644results about "Carbonate preparation" patented technology

Processes are described for the extraction and recovery of alkali metal from the char that results from catalytic gasification of a carbonaceous material. Among other steps, the processes of the invention include a hydrothermal leaching step in which a slurry of insoluble particulate comprising insoluble alkali metal compounds is treated with carbon dioxide and steam at elevated temperatures and pressures to effect the conversion of insoluble alkali metal compounds to soluble alkali metal compounds. Further, processes are described for the catalytic gasification of a carbonaceous material where a substantial portion of alkali metal is extracted and recovered from the char that results from the catalytic gasification process.

Apparatuses and methods for removing carbon dioxide and other pollutants from a gas stream are provided. The methods include obtaining hydroxide in an aqueous mixture, and mixing the hydroxide with the gas stream to produce carbonate and/or bicarbonate. Some of the apparatuses of the present invention comprise an electrolysis chamber for providing hydroxide and mixing equipment for mixing the hydroxide with a gas stream including carbon dioxide to form an admixture including carbonate and/or bicarbonate.

A method of sequestering a greenhouse gas is described, which comprises: (i) providing a solution carrying a first reagent that is capable of reacting with a greenhouse gas; (ii) contacting the solution with a greenhouse gas under conditions that promote a reaction between the at least first reagent and the greenhouse gas to produce at least a first reactant; (iii) providing a porous matrix having interstitial spaces and comprising at least a second reactant; (iv) allowing a solution carrying the at least first reactant to infiltrate at least a substantial portion of the interstitial spaces of the porous matrix under conditions that promote a reaction between the at least first reactant and the at least second reactant to provide at least a first product; and (v) allowing the at least first product to form and fill at least a portion of the interior spaces of the porous matrix, thereby sequestering a greenhouse gas.

Process for producing sodium bicarbonate for purifying flue gases, according to which an aqueous solution containing sodium sulfate is subjected to electrodialysis to produce a sodium hydroxide solution and a sodium bisulfate solution, the sodium hydroxide solution being carbonated in order to obtain sodium bicarbonate.

The invention provides methods and apparatuses for removing carbon dioxide from a gas stream. In particular, the invention provides methods and apparatuses for absorbing carbon dioxide from a coal-fired boiler flue gas stream using an absorbing solution and for regeneration of an alkaline component used in the absorbing solution. In one embodiment, the invention provides a method for removing carbon dioxide from a gas stream by contacting a gas stream containing carbon dioxide with an alkaline liquid stream; absorbing at least a portion of the carbon dioxide into the alkaline liquid stream to produce absorbed carbon dioxide; and catalyzing a reaction of the absorbed carbon dioxide to a form of carbonate.

Disclosed are methods for solution mining of evaporite minerals, such as trona, comprising drilling an access well and at least two lateral boreholes; injecting a fluid; circulating the fluid through the lateral boreholes with a controlled fluid flow; and collecting a pregnant solution. Also disclosed are methods of solution mining that include injecting an aqueous solution into an underground trona cavity at a temperature sufficient to maintain at least a portion of the solution in the cavity in the Wegscheiderite solid phase region; removing aqueous solution from the cavity; and recovering alkaline values from the removed aqueous solution. Also disclosed are methods of solution mining that include injecting an aqueous solution into an underground trona cavity; removing aqueous solution from the cavity, wherein the temperature of the removed aqueous solution is at about the TWA point temperature; and recovering alkaline values from the removed aqueous solution.

The invention discloses a method for composite production of high-purity lithium hydroxide monohydrate, high-purity lithium carbonate and battery grade lithium carbonate. Industrial grade lithium hydroxide is dissolved into pure water or crystallization mother liquor, and a first solution is prepared; a first impurity removal agent is added into the first solution, then filtering is performed, a lithium hydroxide crystal is added into a filtrate, cooling crystallization is performed, solid-liquid separation is performed to obtain a high-purity lithium hydroxide monohydrate wet material and crystallization mother liquor; the high-purity lithium hydroxide monohydrate wet material is dissolved into pure water or carbonization mother liquor, and a second solution is prepared; carbon dioxide is introduced into the second solution to perform primary carbonization, and solid-liquid separation is performed to obtain a lithium carbonate wet material and a filtrate; a second impurity removal agent is added into the filtrate, after a heat preservation reaction is performed, carbon dioxide is introduced to perform secondary carbonization, then, introduction of the carbon dioxide is stopped, the reaction continues to be performed, then, solid-liquid separation is performed, obtained solids are washed, a high-purity lithium carbonate wet material and carbonization mother liquor are obtained, and after the high-purity lithium carbonate wet material is post-processed, a high-purity lithium carbonate product is obtained.

The invention relates to a salt, alkali and calcium combined cycle production technology by the use of well mineral salt. Based on the exploitation of brine from well mineral salt, the salt, alkali and calcium combined cycle production technology by the use of well mineral salt is a cycle production technology, which focuses on the technology for making alkali from brine by the ammonia-soda process and takes account of the vacuum salt-making (including the brine refinement) and calcium-making technologies. Alkali-making wastewater replaces most fresh water to be injected into a salt mine well to collect brine, and the obtained high-calcium brine is taken as the raw material of the salt and calcium (including liquid calcium) co-production as well as the raw material for preparing alkali and other chemical production raw materials, wherein the liquid calcium can be used to produce liquid salt; alkali-making waste residues are injected into an underground dissolution cavern, namely a salt cavern which is formed by the exploitation of brine from well mineral salt, thus accomplishing the combined cycle production technology in which alkali-making and salt-making technologies are closely related with materials. The produced wastes are used as resources or undergo a harmless treatment, thus protecting the environment. In addition, the utilization rate of sodium chloride in rock salt reaches 100%, achieving maximum efficiency.

The invention provides a method to produce a low-magnesium battery grade lithium carbonate from lithium sulfate solution. The method comprises the steps that: (1) purification treatment of lithium sulfate solution as following: lithium sulfate solution is co-precipitated to lower the impurities ions Fe3+, Mg2+, Al3+ and Ca2+, and condensed and filtered to further eliminate impurities, and obtain purification residues and a pure finish solution of lithium sulfate; (2) soda is dissolved and added with purification residues obtained from the purified lithium sulfate solution, and used for a filtering media to filter calcium and magnesium and obtain purified soda solution; (3) the purified soda solution is added with complexant EDTA, and stirred for complexation reaction, and slowly added with condensed and impurities eliminated pure finish solution of lithium sulfate, and a crude lithium carbonate is prepared; (4) the crude lithium carbonate is stirred, cleaned, dried and smashed, thus obtaining the low-magnesium battery grade lithium carbonate. The method of the invention has the advantages of simple production technique, stable product quality and low cost, and expertly employs the waste residues in the process, not only solves the difficulty of impurities elimination for soda, but also enhances the recycling ratio of lithium, which is suitable for the production application of the positive pole material of Li-ion battery.

The invention belongs to the field of antimony smelting arsenic alkali residue treatment and particularly discloses a wet-method recycling and harmless treatment process for antimony smelting arsenicalkali residue. The process adopts a whole-wet-method treatment process and mainly comprises the eight working procedures of breaking, dissolving for leaching, oxidation for antimony outlet, purification for impurity removing, transition for crystallizing, reduction for arsenic sinking, evaporative crystallization and secondary residue harmless treatment. Recycling and harmless treatment of the arsenic alkali residue, zero emission of waste residue and waste water and up-to-standard discharge of exhaust gas are thoroughly achieved, the long-term plagued arsenic alkali residue environmental pollution problem in the antimony smelting industry in China is thoroughly solved, and the environmental risk caused by stacking the arsenic alkali residue is eliminated; and meanwhile, separation, enrichment and effective recovering of valuable elements are achieved.

The invention provides a thermal circulation technology of utilizing sodium sulfate solution or a carrier to cogenerate sodium carbonate and ammonium sulfate. The thermal circulation technology comprises the following steps: regarding an ammonium hydrogen carbonate solution prepared from sodium sulfate, ammonia and carbon dioxide as a raw material to be conducted with a replacement reaction, then carrying out separation to obtain sodium hydrogen carbonate (which can be calcined to obtain a pure alkali product) and an alkali preparing mother solution containing ammonium sulfate, sodium sulfate, ammonium hydrogen carbonate and ammonium carbonate; preheating the alkali preparing mother solution to a high temperature to remove ammonium hydrogen carbonate and ammonium carbonate, and then obtaining the deaminized mother solution containing ammonium sulfate and sodium sulfate; evaporating the deaminized mother solution at a high temperature to obtain sodium sulfate and a niter preparing mother solution; evaporating the niter preparing mother solution at a low temperature to obtain ammonium sulfate and an ammonium preparing mother solution; circulating the sodium sulfate to the replacement reaction working procedure; circulating the ammonium preparing mother solution to the deaminized mother solution high-temperature evaporation working procedure. The main products and byproducts prepared by thermal circulation technology disclosed by the invention are high in quality and added value; the thermal circulation technology is well-adapted in raw materials, low in sodium sulfate theoretical use ratio, production cost and energy consumption, closed circulating, free of three-waste discharge, and capable of saving energy and reducing emission.

The invention relates to a method for high resource treatment of cyclohexanone waste saponification lye. The method is improvement on a method for performing zero emission treatment on waste saponification lye produced by producing cyclohexanone through cyclohexane oxidation technology. By using the method, a process is set that sodium sulfate and pulverized coal are calcined to obtain sodium sulfide and carbon dioxide flue gas on the basis of the prior art, carbon dioxide in flue gas reacts with sodium hydroxide and sodium carbonate in initial waste lye to generate sodium hydrogencarbonate, and partial moisture is evaporated in the waste lye by high-temperature heat in the flue gas. The method utilizes the joint production of the cyclohexanone waste saponification lye to obtain chemical resources with higher level such as sodium carbonate, sodium sulfide, monoprotic organic acid, clean fuel oil and the like, and has more remarkable economic benefit; the method achieves the zero emission through the treatment of a waste with another waste, completely roots up the pollution of the waste lye on the environment, and has remarkable social benefit; and waste resources are circularly utilized, so the method has low energy consumption and mature process, is suitable for the large-scale treatment on the cyclohexanone waste saponification lye, and is also used for industrialized production of the chemical resources in the waste lye.

A method of producing sodium bicarbonate having a high degree of purity and obtaining a net reduction in effluent waste water, as compared to prior processes, when starting from trona ore is disclosed. The process entails utilizing the waste-water effluent stream from the conversion of trona ore to sodium carbonate as the feed for the conversion of sodium carbonate to sodium bicarbonate.

The invention discloses a method for mining low-grade rock salt ores and/or low-grade glauber salt ores by utilizing an alkali production waste liquor byproduct of an ammonia-alkali process and converting sodium sulfate in the ores into sodium chloride for alkali production. The method comprises the following steps of injecting the alkali production waste liquor into an underground cavity of the ores, performing chemical reaction on calcium chloride in the alkali production waste liquor and the sodium sulfate in the low-grade rock salt ores and/or the low-grade glauber salt ores to convert the sodium sulfate into sodium chloride required by alkali production, and mining the sodium chloride as brine for alkali production, precipitating and storing calcium sulfate generated by the reaction in the underground cavity, wherein the low-grade rock salt ores are low-grade rock salt ore resources abandoned by the salt and glauber salt co-production process, and every liter of brine mined by injecting fresh water into a mine of the ores contains 30 to 100 grams of Na2SO4 and 290 to 220 grams of NaCl; the low-grade glauber salt ores are low-grade glauber salt ore resources abandoned by the salt and glauber salt co-production process, and every liter of aqueous glauber salt mined by injecting the fresh water into a mine of the ores contains 200 to 100 grams of Na2SO4 and 120 to 220 grams of NaCl; every liter of alkali production waste liquor contains 95 to 115 grams of CaCl2 and 45 to 56 grams of NaCl.

A technology for producing sodium bicarbonate from mirabilite comprises steps as follows: mirabilite and distillation waste liquor mixed liquor is used as a raw material, sodium carbonate is added to the solution after absorption of ammonia, magnesium, iron and calcium ions in the solution are removed after the solution is subjected to a precipitation reaction at 15-50 DEG C, and a refined solution is obtained; carbon dioxide is added to the refined solution for carbonatation, and sodium bicarbonate solids and heavy alkali mother liquor are obtained through separation after the refined solution is subjected to a replacement reaction at 15-50 DEG C; lime is added to the heavy alkali mother liquor, and ammonia gas, carbon dioxide, calcium sulfate and distillation waste liquor are obtained after distillation reaction at 15-120 DEG C; ammonia gas and carbon dioxide are recovered to ammonia absorption and carbonatation procedures respectively; the distillation waste liquor and mirabilite in Step A are mixed to be recycled. The technology has the characteristics that mirabilite is directly utilized, ammonia is recycled, the comprehensive utilization rate of distillation waste liquor waste is high, the production cost is low, the waste residue discharge is low, the technology is environment-friendly, and the like.

The invention relates to methods for coproducing sodium carbonate and ammonium sulfate from melamine tail gas and mirabilite. The method for producing the sodium carbonate comprises the following steps of: a, providing a sodium sulfate water solution; b, introducing melamine tail gas into the sodium sulfate water solution to form an ammonium carbonate-sodium sulfate water solution; c, introducing carbon dioxide into the ammonium carbonate-sodium sulfate water solution to obtain a suspension serous fluid of sodium bicarbonate crystals; and d, carrying out solid and liquid separation on the suspension serous fluid to obtain sodium bicarbonate and a mother solution I, calcining sodium bicarbonate solid to obtain the sodium carbonate. The method further comprises the following steps of: e, adding the mother solution I into an ammonia stilling tower, heating, forming tower top mixed gas containing ammonia and carbon dioxide, generating a deamination solution in the tower; f, evaporating the deamination solution for dewatering to obtain sodium sulfate crystals and a mother solution II; g, cooling the mother solution II for crystallizing to obtain Na2SO4.(NH4)2SO4.4H2O salt crystals and a mother solution III; and h, evaporating the mother solution III for dewatering, and separating out ammonium sulfate crystals. The methods have the advantages of high utilization rate of raw materials and low energy consumption.

A process to convert carbon dioxide into a stable substance with electrolytically activated seawater and use this process to sequester carbon dioxide from coal power plants (82) and similar carbon dioxide producing equipment, and capture and sequester carbon dioxide from the atmosphere. Electrolytically activated seawater (92) is produced using a unipolar electrolytic cell (91) and is sprayed into a contacting tower (93) or into the air.

The invention relates to a method for co-producing aluminum oxide and sodium carbonate from coal gangue. The method comprises the following steps of: calcining and activating the coal gangue and dissolving the calcined and activated coal gangue in acid to prepare an aluminum chloride acid extract; concentrating and crystallizing the acid extract to prepare crystalline aluminum chloride; calcining and decomposing the crystalline aluminum chloride to prepare crude aluminum oxide; dissolving the crude aluminum oxide in alkali to prepare sodium metaaluminate; performing solid-liquid separation on iron and titanium insoluble substances and other impurities and washing the product to obtain solution of sodium metaaluminate; adding an aluminum hydroxide seed crystal into the solution of sodium metaaluminate to prepare aluminum hydroxide deposit and solution of sodium carbonate; performing solid-liquid separation to obtain an aluminum hydroxide crystal and solution of sodium carbonate; concentrating and crystallizing the aluminum hydroxide crystal and the solution of sodium carbonate to obtain sodium carbonate; and calcining the aluminum hydroxide to prepare metallurgical-grade aluminum oxide. In a production process, sodium hydroxide from a chlorine industry, hydrochloric acid which is a byproduct of a PVC industry and carbon dioxide discharged from a calcium carbide plant in a production place of the coal gangue are fully utilized, so that industry pollution is reduced, a useful product is obtained and comprehensive resource utilization is realized. The method has the advantages of simple production technology, easily-controlled production process, high aluminum oxide extraction ratio, low production cost and stable product quality.

The invention relates to a method for producing sodium hydrogen carbonate and ammonium sulfate by using a sodium sulfate solution, and belongs to the technical field of chemical engineering. The method comprises the following steps: a, absorbing circulating gas by using the sodium sulfate solution at -5 to 10 DEG C to obtain absorbing liquid; b, mixing the absorbing liquid, ammonium hydrogen carbonate and/or mixed salt at -5 to 20 DEG C to obtain mixed slurry; c, performing sealed reaction on the mixed slurry to obtain sodium hydrogen carbonate and reaction mother liquid; d, mixing the reaction mother liquid and complex salt to obtain salt mixture and primary frozen mother liquid after freezing; e, distilling the primary frozen mother liquid to obtain carbon dioxide, ammonium circulating gas and ammonium steaming mother liquid; f, adjusting the ammonium steaming mother liquid by acid to obtain an acidified solution and gas; g, mixing and freezing the acidified solution and crystallizedmother liquid to obtain complex salt and secondary frozen mother liquid; and h, evaporating and concentrating the secondary frozen mother liquid to separate out ammonium sulfate. The method is low inenvironmental pollution and high in raw material utilization rate.