2837results about How to "Achieving zero emissions" patented technology

The invention discloses recovery process of honeycomb type selective catalytic reduction (SCR) waste catalyst. The process includes the following steps: a, preprocessing the SCR waste catalyst and leaching at the high temperature and under high pressure; b, adding hydrochloric acid into leaching liquid, adjusting pH, and removing impurities; c, adding hydrochloric acid into the leaching liquid, reacting, calcining and preparing rutile titanium dioxide; d, preparing ammonium paratungstate; e, preparing ammonium metavanadate; and f, recycling and treating waste water. Main products of ammonium paratungstate, ammonium metavanadate and rutile titanium dioxide obtained in the process are high in purity and recovery rate. By-products of silicon magnesium slags, salty mud, high-concentration sodium chloride liquid and barium sulfate dregs are high-purity harmless useful goods. The process is free of harmful secondary pollutant emission, environment-friendly and capable of circulating, has high economical and social benefit and is practicable.

The invention relates to a membrane and evaporation crystallization integrated process with zero discharge of high-salinity industrial wastewater. The process is as below: carrying out ultrafiltration pretreatment on industrial wastewater and sending the wastewater to a reverse osmosis process through a high-pressure pump; reusing lateral infiltration water; conducting electrodialysis treatment on a concentrate subjected to several times of filtration; evaporating and crystallizing the materials obtained from electrodialysis concentration to obtain salt slurry and water; carry outing posttreatment on the salt slurry; and reusing condensed water. The process provided by the invention couples membrane and evaporation crystallization, not only can recover high quality purified water from industrial wastewater with high salinity but also can realize zero discharge of wastewater with high salinity, and has the characteristics of low energy consumption, low production cost and advanced process.

The invention provides a processing method for reducing and recycling organic waste water. The method comprises steps: (1) pre-treating waste water to obtain pre-treated out-water; (2) treating the out-water obtained from the step (1) through solid-liquid separation; (3) nano-filtering the out-water obtained from step (2); (4) treating nano-filtered concentrated water obtained from the step (3) to obtain out-water subjected concentrated water nano-filtering, returning to the step (3) for mixing the out-water subjected to concentrated water nano-filtering with the out-water subjected to solid-liquid separation, and performing nano-filtering; (5) performing first reverse osmosis treatment on out-water obtained from the step (3) through nano-filtering; (6) performing second reverse osmosis treatment on concentrated water obtained from the step (5) through first reverse osmosis treatment; and (7) evaporating and crystallizing a concentrated liquid obtained from the step (6) through second reverse osmosis treatment in order to obtain crystallized salt and evaporated concentrated water. The invention further provides a processing system of the method. Through the method and system, waste water is truly reduced and recycled.

A high-hydrophobicity, heat conductivity and adhesivity pigment of interface is prepared by taking methyl chloroform and butanone as medium, liquid-phase treating ordinary carbon black by silicone oil to hydrophobic activate, forming coating into dense methyl surface by polyester modified dimethylsilicone and agitation dispersing by supersonic homogenizer. The formed coating (2) is three-dimensional cross-linking network of cured polyphenylene methyl resin, which contains nanometer carbon black and silicon dioxide, and it forms dense methyl thin layer (3) on coating surface. It can be used to treat heat exchanger surface (1) of indoor apparatus and outer tube fin of household air conditioner. It has good hardness and is non- toxic.

A method for detaching and recovering the electronic elements and solder from the rejected circuit board includes uniformly heating said circuit board until the solder is molten, sucking the electronic elements from the molten solder, and solidifying the solder.

The invention discloses a method for cooperatively promoting agglomeration growth of PM (particulate matter) 2.5 and treating desulfuration wastewater in an evaporation manner and a device of the method. The method particularly includes steps that agglomeration liquor prepared by desulfuration wastewater, high polymer adhesive and wetting agent is sprayed into an inlet flue of an electric precipitator and is evaporated by the aid of heat of flue gas, in an evaporation process, the wetting agent promotes dust to enter drops of the agglomeration liquor, the high polymer adhesive is connected with PM2.5 via a polymer chain with polar groups, the grain diameter of the PM2.5 is prompted to be enlarged, so that the PM2.5 can be gathered by the follow-up electric precipitator, the desulfuration wastewater is evaporated completely, suspended matters and dissolvable pollutants in the wastewater are converted into solid to be dissolved out, and the suspended matters and the dissolvable pollutants in the wastewater, together with dust in the flue gas, are gathered by the electric precipitator. The device consists of a boiler, an air preheater, the electric precipitator, a desulfurizing tower, a hydraulic cyclone, a desulfuration wastewater clarification tank and an agglomeration liquor preparation tank, and a double-fluid atomizing nozzle is arranged in the flue between the air preheater and the electric precipitator.

The invention relates to a novel equipment and a method of ethanol fuel production. The water resource in a preparation unit of liquefied wort is the washing water in a CO₂ washing tower. A recovery tower pot collects waste water and a portion of liquor condensate by vaporing when waste water is dealt with to send to a mixing machine of the preparation unit of liquefied wort. And the consumption of fresh water is zero. The process of rectification and dehydration adopts technology of multieffect thermal coupling rectification. Only when the recovery tower pot uses fresh vapor to heat, the energy consumption of the process of rectification and dehydration is reduced largely. The waste wort solution produced by the alcohol production process which is dealt with by the device for pneumatic drying, multieffect evaporation of clear liquid, being anaerobic and oxygen consumption of the vapored condensate liquor and purifying by using ultrafiltration membrane etc, can be recovered with the valuable product. The reasonable treatment plan realizes zero discharge of technique waste water when in the ethanol fuel production.

The invention discloses a double-chamber alga microbial fuel cell and a method thereof for treating waste water and realizing zero carbon emission, which relates to a microbial fuel cell and a method for treating waste water. The invention solves the problem that the traditional microbial fuel cell can generate a large amount of CO2 in the process of treating waste water. In the invention, a cation exchange membrane is vertically arranged in a box body of a reactor; an anode chamber and a cathode chamber are formed in the box body of the reactor; an anode is arranged in the anode chamber; a cathode is arranged in the cathode chamber; leads are connected with the anode and the cathode; one end of a gas duct is hermetically connected with a gas collecting chamber, and the other end of the gas duct is arranged at the bottom of the cathode chamber; and a gas collecting device is hermetically installed at a gas outlet. The method comprises the following steps: (1) starting the reactor; and (2) introducing the waste water into the cathode chamber and the anode chamber, catabolizing organic matters by microbes at room temperature, simultaneously obtaining electrical energy, and introducing the CO2 generated in the anode chamber into the cathode chamber to be used by the alga at the cathode for photosynthesis. The invention realizes zero emission of CO2 and simultaneously can recover electrical energy, thereby really changing waste into resources.

The invention relates to a heating method of deep geothermal renewable energy sources in winter, which is pollution-free, zero-emission, clean, renewable and low-cost. The technical scheme comprises drilling a deep well under the ground, driving sleeve pipes, insulation treating for the sleeve pipes in a non-effective heating depth area under the well, employing circulating water to collect heat energy contained in underground deep rock in an effective heating depth area through the walls of the sleeve pipes, and employing insulation suction pipes to transmit the heat energy to the ground through water circulation to heat targeted users, after radiation, returning low-temperature water to underground via the insulation suction pipes, and collecting the heat energy contained in underground deep rock in the effective heating depth area through the walls of the sleeve pipes again to form a circulating heating system. The heating method for winter has the advantage that the heating method can realize zero-emission, is renewable with extremely low running cost and simple operation, and can benefit people for a lifetime after once investment. The heating method is a key breakthrough of the present heating and energy-saving method, which can largely ease the present supplying situation of winter heating energy, and really realizes energy conservation and emission reduction.

The invention relates to a recycling treatment process for coal coking high-salinity wastewater. The process comprises the following steps: (1) fluorine removing; (2) silicon removing; (3) softening;(4) treatment with a multi-medium filter; (5) ultrafiltration; (6) resin softening; (7) FDG; (8) nanofiltration and salt separation; (9) reverse osmosis concentration; (10) advanced oxidation; (11) resin adsorption; and (12) evaporative crystallization. The process has the advantages that the process of pretreatment, nanofiltration salt separation, reverse osmosis concentration, advanced oxidationand evaporative crystallization is adopted, so that zero emission and quality-divided resource utilization of the coal coking high-salinity wastewater are realized.

The invention discloses a technology method for treating desulfurization wastewater, which are applicable to treating the wastewater generated from limestone-plaster wet flue gas desulfurization and other wastewater with high salt content. The method uses the flue gas of heat-engine plants to carry out evaporation and solidification treatment to the desulfurization wastewater or other wastewater with high slat content which is hard to be recovered. The method is characterized by low cost, little area occupation and low energy consumption, which can provide help to the original limestone-plaster wet flue gas desulfurization treatment technology and realize zero discharge of the wastewater of the limestone-plaster wet flue gas desulfurization technology.

The invention discloses a reclaimed craft to dispose electroplating waste water, which comprises the following steps: adopting oxidation-reduction and chemical precipitation disposing method and film technology (fold filtration, hyperfiltration, Na filtration and reverse osmosis desalination) deep purifying method; avoiding accumulation of salt effectively; reverse osmosis sloughing monovalent salt at last grade; trapping bivalent salt in innocent treatment system; proceeding depositing treatment continually; removing accumulating BOD and COD in water body through biochemical treatment effectively; realizing zero discharge of waste water.

The invention belongs to the technical field of chromium residue detoxifying, and discloses a chromium residue detoxifying process. The process comprises the following steps of: performing wet grinding on chromium residue, adding water into the chromium residue to prepare chromium residue slurry; and after being subjected to acid-leaching reduction reaction, performing solid-liquid separation on the chromium residue slurry to obtain a filter cake, namely the detoxified chromium residue. The process is characterized in that: under the condition of not changing the original alkaline environment of the chromium residue, a reducing agent 1 is added into the chromium residue directly, and then the reducing agent and the chromium residue are subjected to wet grinding to form particles with 100 to 300 meshes; and the water is added to prepare the chromium residue slurry with 30 to 45 baume degrees, wherein the reducing agent 1 is sodium sulphide, sodium bisulfide, sodium thiosulfate or sodium pyrosulfite. The process has simpleness, thorough detoxification, no chromium return phenomenon and easy implementation of mass production; and the process prolongs effective reduction reaction time, improves reaction efficiency, saves the using amount of acid during the acid-leaching reduction, and has low processing cost because Cr6+ in the chromium residue is subjected to two times of dissolution and reduction.

The invention discloses a method and a device for treating garbage percolate, wherein the method comprises the steps of pretreatment, anaerobic treatment, membrane biochemical treatment, nanofiltration treatment, sludge treatment and the like; the device comprises a primary sedimentation tank (1) and an adjusting tank (2), the adjusting tank (2) is connected with an anaerobic reactor (3), the anaerobic reactor (3) is connected with a denitrification tank (4), and the denitrification tank (4) is communicated with a nitrification tank (5); and the nitrification tank (5) is connected with an ultrafiltration apparatus (6), and the ultrafiltration apparatus (6) is connected with a nanofiltration device (7). The method and the device achieve COD degradation of high-concentration wastewater so that the COD of high-concentration COD of 50,000 reaches about 50 after treatment and reaches the standard of industrial reuse water, thus the method and the device achieve zero discharge of the percolate, initiate a new attempt to treat high-concentration percolate, and fill up the domestic blank.

The invention relates to a method for extracting high-quality soybean germ oil by using subcritical butane and relates to the field of grain fine and deep processing. The method comprises: cutting purified soybean germs into slices which are 0.3 to 0.4 millimeters thick; placing the slices in an extraction kettle; performing 1 to 5 times of countercurrent leaching of the cut soybean germs by using liquefied butane as a solvent, wherein the extraction time is 10 to 120 minutes, the material to liquid ratio is 1:(1-6), the extraction temperature is 10 to 90 DEG C, and the extraction pressure is0.2 to 0.1MPa; delivering extracted mixed oil and wet dregs into an evaporation system and desolventizing under reduced pressure; and subjecting the obtained soybean germ crude oil to normal winterization, alkali refining and decolorization processes to obtain a soybean germ oil product with high beta-sitosterol content. In the invention, the soybean germ oil is extracted by using subcritical butane, the manufacturing cost of equipment is reduced considerably, the operation cost is low, the production period is shorter, the yield is high, and the method represents a low-consumption and environment-friendly practical technique for producing soybean germ oil.

The invention discloses a technology for preparing liquefied natural gas and liquid ammonia by using coke oven gas. The coke oven gas is subjected to the steps of compression, purification, methanation, cryogenic separation and liquefaction of synthetic natural gas, variable pressure adsorptive separation and liquid ammonia preparation with hydrogen rich gas, so that the liquefied natural gas (LNG) of which methane purity is more than 99 percent and the liquid ammonia reaching national first level standard are obtained. By the technology, the hydrogen byproduct of the coke oven gas for preparing the LNG is fully utilized; effective ingredients of the coke oven gas such as H2, N2, CH4, CO and CO2 are furthest utilized; the CO and the CO2 are methanated, so that the yield of the CH4 is improved by about 1/3; the liquefied CH4 is used as the LNG and sold; and the rest nitrogen-containing hydrogen-rich gas is used as a raw material for synthesizing ammonia, so that the additional value of the coke oven gas is improved, and reliable raw material guarantee is provided for developing downstream products with high additional values and prolonging the product chain.

The invention discloses a high-salt waste water zero emission and salt separation processing method and device. The method includes the following steps of 1, waste water preprocessing, 2, waste water decrement and concentration and 3, crystallization. By means of the high-salt waste water zero emission and salt separation processing method and device, waste water can be processed efficiently, liquid and salt ingredients in the waste water are effectively separated, a product obtained after waste water can be recycled or sold as other industrial products, so that zero emission of waste water is achieved. The method is simple and easy to implement, high in processing efficiency and small in energy consumption; by the adoption of the method, pollution to the environment is avoided, an active function is played on improvement of regional water environment quality, the utilization rate of waste water is raised, production cost is saved, and environmental and social benefits are quite remarkable. The device is high in operation efficiency, convenient to assemble, low in cost and small in energy consumption.

The invention discloses a coal chemical strong brine zero emission and salt screening technology. Strong brine enters a first special reverse osmosis process pack after being treated by an adjusting pond and a pre-treatment device, freshwater of the strong brine is reused, water produced on the thick water side passes through a softening process pack to remove calcium ions and magnesium ions in wastewater and then enters a first-stage special nanofiltration process pack, water produced on the thick water side of the first-stage special nanofiltration process pack passes through a first evaporation crystallization process pack to obtain industrial-grade sodium sulfate, water produced on the fresh water side enters a second-stage special nanofiltration process pack, water produced on the thick water side of the second-stage special nanofiltration process pack returns to the adjusting pond, water produced on the fresh water side enters a reverse osmosis membrane process pack, the fresh water is reused, water produced on the thick water side enters a second special reverse osmosis membrane process pack, water produced on the fresh water side of the second special reverse osmosis membrane process pack flows back to the adjusting pond or is reused according to water quality, and water produced on the thick water side passes through a second evaporation crystallization process pack to obtain industrial-grade sodium chloride. The technology is simple, cost is low, the automation degree is high, long-time stable operation can be achieved, and secondary pollution is not caused.

The invention provides a technique for treating and recycling lead-zinc ore dressing wastewater and aims to solve the problems of influence on the ore dressing index due to the recycling of the ore dressing wastewater for production and environmental pollution caused by drainage. The novel technique for treating and recycling the lead-zinc sulfide ore dressing wastewater comprises the steps of: adjusting the pH value of the total wastewater of an ore dressing plant; adding ferrous sulfate and flocculant into the wastewater to perform oxidation-coagulation treatment; and oxidizing the treated water by using chlorine dioxide, and performing catalytic oxidation and adsorption by using an active carbon bed, so that the treated water reaches the relevant discharge standard of China; and totally recycling the treated water by adopting the combined application of potential-controlled flotation and an environmental-protection collector. Compared with the field process technique, the method saves the cyanide flotation process and improves the recovery rates of lead, zinc and gold. The method provides whole technical integration of the combined application technique of the potential-controlled flotation and the environmental-protection collector and the wastewater treatment technique for the treatment and recycling of the lead-zinc ore dressing wastewater, and realizes recycling of the ore dressing wastewater.

The invention provides a method for treating industrial wastewater with a high salt content. The method includes steps of pretreating the industrial wastewater with the high salt content, to be more specific, regulating and homogenizing the industrial wastewater with the high salt content by the aid of a high-salinity water regulating tank, then feeding the industrial wastewater into a high-density sedimentation tank, carrying out chemical softening treatment and flocculation sedimentation on the industrial wastewater, simultaneously removing most silicon dioxide and suspended matters, feeding water treated by the high-density sedimentation tank into an immersed ultra-filtration tank and further removing suspended matters and colloidal impurities in the water; carrying out separation and concentration, to be more specific, concentrating and separating the industrial wastewater with the high salt content after the industrial wastewater is pretreated at the pretreatment step, or carrying out ion exchange treatment on the industrial wastewater; recycling crystals, and to be more specific, separating the sodium chloride crystals and the sodium sulfate crystals from the water by the aid of crystallizers. The invention further provides a device for treating the industrial wastewater with the high salt content.