A composition having the structure of formula I:
[R—Ar—(COOH).sub.2].sub.x[Ar—(COOH).sub.3].sub.2-xM.sub.3.sup.2+  (I)
is provided where M is Mn, Cu, Co, Fe, Zn, Cd, Ni, or Pt; R is a bromine, nitro, a primary amine, C.sub.1-C.sub.4 alkyl secondary amine, C.sub.1-C.sub.4 alkyl oxy, Br—(C.sub.1-C.sub.4 alkyl), NO.sub.2—(C.sub.1-C.sub.4 alkyl), a mercaptan, and reaction products of any of the aforementioned with acyl chlorides of the formulas: CH.sub.3(CH.sub.2).sub.mC(O)Cl, or CH.sub.3(CH(C.sub.1-C.sub.4 alkyl)CH.sub.2).sub.mC(O)Cl, or CH.sub.3(CH.sub.2).sub.m-Ph-(CH.sub.2).sub.pC(O)Cl, where Ph is a C.sub.6 phenyl or C.sub.6 phenyl with one or more hydrogens replaced with F, C.sub.1-C.sub.4 fluoroalkyl, or C.sub.1-C.sub.4 perfluoroalkyl; m is independently in each occurrence an integer of 0 to 12 inclusive; p is an integer of 0 to 36 inclusive, to form an amide, a thioamide, or an ester; Ar is a 1,3,5-modified phenyl, and 1.4>x>0. A process of synthesis thereof and the use to chemically modify a gaseous reactant are also provided.

A composition having the structure of formula I:
[R—Ar—(COOH).sub.2].sub.x[Ar—(COOH).sub.3].sub.2-xM.sub.3.sup.2+  (I)
is provided where M is Mn, Cu, Co, Fe, Zn, Cd, Ni, or Pt; R is a bromine, nitro, a primary amine, C.sub.1-C.sub.4 alkyl secondary amine, C.sub.1-C.sub.4 alkyl oxy, Br—(C.sub.1-C.sub.4 alkyl), NO.sub.2—(C.sub.1-C.sub.4 alkyl), a mercaptan, and reaction products of any of the aforementioned with acyl chlorides of the formulas: CH.sub.3(CH.sub.2).sub.mC(O)Cl, or CH.sub.3(CH(C.sub.1-C.sub.4 alkyl)CH.sub.2).sub.mC(O)Cl, or CH.sub.3(CH.sub.2).sub.m-Ph-(CH.sub.2).sub.pC(O)Cl, where Ph is a C.sub.6 phenyl or C.sub.6 phenyl with one or more hydrogens replaced with F, C.sub.1-C.sub.4 fluoroalkyl, or C.sub.1-C.sub.4 perfluoroalkyl; m is independently in each occurrence an integer of 0 to 12 inclusive; p is an integer of 0 to 36 inclusive, to form an amide, a thioamide, or an ester; Ar is a 1,3,5-modified phenyl, and 1.4>x>0. A process of synthesis thereof and the use to chemically modify a gaseous reactant are also provided.

A reactor for oxidizing low concentrations of methane in air or other oxidizable fluid mixtures using a porous heat exchanger and a non-porous heat exchanger and an activation zone that allows the oxidation of very weak streams of methane in air or of other oxidizable fluid mixtures.

A reactor for oxidizing low concentrations of methane in air or other oxidizable fluid mixtures using a porous heat exchanger and a non-porous heat exchanger and an activation zone that allows the oxidation of very weak streams of methane in air or of other oxidizable fluid mixtures.

The present invention describes methods for absorbing a targeted chemical compound from a gas stream into a scrubbing solution for various uses and with various benefits. Methods are described to produce a gas stream that can be further processed with operational benefits, such as through condensing and wastewater treatment with a lower load on the wastewater treatment system. Methods are described for adsorbing the targeted compound with reduced condensation of water from the gas stream. Methods are described for producing a liquid stream comprising an absorbed form of the targeted compound for use as a saleable product, such as adsorbing ammonia for the production of a fertilizer, wherein the concentration of the absorbed form may be increased through reduced condensation from the gas stream. Methods are described for producing a lower volume liquid waste stream from the absorption process through the use of reduced condensation of the gas stream.

The present invention describes methods for absorbing a targeted chemical compound from a gas stream into a scrubbing solution for various uses and with various benefits. Methods are described to produce a gas stream that can be further processed with operational benefits, such as through condensing and wastewater treatment with a lower load on the wastewater treatment system. Methods are described for adsorbing the targeted compound with reduced condensation of water from the gas stream. Methods are described for producing a liquid stream comprising an absorbed form of the targeted compound for use as a saleable product, such as adsorbing ammonia for the production of a fertilizer, wherein the concentration of the absorbed form may be increased through reduced condensation from the gas stream. Methods are described for producing a lower volume liquid waste stream from the absorption process through the use of reduced condensation of the gas stream.

Methods and systems for converting ammonium waste streams into certifiably Organic ammonium salts having a variety of uses in greenhouse gas-reducing activities are herein described. The resulting ammonium salt compositions can be used to enhance crop yield.

Disclosed is a method for the removal of soluble particulate matter from a gas stream, such as urea dust from the off-gas of a finishing section of a urea production plant. The method comprises subjecting the off-gas to at least two quenching stages an aqueous quenching liquid. The quenching liquid used in a first, upstream quench stage, is allowed to have a higher concentration of dissolved particulate matter than the quenching liquid in the second, downstream quench stage. The quenched gas is led through a particle capture zone, typically comprising one or more of a wet scrubber, a Venturi scrubber, and a wet electrostatic precipitator.

Disclosed is a method for the removal of soluble particulate matter from a gas stream, such as urea dust from the off-gas of a finishing section of a urea production plant. The method comprises subjecting the off-gas to at least two quenching stages an aqueous quenching liquid. The quenching liquid used in a first, upstream quench stage, is allowed to have a higher concentration of dissolved particulate matter than the quenching liquid in the second, downstream quench stage. The quenched gas is led through a particle capture zone, typically comprising one or more of a wet scrubber, a Venturi scrubber, and a wet electrostatic precipitator.

Disclosed is a method for the removal of ammonia from the off-gas of a finishing section of a urea production plant. Also disclosed is a corresponding urea plant, and a method of accordingly modifying a pre-existing urea plant. In a scrubbing section, the off-gas is brought into contact with an acidic scrubbing liquid so as to provide a scrubbed off-gas and a utilized scrubbing liquid comprising ammonium salt. The method specifies an evaporation section, which is part of the urea plant that produces urea melt, that is divided into first and second stages. The first stage is part of the urea melt production plant. The second stage decoupled, as regards recirculation of liquids other than the urea product stream, from the urea melt production plant. This is accomplished by sending utilized scrubbing liquid that contains ammonium salts to the second stage evaporation section, and by sending condensed vapours from said second stage evaporation section to said scrubbing section.