C01F11/24

Biocementation Method and System

The invention is directed to kits, compositions, tools and methods comprising a cyclic industrial process to form biocement. In particular, the invention is directed to materials and methods for decomposing calcium carbonate into calcium oxide and carbon dioxide at an elevated temperature, reacting calcium oxide with ammonium chloride to form calcium chloride, water, and ammonia gas; and reacting ammonia gas and carbon dioxide at high pressure to form urea and water, which are then utilized to form biocement. This cyclic process can be achieved by combining industrial processes with the resulting product as biocement. The process may involve retention of calcium carbonate currently utilized in the manufacture of Portland Cement.

System and methods for removing minerals from a brine using electrodialysis

A method includes treating a first brine stream including a plurality of minerals with an anti-scalant to produce a treated brine. The first brine stream is provided by a wastewater treatment system. The method also includes directing the treated brine to a first nanofiltration (NF) system disposed downstream from and fluidly coupled to the wastewater treatment system, generating a first NF permeate stream and a first NF non-permeate stream from the treated brine in the first NF system, directing the first NF non-permeate stream to a mineral removal system disposed downstream from and fluidly coupled to the first NF system, and removing the plurality of minerals from the first NF non-permeate stream to generate a first overflow stream in the mineral removal system. The first overflow stream comprises at least a portion of the plurality of minerals. The method also includes routing a first portion of the first overflow stream to a hydrochloric acid (HCl) and sodium hydroxide (NaOH) production system disposed downstream from and fluidly coupled to the mineral removal system. The HCl and NaOH production system includes a second NF system that may receive the first portion of the first overflow stream and may generate a second brine stream from the first portion of the first overflow stream. The method further includes directing the second brine stream to a first electrodialysis (ED) system disposed within the HCl and NaOH production system and fluidly coupled to the second NF system. The first ED system may generate HCl and NaOH from the second brine stream.

System and methods for removing minerals from a brine using electrodialysis

A method includes treating a first brine stream including a plurality of minerals with an anti-scalant to produce a treated brine. The first brine stream is provided by a wastewater treatment system. The method also includes directing the treated brine to a first nanofiltration (NF) system disposed downstream from and fluidly coupled to the wastewater treatment system, generating a first NF permeate stream and a first NF non-permeate stream from the treated brine in the first NF system, directing the first NF non-permeate stream to a mineral removal system disposed downstream from and fluidly coupled to the first NF system, and removing the plurality of minerals from the first NF non-permeate stream to generate a first overflow stream in the mineral removal system. The first overflow stream comprises at least a portion of the plurality of minerals. The method also includes routing a first portion of the first overflow stream to a hydrochloric acid (HCl) and sodium hydroxide (NaOH) production system disposed downstream from and fluidly coupled to the mineral removal system. The HCl and NaOH production system includes a second NF system that may receive the first portion of the first overflow stream and may generate a second brine stream from the first portion of the first overflow stream. The method further includes directing the second brine stream to a first electrodialysis (ED) system disposed within the HCl and NaOH production system and fluidly coupled to the second NF system. The first ED system may generate HCl and NaOH from the second brine stream.

Fueling station sump dehumidifying system
10239745 · 2019-03-26 · ·

Systems and methods for preventing biocorrosion of fuel handling components located in a sump in a fuel dispensing environment. One method includes exposing a hygroscopic material to moisture-laden air in the sump such that the hygroscopic material deliquesces into a liquid solution and exposing a buffer material to ethanol-blended fuel vapors in the sump. The method also includes collecting the liquid solution in a reservoir and monitoring the level of the liquid solution in the reservoir using a liquid level sensor. Further, the method includes notifying service personnel of the level of the liquid solution in the reservoir.

Fueling station sump dehumidifying system
10239745 · 2019-03-26 · ·

Systems and methods for preventing biocorrosion of fuel handling components located in a sump in a fuel dispensing environment. One method includes exposing a hygroscopic material to moisture-laden air in the sump such that the hygroscopic material deliquesces into a liquid solution and exposing a buffer material to ethanol-blended fuel vapors in the sump. The method also includes collecting the liquid solution in a reservoir and monitoring the level of the liquid solution in the reservoir using a liquid level sensor. Further, the method includes notifying service personnel of the level of the liquid solution in the reservoir.

Sodium hydroxide production with carboxylic acid and sulfur dioxide intermediates
12030846 · 2024-07-09 · ·

The present application pertains to processes producing oxides using a weak acid intermediate. In one embodiment a material comprising calcium carbonate is reacted with a solution comprising aqueous carboxylic acid to form a gas comprising carbon dioxide and a solution comprising aqueous calcium carboxylate. The solution comprising aqueous calcium carboxylate is reacted with sodium sulfate to form a solution comprising aqueous sodium carboxylate and a solid comprising calcium sulfate. The solution comprising aqueous sodium carboxylate is reacted with sulfur dioxide to form sodium sulfite and an aqueous carboxylic acid. The sodium sulfite is separated from said aqueous carboxylic acid and reacted to form a solid comprising calcium sulfite which is decomposed to form calcium oxide and sulfur dioxide.

HEAT STORAGE IN CHEMICAL REACTORS
20240254377 · 2024-08-01 · ·

A process for producing olefins may include dehydrogenating a first alkane in a first reactor to produce a first effluent comprising at least one of a first n-olefin or a first diolefin; removing the first effluent from the first reactor; and regenerating the first reactor. The first reactor may include a first dehydrogenation catalyst and a first phase change material.

HEAT STORAGE IN CHEMICAL REACTORS
20240254377 · 2024-08-01 · ·

A process for producing olefins may include dehydrogenating a first alkane in a first reactor to produce a first effluent comprising at least one of a first n-olefin or a first diolefin; removing the first effluent from the first reactor; and regenerating the first reactor. The first reactor may include a first dehydrogenation catalyst and a first phase change material.

LIGNOSULFONATE COATED CALCIUM CHLORIDE
20190078004 · 2019-03-14 ·

Ice-melt compositions including calcium chloride coated with a lignosulfonate material are disclosed. The ice-melt compositions can be useful as ice-melt products with improved safety. Also disclosed are methods of melting ice using an ice-melt composition and methods of making an ice-melt composition.

LIGNOSULFONATE COATED CALCIUM CHLORIDE
20190078004 · 2019-03-14 ·

Ice-melt compositions including calcium chloride coated with a lignosulfonate material are disclosed. The ice-melt compositions can be useful as ice-melt products with improved safety. Also disclosed are methods of melting ice using an ice-melt composition and methods of making an ice-melt composition.