An electroplating wastewater treatment method includes steps of: (A) crushing the straws into particles, stirring and mixing the crushed straw particles with the electroplating wastewater, and obtaining a mixture, wherein 40-50 g of straw particles are added into each liter of the electroplating wastewater; (B) mixing the seawater with the red mud, adjusting a pH value in a range of 8.5-9.5, filtering after standing, and obtaining a filtrate, wherein: a weight of the red mud which is added into the seawater is 200-300 g per liter seawater; (C) ultrasonically mixing the mixture in step (A) with the filtrate in step (B), standing, and then ultrasonically mixing, and then filtering after standing; and (D) adjusting a pH value of the filtrate obtained in step (C) to 7.

An apparatus (100) for purifying fluid, wherein the apparatus (100) comprises an osmosis unit (102) configured for pre-purifying the fluid to be purified by forward osmosis of the fluid, which is to be purified, through an osmosis membrane (104) into a chamber (106) comprising dissolved first ions, in particular first cations and first anions, an ion exchange unit (108) configured for exchanging at least part of the first ions, in particular at least part of at least one of the first cations and the first anions, by second ions, in particular at least one of second cations and second anions, and a re-concentration unit (110) configured for separating the pre-purified fluid after the ion exchange into purified fluid and into a re-concentrate enriched with the respective ions, in particular anions and cations.

An apparatus (100) for purifying fluid, wherein the apparatus (100) comprises an osmosis unit (102) configured for pre-purifying the fluid to be purified by forward osmosis of the fluid, which is to be purified, through an osmosis membrane (104) into a chamber (106) comprising dissolved first ions, in particular first cations and first anions, an ion exchange unit (108) configured for exchanging at least part of the first ions, in particular at least part of at least one of the first cations and the first anions, by second ions, in particular at least one of second cations and second anions, and a re-concentration unit (110) configured for separating the pre-purified fluid after the ion exchange into purified fluid and into a re-concentrate enriched with the respective ions, in particular anions and cations.

A water purification chamber is provided. In one embodiment, a system comprises a purification chamber comprising a selective adsorbent activated carbon fiber fabric including one or more selective functional groups that bind arsenic.

A water softening ball for generating softened water by immersing it in water is provided, comprising a shell having a generally hollow ellipsoidal shape, wherein a plurality of openings are formed in the shell for the inside and the outside of the shell to communicate; and a filter unit included within the shell and comprising an ion exchange resin. The ellipsoidal shape includes a spherical shape.

A water softening ball for generating softened water by immersing it in water is provided, comprising a shell having a generally hollow ellipsoidal shape, wherein a plurality of openings are formed in the shell for the inside and the outside of the shell to communicate; and a filter unit included within the shell and comprising an ion exchange resin. The ellipsoidal shape includes a spherical shape.

Cross-linked cyclopolymeric resins from N,N-diallyl quaternary ammonium monomers and tetrallylpiperazinium cross-linking monomer or salts, solvates, tautomers or stereoisomers as adsorbent materials for the removal of heavy metals from aqueous solution. A process for producing the cross-linked cyclopolymeric resins by Butler cyclocopolymerization of the monomers with a free radical initiator. The cross linked cyclopolymeric resins are polyzwitterionic or polyzwitterionic and dianionic and feature repeating units with multiple chelating centers that heavy metal ions can bind to. In addition, a method for removing heavy metals from aqueous solution via contacting and treatment with the cross-linked cyclopolymeric resins.

Cross-linked cyclopolymeric resins from N,N-diallyl quaternary ammonium monomers and tetrallylpiperazinium cross-linking monomer or salts, solvates, tautomers or stereoisomers as adsorbent materials for the removal of heavy metals from aqueous solution. A process for producing the cross-linked cyclopolymeric resins by Butler cyclocopolymerization of the monomers with a free radical initiator. The cross linked cyclopolymeric resins are polyzwitterionic or polyzwitterionic and dianionic and feature repeating units with multiple chelating centers that heavy metal ions can bind to. In addition, a method for removing heavy metals from aqueous solution via contacting and treatment with the cross-linked cyclopolymeric resins.

A water softening ball for generating softened water by immersing it in water is provided, comprising a shell having a generally hollow ellipsoidal shape, wherein a plurality of openings are formed in the shell for the inside and the outside of the shell to communicate; and a filter unit included within the shell and comprising an ion exchange resin. The ellipsoidal shape includes a spherical shape.

Cross-linked cyclopolymeric resins from N,N-diallyl quaternary ammonium monomers and tetrallylpiperazinium cross-linking monomer or salts, solvates, tautomers or stereoisomers as adsorbent materials for the removal of heavy metals from aqueous solution. A process for producing the cross-linked cyclopolymeric resins by Butler cyclocopolymerization of the monomers with a free radical initiator. The cross linked cyclopolymeric resins are polyzwitterionic or polyzwitterionic and dianionic and feature repeating units with multiple chelating centers that heavy metal ions can bind to. In addition, a method for removing heavy metals from aqueous solution via contacting and treatment with the cross-linked cyclopolymeric resins.