# US 8,784,756 B2 · Process for the joint production of sodium carbonate and sodium bicarbonate > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 8,784,756 B2 - Document ID: US8784756B2 - Status: Granted - Kind: B2 - Application number: 13/139,430 - Filed: 2009-12-22 - Published: 2011-10-13 - Granted: 2014-07-22 - Earliest claimed: 2008-12-22 - Assignees: Solvay SA - Applicants: Jean-Paul Detournay; Francis M. Coustry; Perrine Davoine - Inventors: Jean-Paul Detournay; Francis M. Coustry; Perrine Davoine - Web page: https://patentgrep.com/patent/US8784756B2 ## CPC - C01D 7/00: Carbonates of sodium, potassium or alkali metals in general - C01D 7/126: {Multi-step processes, e.g. from trona to soda ash} - C01D 7/22: Purification - C01D 7/24: Crystallisation - C01D 7/26: by precipitation or adsorption - Y10T 428/2982: Particulate matter [e.g., sphere, flake, etc.] - C01D: COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM (metal hydrides {monoborane, diborane or addition complexes thereof} C01B6/00; salts of oxyacids of halogens C01B11/00; peroxides, salts of peroxyacids C01B15/00; sulfides C01B17/22; thiosulfates, dithionites, polythionates C01B17/64; compounds containing selenium or tellurium C01B19/00; binary compounds of nitrogen with metals C01B21/06; azides C01B21/08; {compounds other than ammonia and cyanogen, containing nitrogen and other non-metals C01B21/082}; metal amides C01B21/092; nitrites C01B21/50; phosphides C01B21/50; {compounds of noble gases C01B23/0005}; phosphides C01B25/08; salts of oxyacids of phosphorus C01B25/16; carbides C01B32/90; compounds containing silicon C01B33/00; compounds containing boron C01B35/00; cyanides C01C3/08; salts of cyanic acid C01C3/14; salts of cyanamide C01C3/16; thiocyanates C01C3/20) - Y10T: TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION ## Abstract A process for the joint production of sodium carbonate and sodium bicarbonate out of trona, comprising: introducing and dissolving crushed trona ore in a leaching tank containing a solution comprising sodium carbonate and sodium bicarbonate, saturated in sodium bicarbonate, in order to produce solid particles suspended in a production solution comprising sodium carbonate, the solid particles containing insoluble impurities and at least 65% in weight of sodium bicarbonate; separating the solid particles from the production solution containing sodium carbonate; drying and valorizing the separated solid particles; taking at least part of the production solution containing sodium carbonate out of the leaching tank in order to constitute a produced solution which is valorized; and introducing water in the leaching tank. ## Claims ### Claim 1 A process for separate valorization of sodium carbonate and sodium bicarbonate out of trona, comprising: introducing and dissolving crushed trona ore in a stirred leaching tank containing a dissolution solution comprising sodium carbonate and sodium bicarbonate, saturated in sodium bicarbonate, to produce solid particles suspended in a production solution comprising sodium carbonate, the solid particles containing at least 4% by weight of insoluble trona impurities and at least 65% in weight of sodium bicarbonate, wherein the temperature of said dissolution solution and of said production solution is at least 25° C.; separating the solid particles from the production solution containing sodium carbonate; drying and valorizing the separated solid particles; taking out at least part of the production solution containing sodium carbonate from the leaching tank to constitute a produced solution, said produced solution being valorized separately; and introducing an extraction water in the leaching tank, wherein the extraction water is pure fresh water or water comprising from 10 to 35 g/kg of sodium carbonate and/or from 70 to 100 g/kg of sodium bicarbonate. ### Claim 2 (depends on 1) The process according to claim 1, wherein said extraction water is introduced in the leaching tank with a weight ratio of said extraction water to sodium sesquicarbonate of the trona being at most 3.5. ### Claim 3 (depends on 1) The process according to claim 1, wherein the produced solution comprises at least 120 g/kg of sodium carbonate. ### Claim 4 (depends on 1) The process according to claim 1, wherein the solid particles contain at least 70% in weight of sodium bicarbonate. ### Claim 5 (depends on 1) The process according to claim 1, wherein the solid particles have a mean diameter D50 of at least 10 μm. ### Claim 6 (depends on 1) The process according to claim 1, wherein the solid particles have a mean diameter D50 of at most 38 μm. ### Claim 7 (depends on 1) The process according to claim 1, further comprising submitting the solid particles to a magnetic separation to separate and eliminate from them at least part of the insoluble trona impurities. ### Claim 8 (depends on 1) The process according to claim 1, wherein at least part of the produced solution is debicarbonated and introduced into a crystallizer to produce sodium carbonate crystals. ### Claim 9 (depends on 1) The process according to claim 1, further comprising: introducing at least part of the produced solution into less basic compartments of an electrodialyser comprising alternating less basic and more basic adjacent compartments separated from each other by cationic membranes, the more basic compartments being delimited by anionic faces of bipolar membranes on one side and by cationic membranes on the other side; and generating and extracting a solution comprising sodium bicarbonate from the less basic compartments of the electrodialyser, wherein this solution is afterwards cooled to produce a suspension comprising sodium bicarbonate crystals, and wherein the suspension is separated into valorized sodium bicarbonate crystals and a sodium bicarbonate mother liquor. ### Claim 10 (depends on 9) The process according to claim 9, further comprising: introducing water into the more basic compartments of the electrodialyser; producing a solution comprising sodium hydroxide into the more basic compartments, by combination of flux of sodium ions crossing the cationic membranes and flux of hydroxyl ions crossing the anionic faces of the bipolar membranes; and extracting a solution comprising sodium hydroxide from the more basic compartments. ### Claim 11 (depends on 10) The process according to claim 10, further comprising: introducing a solution comprising sodium carbonate and sodium bicarbonate into the more basic compartments of the electrodialyser; producing a solution comprising sodium hydroxide into the more basic compartments, by combination of the flux of sodium ions crossing the cationic membranes and the flux of hydroxyl ions crossing the anionic faces of the bipolar membranes; and extracting a solution enriched in sodium carbonate from the more basic compartments. ### Claim 12 (depends on 1) The process according to claim 1, further comprising: introducing at least part of the produced solution into less basic compartments of an electrodialyser comprising alternating less basic and more basic adjacent compartments separated from each other by cationic membranes, the more basic compartments being delimited by anionic faces of bipolar membranes on one side and by cationic membranes on the other side; decomposing at least part of the sodium bicarbonate contained in the less basic compartments of the electrodialyser into carbon dioxide and water; and extracting carbon dioxide and a solution comprising water from the less basic compartments of the electrodialyser. ### Claim 13 (depends on 8) The process according to claim 8, wherein the crystallizer is a monohydrate sodium carbonate crystallizer. ### Claim 14 (depends on 1) The process according to claim 1, wherein the solid particles comprise at least 6% by weight of insoluble trona impurities. ### Claim 15 (depends on 1) The process according to claim 1, wherein the solid particles contain at least 74% in weight of sodium bicarbonate. ### Claim 16 A process for separate valorization of sodium carbonate and sodium bicarbonate out of trona, comprising: introducing and dissolving crushed trona ore in a stirred leaching tank containing a dissolution solution comprising sodium carbonate and sodium bicarbonate, saturated in sodium bicarbonate, to produce solid particles suspended in a production solution comprising sodium carbonate, the solid particles containing at least 4% by weight of insoluble trona impurities and at least 65% in weight of sodium bicarbonate; separating the solid particles from the production solution containing sodium carbonate; drying and valorizing the separated solid particles; taking out at least part of the production solution containing sodium carbonate from the leaching tank to constitute a produced solution, said produced solution being valorized separately; and introducing an extraction water in the leaching tank, with a weight ratio of said extraction water to sodium sesquicarbonate of the trona of at most 3.5.