nitric oxide analyzer. The catalytic converter includes a polytetrafluoroethylene tube and one or more concentric tubes or high surface substrates made of sulfonated tetrafluoroethylene-based fluoropolymer-copolymer positioned within the polytetrafluoroethylene tube.

The present disclosure provides autocatalytic cycles and chemical reactor systems in which the autocatalytic cycles may be conducted. Also provided are methods of identifying the autocatalytic cycles and methods of conducting the autocatalytic cycles, e.g., to produce a desired product. Regarding the methods of conducting the autocatalytic cycles, such a method comprises: carrying out a comproportionation reaction by reacting a first reactant M.sub.1 and a second reactant M.sub.2 to form a product M.sub.3, wherein M.sub.1, M.sub.2, and M.sub.3 each comprise at least one chemical element in common and the product M.sub.3 is produced in stoichiometric excess; and carrying out an auxiliary reaction by converting the product M.sub.3 to M.sub.1 or M.sub.2.

The present disclosure provides autocatalytic cycles and chemical reactor systems in which the autocatalytic cycles may be conducted. Also provided are methods of identifying the autocatalytic cycles and methods of conducting the autocatalytic cycles, e.g., to produce a desired product. Regarding the methods of conducting the autocatalytic cycles, such a method comprises: carrying out a comproportionation reaction by reacting a first reactant M.sub.1 and a second reactant M.sub.2 to form a product M.sub.3, wherein M.sub.1, M.sub.2, and M.sub.3 each comprise at least one chemical element in common and the product M.sub.3 is produced in stoichiometric excess; and carrying out an auxiliary reaction by converting the product M.sub.3 to M.sub.1 or M.sub.2.

Disclosed is an apparatus for conversion of ammonia into oxides of nitrogen which may comprise an adiabatic burner (108), a set of platinum/rhodium alloy catalytic gauzes (102A), (102B), and (102C), a waste heat recovery boiler (WHRB) (110), an absorption tower (302A), (302B), (302C), (302D) and (302E), a NaOH tank (306) and a surge tank (304). Further, the adiabatic burner may be configured to carry out catalytic oxidation of air and ammonia, using catalytic gauzes (102A), (102B), and (102C) of platinum/rhodium alloy. Further, the mixture of air and ammonia may be selectively oxidized to oxides of nitrogen, which may be absorbed in an alkali medium in the absorption tower (302A), (302B), (302C), (302D) and (302E), to yield sodium nitrites and nitrates.