683results about "Alkali metal sulfite/sulfate purification" patented technology

The process of producing sodium sulfate and sodium chloride in a Na2SO4-NaCl-H2O system belongs to the field of mixed inorganic solution evaporating separation technology. Mixed solution of sodium sulfate and sodium chloride as material is first evaporated and then separated to obtain sodium sulfate, sodium chloride and evaporated mother liquor; the evaporated mother liquor is low temperature evaporated and separated to obtain sodium chloride and salt-making mother liquor; and the salt-making mother liquor is evaporated and separated to obtain sodium sulfate and saltpeter-making mother liquor. The present invention has the features of high main and side product quality, high material adaptability, low cost, low cost, no waste draining, etc.

The invention discloses an industrial application of an MVR (mechanical vapor recompression) crystallizing evaporator technology in the production of sodium sulfate and sodium chloride in Huaian, Jiangsu, and relates to an improvement of a salt and sodium sulfate coproduction evaporation technology, belonging to the technical field of chemical three-waste treatment and utilization, and in particular to an application of an MVR crystallizing evaporator in a sodium sulfate and sodium chloride separation technology. The application is mainly technically characterized in that sodium sulfate liquid is concentrated by the MVR crystallizing evaporator, the sodium sulfate is produced at high temperature, and the sodium chloride is produced at low temperature. According to the invention, the mechanical re-compressed vapor is evaporated, concentrated and crystallized at 90-100 DEG C to obtain sodium sulfate, and the re-compressed vapor at a low temperature of 55 DEG C is concentrated and crystallized to obtain sodium chloride. According to the invention, the application of the MVR technology to the concentration of sodium sulfate liquid is realized, the sodium sulfate is produced at high temperature, and sodium chloride is produced at low temperature. The application disclosed by the invention is an environmental protection project which saves energy, reduces emission and avoids waste gas, waste water and waste residue.

The invention relates to a crystallization treatment method and device of high salt wastewater and belongs to the technical field of water treatment. The method is characterized in that after sodium sulfate concentrated water is treated by a freezing crystallization system, generated mother liquor A enters into an MVR system for evaporative crystallization; after sodium chloride concentrated water is treated by the MVR system, generated mother liquor B enters into a freezing crystallization system for freezing crystallization, and the mother liquor can be treated in a circulation overlapping manner; a drain outlet of the MVR system of the device is connected with a liquid inlet of a crystallization tank in the freezing crystallization system through a pipeline and the drain outlet of the freezing crystallization system is connected with a liquid inlet pipe of the MVR evaporative crystallization system. The method has the advantages that the mother liquor is treated by a freezing crystallization technology and an MVR evaporation crystallization technology in a circulation overlapping manner, so that the problems of zero emission and resource utilization are solved, and therefore, the energy consumption is effectively reduced and the operating cost is lowered.

Zero discharge processing methods for the treatment of agricultural drainage water (ADW) are disclosed. The disclosed methods are capable of meeting the three critical issues in treating ADW: (1) selective removal of sulfate scale-prone species and toxic species; (2) production of usable water that at least meets irrigation water quality; and (3) recovery of sodium sulfate and sodium chloride as valuable commodities.

The invention discloses a method of recovering sodium sulfate from a lead-bearing desulfurized waste liquid. The method is characterized by comprising the following steps: after adding a complexing agent into the lead plaster-bearing desulfurized waste liquid, forming a lead carbonate precipitate of lead complex ions in the liquor by adopting carbon dioxide or sodium hydrogen carbonate, and then carrying out solid-liquid separation to obtain a sodium sulfate filtrate and the lead carbonate precipitate; adding anhydrous sodium sulfate and sodium hydroxide into the sodium sulfate filtrate obtained by separating lead carbonate, and cooling at low temperature to separate out sodium sulfate crystals; and returning the filtrate without the sodium sulfate crystals again for desulfurization of lead oxide-bearing wastes.

The present invention is process of treating effluent from the production of dye intermediate 1-amino-8-naphthol-3, 6-disulfonic acid and recovering resource. The process includes: distilling pre-treatment of the effluent; adsorbing 1-amino-8-naphthol-3, 6-disulfonic acid, intermediate product and other organic matter from the effluent with macroporous weak alkaline resin ND900 in serially connected three column; neutralizing the adsorbed columns treated water with alkali and decompression distilling; and final aerobic biochemical treatment for the water to reach exhaust standard. The process can reduce CODcr in the effluent from 16,700 mg/l to below 100 mg/l. The used resin may be desorbed with NaOH+H2O desorbing agent for reuse, and the desorbed liquid may be distilled for recovery.

The present invention relates to a process for treating sodium sulfate wastewater by using a nanofiltration-reverse osmosis combined membrane. According to the process, the pretreated sodium sulfate wastewater is conveyed to a nanofiltration membrane stack through a high pressure pump, and the nanofiltered concentrated solution is subjected to multiple effect evaporation crystallization to obtain an anhydrous sodium sulfate product and condensed water, wherein the condensed water is recycled; the nanofiltered producing water is conveyed to a reverse osmosis membrane stack through the high pressure pump, the resulting concentrated solution returns to the pretreated sodium sulfate stock solution to carry out the secondary nanofiltration, and the reverse osmosis producing water is recycled, wherein the concentrated solution is subjected to the reverse osmosis membrane stack. Compared to other pollution control technologies, the process of the present invention has the following advantages that: the equipment is compact, and the land occupation is small; no morphological and chemical influence is generated to the treated object; the process is a continuous process, and the automatic and uninterrupted operating can be achieved; the process has characteristics of low energy consumption, no phase change, no temperature change, easy control and simple operation; the process can be directly circulated on the site; the sodium sulfate is subjected to concentration, evaporation crystallization, and recovery utilization in the absence of chemical and physical changes, such that the zero discharge of the sodium sulfate wastewater is achieved; the reverse osmosis producing water is adopted as the process pure water to use so as to save a large amount of the process water.

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 discloses a recycling method for high-salinity wastewater containing sodium chloride and sodium sulfate and belongs to the field of wastewater treatment. The method comprises: filtering wastewater through a nanofiltration membrane; performing evaporative crystallization on filtrate through the nanofiltration membrane to obtain sodium chloride and filtered mother liquor; performing evaporative crystallization on retained liquor which does not pass through the nanofiltration membrane to obtain sodium sulfate and retained mother liquor; mixing the filtered mother liquor with the retained mother liquor to obtain a mixture and adding fluosilicic acid into the mixture; and stirring sufficiently the mixture to obtain sodium fluosilicate by filtering. Filtered acid water is used in pH value adjustment of a system before biochemical treatment.

The invention provides a method for treating wastewater containing ammonia, vanadium, chrome and sodium sulfate. The method comprises the following steps: step 1, deaminating to prepare ammonia; step 2, extracting chromic hydroxide; step 3, absorbing the vanadium and the chrome with resin columns; and step 4, extracting anhydrous sodium sulfate. The method can separate the ammonia, the vanadium, the chrome and the anhydrous sodium sulfate from the wastewater containing the ammonia, the vanadium, the chrome and the sodium sulfate to purify and recycle the wastewater, realize zero emission and generate environmental protection effect, thereby being suitable for extracting usable substances from the wastewater containing the ammonia, the vanadium, the chrome and the sodium sulfate while purifying and recycling the water.

The invention relates to a method of recycling anhydrous sulfate sodium from de-sulfurized lead paste filtration, belonging to a resource recovery and utilization process, which avoids the disadvantages that waste sulfate is used and low concentration sulfate sodium is emitted into the environment. The method of the invention comprises: desulfurized lead paste filtration collection, sodium carbonate neutralization, first time heavy metal removal, filtration PH value adjustment, second-time heavy metal removal, decolorizing step, and vaporization and crystallization step; the device comprises a transfer tank, a neutralization tank, a first-stage purifying tank, a PH adjusting tank, a second-stage purifying tank, a decolorization tank, a filtration collection tank and a vaporization crystallization system; the waste sulfate collection tank is connected with a waste sulfate pre-processing tank, the waste sulfate pre-processing tank is respectively connected with the neutralization tank and the PH adjusting tank. The invention can directly recycle anhydrous sulfate sodium, the waste sulfate is used to neutralize the carbonate sodium remained in the filtration; the heavy metal ions and other ions in the filtration are removed according to two steps, so that the grade of obtained anhydrous sulfate sodium is equal to or larger than industrial grade.

The invention discloses a desulfurization wastewater concentration, evaporation, crystallization, and salt separation process. The process comprises the steps as follows: introducing raw water into a quadruple-effect counter-flow forced circulation evaporator, treating sodium sulfate through evaporating, concentrating and crystalizing, separating sodium sulfate first, and freezing separated mother liquor, wherein most of sodium sulfate in the mother liquor is successfully separated; introducing the frozen mother liquor into a triple-effect evaporator after preheating, evaporating, concentrating and crystalizing sodium chloride, wherein the obtained crystal salt is used as an industrial raw material; introducing the mother liquor produced by a sodium chloride evaporator into a single-effect evaporator to obtain an abraum salt crystal. The process successfully separates the sodium sulfate in the desulfurization wastewater, and the sodium chloride is treated through evaporating, concentrating and crystalizing, the obtained sodium chloride crystal salt is used as the industrial raw material, the mother liquor produced by the sodium chloride evaporator enters the single-effect evaporator to obtain the abraum salt crystal, so that the sodium sulfate and the sodium chloride are effectively separated.

The invention relates to a nanofiltration membrane blending based high salinity wastewater zero discharge processing method, and a device. The nanofiltration membrane blending based high salinity wastewater zero discharge processing method mainly comprises following steps: high salinity wastewater is delivered through a pretreatment system for impurity removing, salt extraction concentration, andsoftening; softened concentrated water is introduced into a nanofiltration blending system for blending of the concentrations of monovalent and divalent salts, so that the monovalent salt to divalentsalt concentration ratio is controlled to be 0.01 to 0.1; concentrated water discharged from the nanofiltration blending system is introduced into a sodium sulfate crystallization system for processing so as to obtain divalent salt products capable of satisfying industrial salt requirements and a sodium chloride-containing mother liquor; an obtained nanofiltration blending system penetrating fluidis delivered through an extraction concentration system, and is introduced into a sodium chloride crystallization system so as to obtain sodium chloride salt products and a sodium sulfate-containingmother liquor; the sodium chloride crystallization mother liquor is subjected to impurity removing, and is introduced into the sodium sulfate crystallization system; the sodium sulfate crystallizationmother liquor is subjected to impurity removing, and is introduced into the sodium chloride crystallization system. The nanofiltration membrane blending based high salinity wastewater zero dischargeprocessing method is capable of realizing wastewater zero discharge, and stabilizing salinity fluctuation in the crystallization systems.

The invention discloses a method for recovering sodium sulfate by utilizing sodium sulfate containing waste salt residue. According to the invention, a combined process of heat treatment, dissolutionand water-washing, multistage purification and impurity removal, and thermal evaporation concentration and crystallization is adopted to treat waste salt residue with a main component of sodium sulfate. Through heat treatment, organic components in the sodium sulfate containing waste salt residue are completely degraded and decomposed under the condition of a high temperature; through dissolutionand water-washing treatment, waste salt components in the sodium sulfate containing waste salt residue are completely dissolved, and residual carbon black residue is removed through solid-liquid separation; through purification and impurity removal treatment, impurity components like metal ions in a salt solution are removed by adoption of technologies like chemical precipitation and filtration; and through thermal evaporation concentration and crystallization treatment, a clean salt solution is treated by adoption of a steam heating evaporation technology to obtain a sodium sulfate product. In the whole process, harmless treatment and resourceful utilization of the sodium sulfate containing waste salt residue are realized; the sodium sulfate product produced by using the process providedby the invention reaches the standards (GB/T6009-2014) of an industrial-grade anhydrous sodium sulfate product; economic benefits are improved; and environmental pollution is avoided.

The invention relates to an environment-friendly production process of 2-naphthol. The environment-friendly production process of the 2-naphthol comprises the following steps: adding refined naphthalene into a sulfonation kettle, adding concentrated sulfuric acid, heating and performing sulfonation reaction, neutralizing a mixture by using alkali after the reaction is finished, crystallizing, filtering, drying, performing alkali fusion and diluting; neutralizing the diluted alkali fused sulfonation liquid by using sulfuric acid at 70 to 80 DEG C, controlling the pH to be 4 to 7, standing and layering, and separating out crude 2-naphthol; washing, dehydrating and rectifying the separated crude 2-naphthol to obtain refined 2-naphthol; and removing alkali from the separated waste liquid, neutralizing to serve as alkaline liquid, absorbing sulfur dioxide generated by neutralization by using a sodium carbonate aqueous solution to produce sodium sulfite, adjusting the pH value of the waste liquid after 2-sodium naphthalene sulfonate is separated to be 2+/-1, performing three-stage extraction by using an extracting agent, performing reverse extraction on the extracting liquid by using dilute alkali, diluting sulfonated liquid by using the reverse extraction liquid, oxidizing the water phase by using a Fenton reagent or KMnO4, decoloring by using active carbon, and recovering sodium sulfate by a mechanical vapor recompression (MVR) concentration technology. By the process provided by the invention, no waste water is discharged basically and the production cost is reduced.

The invention relates to a high-salt-content industrial wastewater electrodialysis-high pressure nanofiltration combined salt separation system and technique, belonging to a water treatment technique. The technique comprises the following steps: high-salt-content wastewater treated by a front end pretreatment system is supplied to an electrodialysis system and concentrated by the electrodialysis system to obtain high-salt-content concentrated water; the high-salt-content concentrated water is directly sent into a high pressure nanofiltration system by a charging pump, and separated by a high pressure nanofiltration membrane assembly in the high-pressure nanofiltration system into sodium chloride concentrated water and sodium sulfate concentrated water; the sodium chloride concentrated water directly enters a subsequent evaporative crystallizing system I, thereby finally obtaining industrial-grade sodium chloride; and the sodium sulfate concentrated water directly enters a subsequent evaporative crystallizing system II, thereby finally obtaining the industrial-grade sodium sulfate. The system and technique are simple to operate, and have the characteristics of stable operation, high salt separation efficiency and the like. Compared with the existing salt separation technique, the technique provided by the invention implements salt separation on ultrahigh-salt-content water, can achieve the effect of high-efficiency salt separation, and greatly lowers the energy consumption and operating cost.

The invention relates to a method and equipment for extracting potassium salt from sintering machine head electroprecipitating dust in the metallurgical industry. The method comprises the following steps of stirring and leaching, chemical precipitation, mechanical centrifugation, and evaporation and crystallization. The equipment comprises a sintering dust leaching pool which is sequentially connected with a primary pressure-filtration unit, a rich liquid storage tank, a chemical precipitation tank, a mechanical centrifugation unit, and an evaporation and crystallization unit. According to the method disclosed by the invention, electroprecipitating dust is directly leached by using industrial water to leach potassium salt; the chemical method enables impurity metal ions in the leachate to rapidly and stably form a precipitate, and the product purity is higher; the solution after precipitation is efficiently separated by mechanical centrifugation; the filter residue is secondarily leached by adding the industrial water and the condensed water returned by the evaporation and crystallization unit, and the barren solution generated by the secondary pressure-filtration and centrifugation unit is returned as a sintering ash leachate, thus ensuring furthest extraction for the potassium salt in the sintering ash, and ensuring the reasonable allocation of the leachate of the whole system, without wastewater drainage. The equipment disclosed by the invention is simple in structure, economic and reliable, and capable of obtaining a high-purity potassium salt product after evaporation and crystallization, and drying.

The invention discloses a method for producing reagent grade sodium sulfate by using a white carbon black mother solution. The method comprises the following steps of: 1) removing a little amount of solid residue such as white carbon black and the like in the white carbon black mother solution by using a mixed cellulose micropore filtration membrane with thickness phi of less than or equal to 0.15 micron, and preliminarily purifying the white carbon black mother solution into a sodium sulfate solution; 2) treating the sodium sulfate solution obtained in the step 1) by using chelating resin toobtain a 5 to 6 percent pure sodium sulfate solution; 3) performing electrodialytic concentration on the 5 to 6 percent pure sodium sulfate solution obtained in the step 2) to obtain a 15 to 25 percent pure sodium sulfate solution; and 4) performing multi-effect evaporation on the 15 to 25 percent pure sodium sulfate solution obtained in the step 3) to obtain crystal, separating the crystal by using a centrifuge, drying the separated crystal at the temperature of 120 DEG C, and thus obtaining a finished product. The sodium sulfate product prepared by the method has the characteristics of low impurity content, high quality, low moisture content and the like, and is a high reagent grade sodium sulfate product.

The invention relates to a method for purifying a penicillin production waste liquid and recycling sodium sulfate. The method comprises the following steps: firstly, primarily evaporating the penicillin production waste liquid; concentrating a raw material liquid in desorbing residual solvents in the waste liquid; adding activated carbon into the primarily concentrated raw material liquid, wherein the liquid phase obtained from separation is a destaining solution of which a part of organisms are removed; continuously evaporating the destaining solution to obtain a concentrated destaining solution; adding alkali into the concentrated destaining solution, reacting to remove the impurities, filtering and precipitating, wherein an obtained liquid is an alkali treated liquid; adding a dilution agent for dilution crystallization into the alkali treated liquid, performing solid-liquid separation, and recrystalizing the solid, thereby obtaining high-purity sodium sulfate crystal; feeding a liquid into a solvent recycling tower for recycling the dilution agent, and feeding a tower kettle liquid to a biochemical pool for treatment. Compared with the prior art, organisms such as protein and pigment in the penicillin production waste liquid are reduced, at the same time sodium sulfate is recycled, then circulation application of sodium sulfate and water is achieved, the treatment difficulty and cost of the penicillin production waste liquid are remarkably alleviated and lowered, and great economic and environment benefits are achieved.

The invention discloses a production process of lithium hydroxide. According to the production process of lithium hydroxide, the crystallization mother liquor with high-concentration sodium sulfate and lithium hydroxide is used as the raw material, wherein the crystallization mother liquor with high-concentration sodium sulfate and lithium hydroxide is obtained after crystallization precipitation of sodium sulfate decahydrate in the production process of lithium hydroxide by the lithium sulfate method. Lithium hydroxide is prepared by the following steps: step A, introducing the crystallization mother liquor into a membrane separation system, wherein concentrated sodium sulfate solution is the intercept liquid and lithium hydroxide solution is the permeate liquid; step B, cooling (or cooling after further concentration) the sodium sulfate solution obtained in the step A, separating the sodium sulfate solution by centrifugation and drying the centrifuged sodium sulfate solution, so that crystal of sodium sulfate decahydrate is obtained; step C, concentrating the lithium hydroxide solution obtained in the step A by a steamer and further concentrating the concentrated lithium hydroxide solution in a crystallizing tank, then cooling, crystallizing and separating the concentrated lithium hydroxide solution by centrifugation and drying the centrifuged lithium hydroxide solution to obtain crystal of lithium hydroxide monohydrate. According to the production process, sodium sulfate and lithium hydroxide are effectively separated by the membrane separation technology, so that the purity of the lithium hydroxide solution is improved; thus, the quality of the lithium hydroxide product is effectively improved and production efficiency of the lithium hydroxide product is raised while the production cost is reduced.

The invention relates to a treatment method and treatment system for ternary positive electrode material production wastewater. According to the treatment method, a technological process of combining film separation, solid-liquid separation and evaporative crystallization is adopted for the first time: firstly, a sulfuric acid solution is taken as an absorbent and ammonia nitrogen in the wastewater is converted into ammonium sulfate by adopting film separation to achieve deamination; since the pH at an earlier stage is alkaline, a lot of metals in the wastewater are broken after deamination and form sediments together with alkali, and heavy metal sediments in the solution are filtered and removed; and supernate is subjected to evaporative crystallization to obtain sodium sulfate after filtration. According to the treatment method, ternary positive electrode material production wastewater is subjected to advanced treatment and reuse, so that the problem of treatment of the ternary positive electrode material production wastewater is effectively solved, ammonia, heavy metal and sodium sulfate resources in the wastewater are recovered, the water recovery rate is high and zero emission is achieved.

The invention relates to a production method for increasing nitrate removal capacity by a membrane method. Light brine from a brine electrolytic dechlorination working section is subjected to pretreatment, and then, enters a membrane device for filtering sodium sulfate; outlet water of the membrane device for filtering the sodium sulfate is divided into two parts; one part which is nitrate-poor brine with a concentration being lower than 3 g/l enters a primary brine device of a sodium hydroxide device for salt dissolving; the other part which is nitrate-rich brine with a concentration being higher than 45 g/l enters a refrigeration denitration unit, temperature is once decreased to -7 to -8 DEG C, and the temperature is readjusted to 1 to -3 DEG C so as to separate out Glauber's salt crystals; the Glauber's salt crystals enter a centrifuge so as to produce Glauber's salt products; and mother liquor is returned for repeated use. With the adoption of the production method provided by the invention, the content of rich nitrate is increased through refiltering the nitrate-rich brine under the conditions of existing nitrate removal device by the membrane method, and more Glauber's saltcrystals are correspondingly separated out under the condition of using the same flow of nitrate-rich brine, so that the production capacity of the nitrate removal device by the membrane method is increased, and brine with a qualified sulfate indicator is ensured to be obtained.