761results about "Iron sulfates" patented technology

The process of this invention is directed to the removal of metals from an unsupported spent catalyst. The catalyst is subjected to leaching reactions. Vanadium is removed as a precipitate, while a solution comprising molybdenum and nickel is subjected to further extraction steps for the removal of these metals. Molybdenum may alternately be removed through precipitation.

The invention relates to potassium feldspar decomposition and comprehensive utilization technology and in particular relates to a process for decomposing potassium feldspar by adopting a low-temperature semidry method for comprehensive utilization. The process comprises the steps of fully mixing potassium feldspar, fluorite and sulfuric acid, then adding the mixture to a converter reactor to react at 180-250 DEG C, separating SiF4 and HF generated through a reaction from a system under the condition of negative pressure, carrying out absorption with ethanol and water solution to prepare white carbon black, recovering fluorine resources in the process from the solution in the forms of ammonium fluoride and other aids by adopting the method of adding ammonia water and applying the recovered fluorine sources to decomposition of potassium feldspar and carrying out a series of processes such as extraction on the solids after a reaction to obtain calcium sulfate whisker, potassium fluosilicate, aluminium hydroxide and ferric sulfate products. Compared with the method for decomposing potassium feldspar by a high temperature method, the process has the advantages that the reaction conditions are mild and the requirements for equipment are lower; the white carbon black is directly prepared through gas hydrolysis, thus avoiding the tedious course from solid phase separation; and the fluorine resources introduced to the decomposition course are recycled by adopting the mode of ammonium fluoride, thus avoiding waste of the fluorine resources.

The present invention belongs to the technical field of soil heavy metal remediation, specifically discloses a method for preparing the iron-based biochar material, the iron-based biochar material prepared there from and a method for controlling the heavy metal pollution in soil using the iron-based biochar material. For the iron-based biochar material of the present invention, by using a method of high-temperature carbonization, a biomass is used as a raw material and an iron-containing compound is add in the process of preparing biochar, wherein iron is incorporated in a specific ratio, to form the iron-based biochar material with a special structure and function. The material has a simple preparation process, low cost and a short production period; the prepared iron-based biochar material has an unique effect on the arsenic-cadmium combined pollution soil remediation, can effectively reduce the bioavailability of arsenic and cadmium in the soil, significantly reduces the arsenic and cadmium contents in the agricultural products planted in the arsenic-cadmium combined pollution soil, and has no toxic and side effects on the crops, is safe to apply and can be applied to the control of arsenic-cadmium combined pollution soil in a large scale.

Ammonia is used as precursor source of hydrogen fuel in an on-vehicle internal combustion engine. Ammonia is stored as, for example, a ligand in an on-vehicle transition metal composition. Upon demand for hydrogen by the vehicle's engine control system, ammonia is expelled as a gas from some of the composition and the ammonia gas is dissociated into a mixture of hydrogen and nitrogen and delivered as a fuel-containing mixture to the engine. In a preferred embodiment, the hydrogen is used as a supplement to gasoline as a fuel for engine operation.

The invention relates to a process for recovering sulfuric acid and sulfate from waste acid generated in the preparation of titanium dioxide by using a sulfuric acid method, belonging to the technical field of waste acid treatment in the industrial production. The invention recovers sulfuric acid and sulfate products from waste acid generated in the production process for preparing the titanium dioxide by using the sulfuric acid method through the sedimentation pretreatment and the simple process including the first segment of flash evaporation-crystallization, concentration and separation, the second segment of vacuum evaporation, concentration and separation and the third segment of vacuum evaporation, concentration and separation. The invention has simple process, convenience of operation, simple equipment, high performance price ratio and high yield, high concentration and less impurities of the product acid, can recycle resources without waste liquid or waste residue emission and can be favorable to environmental protection and energy saving, and emitted exhaust mainly contains air and less vapor, is non-toxic to the environment and can effectively overcome the difficulties of fouling and clogging of the equipment. The invention can be widely applied to the recovery of waste acid in the industrial production and be particularly suitable for recovering the waste acid generated in the preparation of titanium dioxide by using the sulfuric acid method.

The invention discloses a method for concentrating waste sulfuric acid by utilizing waste heat of a titanium dioxide calcinator, comprising the following steps: at normal temperature and pressure, proper amount of water absorbent is added to titanium dioxide waste acid, liquid water is dissolved out in the form of solid crystal water through the water absorbent, filtrate after solid-liquid separation is cooled, iron vitriol in the solution is crystallized and dissolved out, and the acid liquid is further concentrated; the two steps are repeatedly carried out until the concentration of sulfuric acid in the final filtrate reaches more than 60%, and then the final filtrate is utilized in the acid hydrolysis procedure; and the water absorbent is dehydrated and dried to be regenerated by taking dustproof tail gas of the calcinator, and the steam generated in the drying and regeneration is cooled and flows back to technological process as washing water in titanic acid rinsing or is drained. The method provided by the invention solves the problems of more equipment, long flow and easy blockage in the existing technology, and the equipment investment and operating cost are reduced; and the water absorbent is recycled after being regenerated, so that the energy is saved, the consumption is reduced, and the efficiency is obvious; no wastewater, waste gases and residues are generated in the whole technology, the operability is strong, the productivity of equipment is high, the flow is simple, the investment is less, the cost is low, energy is saved, emission is reduced, and the benefit is obvious.

The invention discloses a method for purifying a ferrous sulfate heptahydrate byproduct in titanium white production, which comprises the following steps of: (1) adding a solvent into the byproduct in titanium white production, heating to the temperature of between 65 and 105 DEG C, and stirring for dissolution to prepare saturated solution; (2) adding iron powder at the temperature of between 95 and 105 DEG C; (3) adding phosphoric acid and heating at the temperature of between 95 and 105 DEG C for 10 to 20 minutes; (4) cooling the mixture to the temperature of between 80 and 90 DEG C, adding sulfide, stirring for 30 to 60 minutes, and adding sulphuric acid; (5) adding polyacrylamide, stirring for 3 to 10 minutes, precipitating, and filtering to obtain ferrous sulfate solution; and (6) cooling and crystallizing the ferrous sulfate solution, filtering and separating to prepare ferrous sulfate crystals. The content of the ferrous sulfate heptahydrate prepared is over 20.1 percent, and the content of titanium, lead, cadmium, chromium and magnesium is less than 10ppm based on the lead. The process is simple and the process flow is short.

The invention discloses a preparation method of a polysilicate aluminium ferric flocculant, which comprises the steps of: dissolving ferrous sulfate heptahydrate, which is a by-product of a titanium white industry and used as a main raw material, in water, regulating the pH value of the dissolved ferrous sulfate heptahydrate to be 0.6-1.0, and then adding titanium white for oxidation; adding aluminum sulfate for polymerization reaction for 30-50min at the water bath temperature of 50-100 DEG C to obtain the polysilicate aluminium ferric flocculant; adding H3PO3 to be used as a stabilizer in the polymerization reaction process; adding a small amount of Na2CO3 when the liquid is even to regulate the alkalization degree of the mixed liquid to be 0.05-0.6; and finally, obtaining a dark-brown polymerized liquid product, i.e. the silicate aluminium ferric flocculant. The preparation method provided by the invention has the advantages of simple process, low cost, and no waste liquid, waste gas, and waste residues in a production process. The product has high content of active flocculation components, is superior to the traditional industrial product in full-ferric content and the flocculation property, and can be widely applied to feed water treatment and sewage and wastewater treatment.

The invention discloses a resource utilization method of Fenton iron sludge. The method comprises the following steps of: (1) treating Fenton; adding the rest of ferrum into concentrated sulfuric acid; and controlling the temperature to be between 70 and 75 DEG C to stir for 30 minutes; (2) adding excessive quantities of scrap iron chips into an iron sludge solution obtained in the step (1) to reduce; detecting Fe3<+> by using a phenol solution until Fe<3+> is totally reduced into Fe<2+>; and (3) after the reduction is finished, standing for precipitating for 30 minutes; extracting supernate; adding ethanol according to the proportion that V(supernate)/V(ethanol) is equal to 10 to 1 and shortening the crystallizing time of ferrous sulfate; and after the crystallization is finished, obtaining an industrial FeSO4.7H2O finished product. According to the method, the bottle neck problem of Fenton technology promotion can be solved, the resource utilization of solid wastes is realized, and Fenton iron sludge is turned from waste into treasure, so that sustainable development of human society is facilitated.

There are provided processes for extracting aluminum ions from aluminous ores. Such processes can be used with various types of aluminous ores such as aluminous ores comprising various types of metals such as Fe, K, Mg, Na, Ca, Mn, Ba, Zn, Li, Sr, V, Ni, Cr, Pb, Cu, Co, Sb, As, B, Sn, Be, Mo, or mixtures thereof.

The invention relates to a recyclable dry desulfurizer with high sulfur capacity. The desulfurizer contains not less than 88% of substances containing FeOOH and not less than 7% of organic binders, wherein the organic binder is one or more of sodium carboxymethyl cellulose, sesbania and cellulose powder. The invention further discloses a preparation method of the desulfurizer and a regeneration method of waste agents generated after the desulfurizer is used. The invention solves the following problems in the prior art: the dry-formed desulfurizer has low sulfur capacity, and after the dry-formed desulfurizer is used once, the waste agents can not be regenerated or the regeneration cost is high, so that great amount of waste agents are only buried, thus not only wasting the effective resources in the original desulfurizer but also leading to new environmental pollution problems.

The preparation method for battery grade ferrous sulfate heptahydrate crystal of the present invention includes using ferrous sulphate which is the by-product in the titanium dioxide production as raw material, using the operation of purification, filtration, crystallization and dryness, and preparing ferrous sulfate heptahydrate by using the difference of the solubility of ferrous sulphate changing with the temperature. The operation of purification includes performing reduction of ferric iron in ferrous sulphate which is the by-product in the titanium dioxide production to ferrous iron by using a reducing agent, adding ferrous sulfide to remove the heavy metal ions such as cobalt, nickel, zinc, copper, plumbum and cadmium, and using fluoride to remove calcium and magnesium ions. The preparation method uses vacuum drying and packaging, and the main content of ferrous sulfate heptahydrate in the dried material is more than 99.7%. The preparation method has simple technology and low cost, can recycle fluorinion by precipitation conversion, and can reduce the discharge of hazardous waste. Moreover, the prepared product has high purity, low impurity and ferric iron contents, and can be long-term storage. The recovery rate of ferrous sulphate is greatly improved.

The invention discloses a method for synthesizing polymeric ferric sulfate, which employs air, oxygen or oxygen-enriched air as an oxidizing agent, uses ferric persulfate, sulfuric acid or waste acid of titanium white by sulfuric acid process raw materials, using acid nitric ferric sulfate as an accelerating agent and synthesizing the polymeric ferric sulfate in an enamel autoclave which is provided with a packed tower, finally, using ferric persulfate to process the oxidation off-gas. The invention has the advantages of low energy consumption, low cost and convenient operation, not only effectively utilizing the industrial waste acid and the industrial waste slag, but also avoiding polluting to the environment.

The invention relates to a treatment method of a zinc-containing and iron-containing waste acid. The method comprises the following steps: adding a reducing agent to the zinc-containing and iron-containing waste acid, and fully reacting to obtain a reducing liquid; filtering the reducing liquid to collect a first filtrate; adding concentrated sulfuric acid into the first filtrate, and uniformly stirring to obtain a mixed liquid; evaporating and concentrating the mixed liquid at 90-110 DEG C to obtain a concentrated liquid; filtering the concentrated liquid at 70-100 DEG C to obtain a mixture with solids of FeSO4.H2O and ZnSO4.H2O. A certain amount of zinc-containing and iron-containing waste acid and concentrated sulfuric acid is added into the filtered second filtrate for a concentration and crystallization process in the next cycle. According to the treatment method of the zinc-containing and iron-containing waste acid, heavy metal ions are replaced to single substances, and after solid impurities in the reducing liquid are filtered to remove, the concentrated sulfuric acid is added. The mixture is evaporated, concentrated and filtered to obtain the crystal mixture with solids of FeSO4.H2O and ZnSO4.H2O. The crystal mixture can be used as a mineral additive for feed. According to the treatment method of the zinc-containing and iron-containing waste acid, the recovery rates of zinc and iron are higher, and the product has broad market prospect.

The invention discloses a preparation method of solid polymeric ferroaluminum sulfate, comprising the following steps: (1) basic ferric sulfate is prepared from ferrous sulfate; (2) water, sulfuric acid and hydrogen peroxide are added into the basic ferric sulfate in sequence, stirring and standing; (3) an aluminized compound is added and further stirred; (4) being self-cured and precipitated under dry condition; and (5) being aged at room temperature and crushed so to obtain a product. The invention uses a blast oxidation process and solves the pollution problem which is generated by the catalytic oxidation process in the traditional iron-based coagulant industry. The polymeric ferroaluminum sulfate is a solid product; compared with the liquid product, the polymeric ferroaluminum sulfate has advantages of storage and transportation, has long service life, and does not need evaporation or decompression evaporation process, and the coagulation active component of the product is retained to the largest extent. Quality indicators such as basicity, active component, and the like are all higher than the quality indicators in the prior art. When in actual implementation and embodiment of water body, the effect of the polymeric ferroaluminum sulfate is better than the effect of the inorganic coagulant such as polyaluminum chloride polymeric ferroaluminum sulfate and the like.

The invention discloses a purification method of ferrous sulfate as a byproduct of titanium dioxide. The ferrous sulfate as the byproduct of the titanium dioxide contains titanium, magnesium and manganese impurity elements. The preparation method comprises the following steps: (1) dissolving the ferrous sulfate as the byproduct of the titanium dioxide with water to obtain a ferrous sulfate solution; (2) adding iron powder into the ferrous sulfate solution obtained in the step (1), heating to 90 DEG C or above, and adding phosphoric acid till the pH value of the solution is up to 3 to 4.5; (3)adding sulfide and fluoride into the solution obtained in the step (2), and stirring; (4) adding a flocculant into the solution obtained in the step (3), and then removing flocculating sediment to obtain a purified ferrous sulfate solution. The impurity element content of the extracted ferrous sulfate can meet the requirement of producing battery grade iron phosphate.

The invention discloses a waste acid and wastewater treatment process in processes of pickling and purifying quartz or feldspar. The process comprises three steps of treatment of the waste acid, treatment of washing water and treatment of wastewater. The waste acid is processed by cation-anion resin, the washing water is fed to a neutralizing tank to process by using lime milk, the wastewater is processed by a concentrated sulfuric acid, and the waste acid and the wastewater generated in the processes of pickling and purifying the quartz or feldspar are completely recycled and applied in cycle. Especially, the wastewater containing calcium chloride which cannot be removed by the prior art is successfully processed, and zero pollution and zero emission are really achieved.

The invention provides a preparation method of polyferric sulfate. The method is that a sulfuric acid aqueous solution and ferrous sulfate are mixed to obtain a mixing solution of which the pH is 0.5 to 1.5; the mixing solution and hydrogen peroxide respectively individually flow through independent flowing channels and then are synchronously poured into a reaction system to react to obtain polyferric sulfate. With the adoption of the method, the oxidizing capacity of hydrogen peroxide can be improved, the rate of converting ferrous ions into ferric ions can be increased, and moreover, ferrous ions and hydrogen peroxide can fully contact and rapidly react; therefore, the problem of decomposing of hydrogen peroxide at a high temperature or strong acid condition in the prior art can be effectively solved, the dosage of hydrogen peroxide can be reduced, the cost input can be decreased, the operation process is simplified, and the reaction time is greatly reduced. The quality of polyferric sulfate prepared by the method meets indicators as specified by national standard on top quality goods; with the adoption of the polyferric sulfate to treat wastewater, the COD of drained water can be stabilized to be less than or equal to 86mg/L, so that the method is applicable to industrial production.

The invention relates to a method for preparing white carbon black, alumina and kerogen with oil shale, comprising the steps that: (1) the oil shale is crumbled into grains with a diameter less than 0.84 mm or less; (2) the oil shale, NaOH and water are added into a reactor for reaction for 0.5 to 24 hours at 20 DEG C to 200 DEG C, then filtration is made and a first filtrate and a first filter cake are obtained, then inorganic acid is used to adjust the pH value of the first filtrate and dispersant is added, and the white carbon black is obtain after 0.5 to 24 hours of aging; (3) the first filter cake is mixed with inorganic acid, the acid leaching temperature is 20 DEG C to 100 DEG C and the acid leaching time is 0.5 to 24 hours, then a second filter residues and a second filtrate are obtained upon filtration; (4) aqueous slkali is added into the second filtrate to adjust and control the pH value till precipitate Al(OH)3 is produced, then filtration is made and a third residues Al(OH)3 precipitate and a third filtrate are obtained; the Al(OH)3 precipitate can be used for preparing Al2O3 products with different contents by being sintered at 450 DEG C to 1250 DEG C; (5) the third filtrate can be prepared into Fe2(SO4)3 concentrated solution with different density after being concentrated, then the concentrated solution is further processed and Fe2(SO4)3 product is prepared. The invention has simple technique and low energy consumption.