This invention relates to treated geothermal brine compositions containing reduced concentrations of lithium, iron and silica compared to the untreated brines. Exemplary compositions contain concentration of lithium ranges from 0 to 200 mg/kg, concentration of silica ranges from 0 to 30 mg/kg, concentration of iron ranges from 0 to 300 mg/kg. Exemplary compositions also contain reduced concentrations of elements like arsenic, barium, and lead.

A method for removing silica from an aqueous solution is provided. The method includes steps of flowing the aqueous solution into an electro-Fenton reactor, wherein the reactor comprises one or more electrodes in a bipolar arrangement positioned between a monopolar iron anode and a monopolar cathode; applying an electric current to the aqueous solution such that silica aggregates form on ferric hydroxide; and removing the silica aggregates from the aqueous solution.

The highway sponge-type composite side ditch carbon neutralization system of the present invention includes three units, i.e., a silt pre-sedimentation channel, a filtering and oil-absorbing channel and an ecologic purification channel which are connected horizontally and successively. These three units work together to jointly complete the low-impact development functions of runoff collection, guide and drainage, purification and utilization, carbon emission is reduced by adopting various technical measures, the carbon sink effect is improved, and the full-life-cycle carbon neutralization effect from raw material production, construction to operation can be realized.

Methods, systems, and apparatus, relate to a method for carbon capture from sea water. A first source of sea water into a reverse osmosis chamber. Reverse osmosis is performed on the sea water to produce fresh water and brine. The brine is provided to an electrolyzer. A current is passed through the brine and fresh water, thereby producing a hydroxide solution in a cathode chamber of the electrolyzer. The hydroxide solution is collected and placed into a contacting chamber and new sea water introduced. Precipitates are produced comprising at least calcium carbonate and magnesium carbonate.

A method to improve the solid/solid separation of an amorphous aluminium trihydroxide containing suspension from a gypsum containing suspension in a saturated calcium sulphate solution without the need for a dewatering step following the solid-solid separation.

Systems and methods of gas-liquid contactors for direct ocean capture and/or direct air capture are described.

A method of treating contaminated water that has ferrous ions and at least one additional mineral in solution includes the steps of: adding a sufficient quantity of a caustic agent to the contaminated water to achieve a basic pH, and adding oxygen to the contaminated water to achieve a molar ratio of oxygen to ferrous iron of at least 1:10. The pH and the oxygen concentration are sufficient to produce ferrous hydroxide (Fe(OH).sub.2) from ferrous ions and ferric hydroxide (Fe(OH).sub.3) from the ferrous hydroxide while limiting colloidal iron formation, at least the ferric hydroxide forming a precipitate. The precipitate is separated from the contaminated water.

An ion recovery device including an ion selective permeable membrane with an ion conductive layer containing a lithium ion conductor formed of an inorganic substance, and a support layer is formed of a porous body wherein the ion selective permeable membrane has a configuration (I). In configuration (I) the ion conductive layer is provided in contact with one principal surface side of a support layer, and an electrode is provided in contact with another principal surface side opposite to the one principal surface side on which the ion conductive layer is provided.

The system for harvesting minerals from desalination brine includes a desalination module for receiving a stream of saltwater and producing a stream of purified water and a stream of desalination brine. A separator receives a first portion of the stream of desalination brine and separates monovalent ions from multivalent ions in the stream of desalination brine. The separator outputs a reject stream including the multivalent ions and a permeate stream including the monovalent ions. A membrane brine concentrator receives the permeate stream and produces a stream of lower concentration saltwater and a stream of higher concentration salt brine. The stream of lower concentration saltwater is mixed with the stream of saltwater received by the desalination module. A crystallizer receives the stream of higher concentration salt brine and produces a crystallized mineral product and a stream of bitterns.

Electrochemical water treatment devices are disclosed. The device includes a feed inlet fluidly connectable to a source of water including dissolved silica and a chlorine-containing compound and an electrochemical separation module fluidly connectable to the feed inlet. The electrochemical separation module includes a dilution compartment, a concentration compartment, an ion exchange membrane positioned between the dilution and concentration compartment, and first and second electrodes. A first portion of a volume of the dilution compartment includes a first ion exchange media positioned proximate to the feed inlet. A second portion of the volume of the dilution compartment includes a second ion exchange media positioned distal to the feed inlet. The first ion exchange media has a greater resistance to the chlorine-containing compound than the second ion exchange media. Methods of reducing a concentration of dissolved silica in water are disclosed. Methods of facilitating treatment of water containing dissolved silica are disclosed.