There is disclosed a process for debromination of novel brominated flame retardants (NBFRs) through co-pyrolysis with zinc oxide (ZnO) and franklinite (ZnFe.sub.2O.sub.4) to effectively restrict brominated species emission from NBFRs during thermal degradation. The method addresses environmental concerns by converting tetrabromobisphenol A 2,3-dibromopropyl ether (TBBPA-DBPE) and tetrabromobisphenol A diallyl ether (TBBPA-DAE) into bromine-free hydrocarbons. Utilizing Zn-based metal oxides from electrical arc furnace dust (EAFD), this process transforms them into metal bromides, facilitating selective zinc extraction. Thermogravimetric analysis guides pyrolysis at up to 500 C., revealing ZnO's efficacy in capturing 92% of HBr gas and producing minimal brominated compounds (relative area, 0.83%). Phenol emerges as a significant condensable product, while inorganic gases and methane dominates the non-condensable fraction. The retained metal bromides in pyrochar and <8% HBr gas emissions underscore ZnO's debromination potential. This method also suggests ZnO's application for dehalogenating other polymers and using spinel ferrites in combating brominated polymers.

The invention is directed toward non-wild-type organophosphorus acid anhydrolases having three site mutations, method of production, and method of use to effectively degrade toxic chemical compounds such as (Ethyl({2-[bis(propan-2-yl)amino]ethyl}sulfanyl)(methyl)phosphinate (VX).

The invention is directed toward non-wild-type organophosphorus acid anhydrolases having three site mutations, method of production, and method of use to effectively degrade toxic chemicals such as N,N-diethyl-2-(methyl-(2-methylpropoxy)phosphoryl)sulfanylethanamine) (VR).

A system and method for chemically destroying, degrading and incinerating a fluorocarbon or fluorinated material, such as perfluoroalkyl and polyfluoroalkyl substances (PFAS), with reduced emissions of gaseous PFC is provided. The method includes mixing the fluorinated material, a hydroxide base, and optionally a solvent system in a batch reactor to form a suspension. The PFAS and solvent system can be provided by AFFF. The reaction mixture is heated to a temperature ranging from about 25 C. to about 400 C. for about 0.5 hours to about 240 hours to defluorinate the fluorocarbons in the PFAS and produce a defluorinated waste product. More specifically, the method converts organic fluorine present in the PFAS to inorganic fluoride. Thus, the defluorinated waste product can be incinerated with reduced emissions of harmful gaseous PFCs.

A system and method for chemically destroying, degrading and incinerating a fluorocarbon or fluorinated material, such as perfluoroalkyl and polyfluoroalkyl substances (PFAS), with reduced emissions of gaseous PFC is provided. The method includes mixing the fluorinated material, a hydroxide base, and optionally a solvent system in a batch reactor to form a suspension. The PFAS and solvent system can be provided by AFFF. The reaction mixture is heated to a temperature ranging from about 25 C. to about 400 C. for about 0.5 hours to about 240 hours to defluorinate the fluorocarbons in the PFAS and produce a defluorinated waste product. More specifically, the method converts organic fluorine present in the PFAS to inorganic fluoride. Thus, the defluorinated waste product can be incinerated with reduced emissions of harmful gaseous PFCs.

A system and method for destroying and disposing a fluorinated material, such as PFAS, with reduced emissions of gaseous PFC is provided. The method can be applied to soil or other environmental media containing the PFAS, for example at the site of the soil, either in a batch reactor or in situ. The method can include mixing PFAS, a hydroxide base, and optionally a solvent in the batch reactor to form a suspension. The reaction mixture can be heated to a temperature of 25 C. to 400 C. for about 0.5 hours to 240 hours to defluorinate the corresponding PFAS fluorocarbons and produce a defluorinated waste product. Alternatively, the suspension can be maintained for a sufficient time at room temperature. The hydroxide base and optional solvent can also be sprayed on the PFAS and optionally heated. The method converts organic fluorine present in the PFAS contaminated soil to inorganic fluoride.

A system and method for destroying and disposing a fluorinated material, such as PFAS, with reduced emissions of gaseous PFC is provided. The method can be applied to soil or other environmental media containing the PFAS, for example at the site of the soil, either in a batch reactor or in situ. The method can include mixing PFAS, a hydroxide base, and optionally a solvent in the batch reactor to form a suspension. The reaction mixture can be heated to a temperature of 25 C. to 400 C. for about 0.5 hours to 240 hours to defluorinate the corresponding PFAS fluorocarbons and produce a defluorinated waste product. Alternatively, the suspension can be maintained for a sufficient time at room temperature. The hydroxide base and optional solvent can also be sprayed on the PFAS and optionally heated. The method converts organic fluorine present in the PFAS contaminated soil to inorganic fluoride.

Certain embodiments provide ligand-metal composite materials and compositions that could serve as catalyst-reductive agents to accelerate PFAS compounds defluorination. Certain embodiments provide optionally substituted 2,2-bipyridine and 1,10-Phenanthroline ligand coordinated zero-valent metal as described herein and their use for defluorinating PFAS compounds.

Certain embodiments provide ligand-metal composite materials and compositions that could serve as catalyst-reductive agents to accelerate PFAS compounds defluorination. Certain embodiments provide optionally substituted 2,2-bipyridine and 1,10-Phenanthroline ligand coordinated zero-valent metal as described herein and their use for defluorinating PFAS compounds.

Treatment systems and methods for capable of extracting or extracting and degrading trapped PCBs within a variety of building materials.