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43results about How to "Realize closed loop recycling" patented technology

Classifying and recycling process for waste magnesia carbon bricks produced after use of steel tundish working linings as well as dry material and coating material for tundish

ActiveCN103319189AAchieving RecyclabilityMaximize regeneration valueSolid waste disposalBrickGranularity
The invention relates to a classifying and recycling process for waste magnesia carbon bricks produced after use of steel tundish working linings as well as a dry material and a coating material for a tundish. The waste magnesia carbon bricks produced after use of the steel tundish working linings are subjected to recovery processing and are classified into reclaimed materials with three grain levels, i.e., the granularity is more than or equal to 3mm and less than 5mm, the granularity is more than or equal to 1mm and less than 3mm and the granularity is less than 1mm; the reclaimed materials with the granularity more than or equal to 3mm and less than 5mm and the granularity more than or equal to 1mm and less than 3mm are used as raw materials to prepare the dry material for the tundish, and the dry material is used for carrying out continuous casting on a slag line 2 and a tundish wall 3 and a tundish bottom 4 below the slag line 2 of the tundish working lining; the reclaimed materials with the granularity more than or equal to 1mm and less than 3mm and the granularity less than 1mm are used as raw materials to prepare the coating material for the tundish, and the coating material for the tundish is used for carrying out continuous costing on a tundish edge 1 above the slag line of the tundish working lining. The invention further provides a construction method for manufacturing the combined continuous casting tundish working lining by adopting the dry material and the coating material for the tundish. According to the classifying and recycling process, the dry material and the coating material for the tundish and the construction method, the classifying and recycling rate of the waste magnesia carbon bricks produced after use of the steel tundish working linings reaches 100 percent.
Owner:LAIWU IRON & STEEL GRP

Process for extracting nickel and cobalt from laterite-nickel ore

The invention discloses a method for extracting nickel and cobalt from a lateritic nickel ore which includes the steps of: (1) preparing the slurry of the ore: cracking the ores and preparing the slurry; (2) dipping the ores with muriatic acid: adding the muriatic acid in the slurry of the ore to carry out stirring and extraction under a normal pressure; (3) separating the solid and liquid; (4) neutralizing an extraction liquid; (4) sulfurizing and depositing the nickel; (6) regenerating the muriatic acid: the mother deposition liquid after nickel depositing is concentrated and roasted, the metal chloride in the mother liquid is hydrolyzed into chlorine hydride and metal oxide; the chlorine hydride after being absorbed by water obtains the regenerated muriatic acid and return to the working procedure of ore extraction; the metal oxide after being cracked and grinded returns to the working procedure of neutralizing. The method of the invention has a simple flow and an environment protective technique; the application range to resources is large; besides, the extraction speed is fast; the impurity removing capacity is high; the extraction rate of the nickel and cobalt is high; the method realizes the closed circulation of HCl and the comprehensive utilization of the resources.
Owner:CENT SOUTH UNIV

Comprehensive treatment method for smelting dust containing miscellaneous gold concentrate

The invention discloses a comprehensive treatment method for smelting dust containing miscellaneous gold concentrate and belongs to the technical field of precious metal pyrometallurgy. The comprehensive treatment method for the smelting dust containing the miscellaneous gold concentrate comprises the steps that firstly, the smelting dust is subjected to primary hydrochloric acid leaching, leachedslurry is subjected to high-price antimony reduction and hydrolysis antimony fixing, high-antimony gold concentrate and primarily-hydrolyzed liquid are obtained, secondary hydrochloric acid leachingis conducted on the high-antimony gold concentrate, high-grade gold concentrate with low impurities and secondary lixivium are obtained, high-grade oxychloride and secondarily-hydrolyzed liquid are obtained after hydrolysis is conducted on the secondary lixivium, dechlorinating transformation is conducted on the oxychloride, and then an antimony white terminal product is obtained; and a molysite arsenic fixing process is adopted for arsenic-containing liquid, and stable low-toxicity arsenic compound ferric arsenate and arsenic-removed liquid are obtained. By the adoption of the method, the smelting dust containing the miscellaneous gold concentrate is treated, the precise metal antimony can be effectively recovered, and the harmful element arsenate is fixed, so that the industrial problemthat arsenic and antimony dust is difficult to treat is solved.
Owner:ANHUI UNIVERSITY OF TECHNOLOGY

Electroplating chromium-containing wastewater treatment method and device

The invention discloses an electroplating chromium-containing wastewater treatment method and device. The treatment method comprises the following steps: (A) pre-removing impurities in chromium-containing wastewater by virtue of a pretreatment device, so as to acquire primarily treated effluent; (B) sequentially carrying out primary desalination on effluent by virtue of a cation exchanger and an anion exchanger, carrying out secondary desalination on effluent by virtue of an advanced treatment cation bed and an advanced treatment anion bed again, so as to obtain desalted water which can be recycled for chromium plating rinsing; (C) regenerating by virtue of a cation bed regeneration device when the cation exchanger is saturated and penetrated, and regenerating by virtue of an anion bed regeneration device when the anion exchanger is saturated and penetrated; and (D) carrying out sodium removal on anion bed regenerated liquid, and concentrating to form recyclable high-concentration chromic acid or carrying out evaporative crystallization. According to the electroplating chromium-containing wastewater treatment method, by virtue of a two-stage cation-anion bed system, the environmental pollution of hexavalent chromium is eliminated, and meanwhile, high-quality desalted water can be obtained and can be applied to production, so that the consumption of tap water and desalted water is saved, and the good economic benefit is achieved.
Owner:GUANGDONG XINTAILONG ENVIRONMENTAL PROTECTION GRP CO LTD

Method for separating valuable components of monazite slags

The invention discloses a method for separating valuable components of monazite slags, and particularly relates to a method for separating valuable components of monazite slags into a liquid phase (a solution containing uranium, thorium and rare earth) and a solid phase (a filter residue containing useful minerals such as monazite, zirconite and rutile). The method is characterized by comprising the following steps of acid leaching, filter pressing and water scrubbing. According to the invention, monazite slags are subjected to low-acid and low-temperature leaching, and a liquid phase and a solid phase are separated easily; after secondary slags are subjected to mineral processing and alkaline decomposition by using a mineral processing process, the closed cycle collection of uranium, thorium and rare earths can be realized; meanwhile, an extract residue waste acid can be subjected to cyclic utilization, thereby reducing the wastewater discharge, reducing the consumption of sulfuric acids and new water and the wastewater treatment cost, and reducing the production cost; and the recovery rates of valuable elements such as uranium, thorium and rare earths can be greater than 97%, therefore, an effect of no radioactive wastewater and waste residue discharge in the whole process can be achieved.
Owner:YIYANG HONGYUAN RARE EARTH

Resource utilization method of high-concentration ammonia nitrogen waste liquid

The invention discloses a resource utilization method of a high-concentration ammonia nitrogen waste liquid. The method comprises the steps as follows: 1, impurity removal: after copper in an etching liquid containing copper is recovered, an ion exchange technique is utilized to absorb and recover low-concentration copper ions in residual high-concentration ammonia nitrogen wastewater, and a regenerative copper chloride raw material is obtained after resin dissolving; and an appropriate amount of barium chloride is added in wastewater without copper so as to remove sulfate radical impurities introduced during a copper sulfate production process; and 2, blending: residual wastewater without copper is the high-concentration ammonia nitrogen wastewater, ammonium chloride concentration is adjusted with an addition method or through evaporation and concentration by a multi-effect evaporator, and then an auxiliary etching liquid is blended according to a corresponding formula and is reused for the circuit board industry. With the adoption of the method, not only is an environmental pollution problem caused by heavy metal ions and the high-concentration ammonia nitrogen waste liquid solved, but also the closed cyclic utilization of the etching liquid of the circuit board industry is achieved, the resource is saved, and the environment is protected.
Owner:惠州TCL环境科技有限公司

Method for treating ammonia nitrogen in tungsten smelting by using extraction absorption

The invention discloses a method for treating ammonia nitrogen in tungsten smelting by using extraction absorption. According to the method, the recovery rate of the ammonia nitrogen is further improved, and the working environment is improved and the production cost is decreased. Primary extraction: organic phase extractants are added to weak aqua ammonia recycled by evaporation to perform extraction to obtain ammonium ions NH4+, and free water and hydroxide ions in ammonia water enter extraction residual liquid water phases; secondary extraction: industrial concentrated hydrochloric acids are added in extracted organic phases, heavy phases after reverse extraction are ammonium chloride at the bottom; light phases containing P507 organic phases enter a next circle for extraction after washing; an reverse extraction solution of an ammonium chloride solution is subjected to ammonia absorption; ammonia water with a concentration of 110g/l returns to a tungsten smelting departure and transfer procedure to serve as an analyzing agent; and final washing: salt-free water is added to organic phases after reverse extraction, organic phase residual ammonium chloride is guaranteed to be discharged as far as possible, an after-washing solution is an ammonium chloride solution, the ammonium chloride solution and the reverse extraction of the last step are subjected to ammonia absorption, and an organic phase extraction agent P507 after washing enters a next circle for usage. The method further improves the ammonia nitrogen recovery rate, the work environment is improved, and the production cost is reduced.
Owner:XIAMEN TUNGSTEN

Ammonia recycling method and system in APT production process

The invention provides an ammonia recycling method and a system in APT production process. The ammonia recycling method comprises following steps: 1, APT crystallization steam is discharged using a centrifugation blower fan, is introduced into a rectifying tower for rectification and condensation of ammonia tail gas to remove most water, and is introduced into a heat exchanger; 2, a three stage solution obtained via ion exchange is directly used for preparing a desorption agent, the rest ammonia nitrogen wastewater is pumped into a stirring tank, an alkali is added for ammonia activation, andgenerated ammonia tail gas is introduced into the heat exchanger; wastewater obtained via ammonia activation is pumped into an air stripping tower, and ammonia tail gas obtained via air stripping is introduced into the heat exchanger; when the ammonia-nitrogen value of obtained air stripping wastewater is detected to be qualified, discharging through a branch pipe is carried out, otherwise, the wastewater is pumped into the air stripping tower for air stripping; and 3, the temperature of the ammonia tail gas is reduced to be lower than 45 DEG C after treatment using the heat exchanger, the ammonia tail gas is introduced into a hydrochloric acid absorbing tower for circulating absorption, and an obtained solution is sent back to the main treatment stream directly for preparation of the desorption agent. The ammonia recycling method and the system are used for comprehensive treatment of ammonia nitrogen wastewater waste gas obtained in tungsten smelting, waste is changed into valuables,the method flow is simple, operation is convenient, the method is easy to control, and cost is low.
Owner:江西铜鼓有色冶金化工有限责任公司

Method for preparing regenerated polyester by closed-loop recovery of waste polyester with typical green and low-carbon characteristics

The invention discloses a method for preparing regenerated polyester by closed-loop recovery of waste polyester with typical green and low-carbon characteristics. The method comprises the steps: selecting a specific depolymerization catalyst to depolymerize waste polyester under a microwave condition; removing a polyol solvent from the depolymerized product, and purifying to remove byproducts to obtain a depolymerized monomer; and mixing the depolymerized monomer with dibasic acid, polyol, a polymerization catalyst and a chain extender, carrying out esterification reaction, adding a stabilizer and a catalyst, and carrying out polycondensation to obtain the regenerated polyester. According to the method, the depolymerization temperature is low, the efficiency is high, the dosage of the polyol solvent is small, and the content of the byproducts is extremely low; meanwhile, the depolymerization catalyst does not need to be separated, co-esterification of the regenerated polyester can be directly carried out, and no adverse effect is caused on the performance of the prepared regenerated polyester. The method provided by the invention can realize closed-loop recovery of waste polyester.
Owner:NAT POLYMER MATERIALS IND INNOVATION CENT CO LTD

A process for recovering ammonia from tungsten smelting ammonia nitrogen wastewater waste gas

The invention relates to a process of recovering ammonia from ammonia-nitrogen wastewater and exhaust gas of tungsten metallurgy. The process is characterized by comprising the following steps: introducing ammonium paratungstate crystal steam and ammonia tail gas into a rectifying tower by virtue of an induced draft fan, maintaining the temperature in a range of 90-95 DEG C and condensing and recovering ammonia by using a steam separator; pumping kettle raffinate and ammonia-nitrogen wastewater which are generated after rectifying the ammonia-nitrogen wastewater into a stirring tank, adding sodium hydroxide for ammonia activation, and adjusting the pH value to 10-11; after ammonia activation, pumping to an air stripping tower, and meanwhile, introducing ammonia wastewater generated by ammonia activation into the air stripping tower, adding sodium hydroxide to adjust the pH value to 10-11.5, and controlling the temperature at 45-90 DEG C and carrying out air stripping for 2 hours; feeding ammonia gas generated in the air-stripping process and ammonia gas which is not condensed by the steam separator into a hydrochloric acid spray tower for circular adsorption to generate ammonium chloride and returning to the main process to prepare an analytical solution. The process provided by the invention is simple in process flow, stable in treatment effect, less in equipment investment, free from secondary pollution and low in treatment cost.
Owner:CNMC GUANGXI PGMA

Blending method of dry coke quenching dust-removal ash in coal blending process

The invention discloses a blending method of dry coke quenching dust-removal ash in a coal blending process. The blending method comprises the following steps: transporting dust-removal ash generated by dry coke quenching every day to a coal storage yard through an ash discharge opening, arranging the dust-removal ash near low-sulfur coking coal of which the content of sulfur is less than 0.4% and low-ash meager lean coal of which the content of ash is less than 8.5% which can be blended for separately storing; according to the blending ratio required by the blending instruction of a forklift in a coal blending workshop, fully and uniformly blending the dry coke quenching dust-removal ash, low-sulfur coking coal and the low-ash meager lean coal at a weight ratio of 1:5:5 to form novel mixed dust-removal ash; conveying the mixed dust-removal ash to a coal blending bin, blending the mixed dust-removal ash and 1 / 3 coking coal, gas coal, coking coal and meager lean coal at a weight ratio of 7: 3 and rich coal to form into-the-furnace coal, crushing the into-the-furnace coal, adding water and conveying to the coal storage bin for coking coal production to replace partial meager lean coal for return blending and coking, wherein the mixed dust-removal ash, the 1 / 3 coking coal, the gas coal, the coking coal and meager lean coal at a weight ratio of 7:3 and the rich coal respectively account for 15%, 32%, 15%, 21% and 17% of the into-the-furnace coal in weight ratio. The process is convenient to operate and has the characteristic of high flexibility.
Owner:山东泰山焦化有限公司

Green cyclic utilization method of honeycomb type denitration catalyst

The invention relates to a green cyclic utilization method of a honeycomb type denitration catalyst, and belongs to the field of flue gas denitration and material cyclic utilization. A regeneration process route and a repreparation process route are set, and a regeneration production line and a repreparation production line are arranged in parallel; a regeneration process or a repreparation process is selected according to the performance of the waste honeycomb type denitration catalyst for green cyclic utilization; and the selection basis of the regeneration process and the repreparation process is as follows: if the axial compressive strength and the radial compressive strength of the waste honeycomb type denitration catalyst are respectively greater than or equal to 1.0 MPa and greaterthan or equal to 0.2 MPa, and the specific surface area is greater than or equal to 40.0 m<2>/g, the regeneration process route is selected, and otherwise, the repreparation process route is selected.According to the green cyclic utilization method of the honeycomb type denitration catalyst, regeneration and repreparation processes are combined, valuable components in the waste denitration catalyst are fully utilized, the use amount of water is greatly reduced, and closed-loop cyclic utilization of the denitration catalyst can be realized.
Owner:UNIV OF SCI & TECH BEIJING

Coke CDQ Dust Removal Ash Mixing Method in Coal Blending Process

The invention discloses a blending method of dry coke quenching dust-removal ash in a coal blending process. The blending method comprises the following steps: transporting dust-removal ash generated by dry coke quenching every day to a coal storage yard through an ash discharge opening, arranging the dust-removal ash near low-sulfur coking coal of which the content of sulfur is less than 0.4% and low-ash meager lean coal of which the content of ash is less than 8.5% which can be blended for separately storing; according to the blending ratio required by the blending instruction of a forklift in a coal blending workshop, fully and uniformly blending the dry coke quenching dust-removal ash, low-sulfur coking coal and the low-ash meager lean coal at a weight ratio of 1:5:5 to form novel mixed dust-removal ash; conveying the mixed dust-removal ash to a coal blending bin, blending the mixed dust-removal ash and 1 / 3 coking coal, gas coal, coking coal and meager lean coal at a weight ratio of 7: 3 and rich coal to form into-the-furnace coal, crushing the into-the-furnace coal, adding water and conveying to the coal storage bin for coking coal production to replace partial meager lean coal for return blending and coking, wherein the mixed dust-removal ash, the 1 / 3 coking coal, the gas coal, the coking coal and meager lean coal at a weight ratio of 7:3 and the rich coal respectively account for 15%, 32%, 15%, 21% and 17% of the into-the-furnace coal in weight ratio. The process is convenient to operate and has the characteristic of high flexibility.
Owner:山东泰山焦化有限公司

A method and application of recovering and preparing titanium-tungsten powder from waste scr denitrification catalyst

The invention relates to a method for preparing titanium tungsten powder by recycling waste SCR denitration catalyst. The method comprises the following steps that the waste SCR denitration catalyst is pretreated so as to obtain pretreated waste catalyst powder; activated treatment is carried on the pretreated waste catalyst powder by using sulfuric acid, and after the waste catalyst powder is cooled and diluted, crude activated slurry is obtained; glass fibers are removed in the crude activated slurry to obtain purified and activated slurry; the activated slurry is heated and purified to obtain a reconstructed slurry; the reconstructed slurry is filtered so as to obtain a solid-phase product and a filtrate; and solid-phase products are sequentially washed, dried and calcined to obtain titanium-tungsten powder products. According to the method, the waste SCR denitration catalyst is converted into the titanium tungsten powder, and the whole process is simple in process, so that the process complexity caused by the step of extracting Ti and W metal components step by step is avoided, the cost is high, the recovery rate of Ti and W exceeds 97%, and the obtained titanium tungsten powder products meet the requirements of industry indexes can completely replace fresh titanium tungsten powder, and are used for production of the SCR catalyst.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI

Classifying and recycling process for waste magnesia carbon bricks produced after use of steel tundish working linings as well as dry material and coating material for tundish

ActiveCN103319189BMaximize recycling rateMaximize regeneration valueSolid waste disposalBrickGranularity
The invention relates to a classifying and recycling process for waste magnesia carbon bricks produced after use of steel tundish working linings as well as a dry material and a coating material for a tundish. The waste magnesia carbon bricks produced after use of the steel tundish working linings are subjected to recovery processing and are classified into reclaimed materials with three grain levels, i.e., the granularity is more than or equal to 3mm and less than 5mm, the granularity is more than or equal to 1mm and less than 3mm and the granularity is less than 1mm; the reclaimed materials with the granularity more than or equal to 3mm and less than 5mm and the granularity more than or equal to 1mm and less than 3mm are used as raw materials to prepare the dry material for the tundish, and the dry material is used for carrying out continuous casting on a slag line 2 and a tundish wall 3 and a tundish bottom 4 below the slag line 2 of the tundish working lining; the reclaimed materials with the granularity more than or equal to 1mm and less than 3mm and the granularity less than 1mm are used as raw materials to prepare the coating material for the tundish, and the coating material for the tundish is used for carrying out continuous costing on a tundish edge 1 above the slag line of the tundish working lining. The invention further provides a construction method for manufacturing the combined continuous casting tundish working lining by adopting the dry material and the coating material for the tundish. According to the classifying and recycling process, the dry material and the coating material for the tundish and the construction method, the classifying and recycling rate of the waste magnesia carbon bricks produced after use of the steel tundish working linings reaches 100 percent.
Owner:LAIWU IRON & STEEL GRP

Method and device for recycling hot-dip copper waste liquid

The invention relates to a method and a device for recycling a hot-dip copper waste liquid. The method comprises the following steps: feeding a waste liquid in a plating solution tank into an oxidation tank, adding hydrogen peroxide into the oxidation tank, adding compressed air into the oxidation tank, stirring 4-6 times to recover the pressure of a gas part at the upper portion of the oxidation tank to normal pressure, adding copper oxide into the oxidation tank, adjusting the pH value of the solution to 3.5-4, keeping for 8-10 hours, draining back the clear liquid in the oxidation tank to the plating solution tank, and after the residual turbid liquid in the oxidation tank is stirred for 8-10 minutes, making the turbid liquid flow into a turbid liquid recycling tank; and after the turbid liquid is subjected to solid-liquid separation, pumping the liquid into the plating solution tank to be reused, and recovering and storing the solid after being dried or air-dried. According to the invention, a copper plating enterprise can remove excessive ferrous ions in a waste liquid on site in a copper plating place by using simple equipment, a convenient process and low cost, copper ions in the waste liquid are recycled, and the ferrous ions are finally converted into a chemical raw material ferric hydroxide, so that closed-loop recycling is realized, high sewage treatment cost is saved for the enterprise, and considerable profits can be earned for enterprises due to cost difference.
Owner:周雪阳

Method for treating ammonia nitrogen in tungsten smelting by using extraction absorption

The invention discloses a method for treating ammonia nitrogen in tungsten smelting by using extraction absorption. According to the method, the recovery rate of the ammonia nitrogen is further improved, and the working environment is improved and the production cost is decreased. Primary extraction: organic phase extractants are added to weak aqua ammonia recycled by evaporation to perform extraction to obtain ammonium ions NH4+, and free water and hydroxide ions in ammonia water enter extraction residual liquid water phases; secondary extraction: industrial concentrated hydrochloric acids are added in extracted organic phases, heavy phases after reverse extraction are ammonium chloride at the bottom; light phases containing P507 organic phases enter a next circle for extraction after washing; an reverse extraction solution of an ammonium chloride solution is subjected to ammonia absorption; ammonia water with a concentration of 110g / l returns to a tungsten smelting departure and transfer procedure to serve as an analyzing agent; and final washing: salt-free water is added to organic phases after reverse extraction, organic phase residual ammonium chloride is guaranteed to be discharged as far as possible, an after-washing solution is an ammonium chloride solution, the ammonium chloride solution and the reverse extraction of the last step are subjected to ammonia absorption, and an organic phase extraction agent P507 after washing enters a next circle for usage. The method further improves the ammonia nitrogen recovery rate, the work environment is improved, and the production cost is reduced.
Owner:XIAMEN TUNGSTEN
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