NOVELTY - A system for recovering phosphorus from solid animal or municipal wastes comprises (i) a phosphorus extraction tank containing solid animal or municipal wastes, and (ii) a phosphorus removal tank in fluid communication with the extraction tank where the removal tank further comprises a system for removal of ammonia (NH3) from a liquid effluent (6) containing phosphorus and NH3 from the extraction tank.    USE - The systems are used for recovering phosphorus from solid animal or municipal wastes; treating a liquid effluent; reducing the concentration of NH3 from an anaerobic digester; reducing the concentration of NH3 in a wastewater tank; treating wastewater; and enriching irrigation water with NH3 (all claimed).    ADVANTAGE - Systems that remove NH3 and recover the nitrogen in a concentrated purified form are provided.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a system for treating a liquid effluent; (2) a system for reducing the concentration of NH3 from an anaerobic digester comprising (i) an effluent stream in fluid communication with an anaerobic digester, (ii) an anaerobic digester in fluid communication with the effluent stream where the digester comprises a membrane manifold system in fluid communication with a stripping solution tank to reduce the concentration of NH3 in the liquid effluent, (iii) a stripping solution tank in fluid communication with the digester where the tank comprises a stripping solution, and (iv) a pH measurement and acid addition dispenser in fluid communication with the stripping solution in the stripping solution tank, where the least reducing the concentration of NH3 increases the production of biogas by eliminating the toxicity of high NH3 concentration to methanogens; (3) a system for reducing the concentration of NH3 in a wastewater tank comprising (i) an effluent stream in fluid communication with a wastewater tank, (ii) a wastewater tank in fluid communication with the effluent stream and an anaerobic digestor where the tank comprises a membrane manifold system in fluid communication with a stripping solution tank where a raw waste stripped of NH3 is produced, and a mixer to reduce the concentration of NH3 in the liquid effluent, (iii) a stripping solution tank in fluid communication with the wastewater tank where the tank comprises a stripping solution, and (iv) an anaerobic digester in fluid communication with the wastewater tank where the NH3 stripped raw waste is transported from the wastewater tank to the anaerobic digester, where the reducing the concentration of NH3 increases the production of biogas by eliminating the toxicity of high NH3 concentration to methanogens; (4) a wastewater treatment system comprising (i) a wastewater tank in fluid communication with a deamonification tank through a flat microporous, hydrophobic gas-permeable membrane where the wastewater tank includes a mixer, a pH measurement and alkali addition dispenser, (ii) a flat microporous, hydrophobic gas-permeable membrane in fluid communication with the wastewater tank and the deamonification tank where the membrane forms a common partition between the tanks, (iii) a deamonification tank in fluid communication with the wastewater tank through a flat microporous, hydrophobic gas-permeable membrane where the deamonification tank includes a blower, a mixer, and a composition comprising a mixture of isolated bacteria selected from Nitrosomonas sp. strain HPNS.1, Mycetocola sp. strain HPNS.2, Chitinophaga sp. strain HPNS.3, Unclassified sp. strain HPNS.4, Castellaniella sp. strain HPSN.5, Sejongia sp. strain HPNS.6, Kalistella sp. strain HPNS.7, Pedobacter sp. strain HPNS.8, Nitrosomonas sp. strain HPNS.9 Comamonas sp. strain HPNS.10, Subtercola sp. strain HPNS.11, Coamonas sp. strain HPNS.12, Catellaniella sp. strain HPNS.13, Thermomonas sp. strain HPNS.14, Adhaeribacter sp. strain HPNS 15, and Comamonas sp. strain HPNS.15, of the High Performance Nitrifying Sludge Culture HPNS, deposited as NRRL deposit accession number NRRL B-50298 and Candidatus Brocadia caroliniensis, Isolate deposited as NRRL B-50286; and (5) a system for enriching irrigation water with NH3 comprising (i) a source of irrigation water in fluid communication with a wastewater tank, (ii) a wastewater tank containing NH3 containing liquid effluent in fluid communication with a source of irrigation water and a unit for irrigating plants where the wastewater tank includes a microporous hydrophobic gas-permeable membrane in fluid communication with the irrigation water and the unit for irrigating plants, (iii) a microporous hydrophobic gas-permeable membrane in fluid communication with the irrigation water and the unit for irrigating plants, and (iv) a unit for irrigating plants in fluid communication with the microporous hydrophobic gas-permeable membrane, where the membrane removes NH3 from the NH3 containing liquid effluent and the irrigation water in the membrane sweeps the NH3 to the unit for irrigation.    DESCRIPTION OF DRAWING(S) - The drawing shows a three dimensional schematic view of ammonia capture system.    Stripping solution (1)    Tank/reservoir (2)    Fluid pump (4)    Wastewater tank (5)    Liquid effluent (6)    Membrane (8)    Membrane pores (9)    Pump intake end (11)    Pump discharge end (12)    Membrane assembly (15)