11results about How to "Promote denitrification" patented technology

The invention discloses a method for enhancing nitrogen and phosphorus removal effects of a whole-course autotrophic nitrogen removal system, and belongs to the technical field of sewage treatment. According to the method, the steel slag powder and the steel slag particles are applied to a nitrification section and a sulfur autotrophic denitrification section respectively, alkalinity consumed by nitrification is supplemented by adding the steel slag powder in the nitrification section, enrichment of nitrifying bacteria is facilitated, metal ions leached from the steel slag powder improve the ammonia nitrogen removal rate, meanwhile, part of phosphate is removed, and the ammonia nitrogen removal rate is increased. The average removal rate of ammonia nitrogen is 99.75%, and the average removal rate of phosphate is 23.22%. According to the invention, the denitrification potential and denitrification effect of the sulfur autotrophic denitrification section are improved, and when the HRT is 3h, the average 97.04% of total nitrogen and the average 86.4% of total phosphorus can be removed; in the denitrification process, metal ions leached from the steel slag can generate precipitates with phosphate, and H < + > generated in the denitrification process can accelerate erosion of the steel slag, so that the phosphorus removal capacity of the steel slag is improved.

The invention relates to the technical field of sewage treatment, in particular to a system for efficiently treating livestock and poultry breeding sewage by utilizing algal-bacterial symbiosis, which comprises a solid-liquid separation module arranged on the ground, the solid-liquid separation module comprises a water inlet pipe, a separation box and a filter basket, a nitrification and denitrification tank is arranged on the top of the ground, and a stirring assembly is arranged in the nitrification and denitrification tank; the chemical phosphorus removal module comprises a coagulation, flocculation and sedimentation tank and a stirring assembly, the coagulation, flocculation and sedimentation tank is arranged on the ground, and the stirring assembly is arranged in a coagulation and flocculation area in the coagulation, flocculation and sedimentation tank; according to the system for efficiently treating the livestock and poultry breeding sewage by utilizing the bacterial-algae symbiosis, compared with an existing method for removing the total nitrogen content in the sewage by independently utilizing microorganisms, pollutants in the sewage are synergistically removed in the oxidation pond by utilizing a bacterial-algae symbiosis structure, microalgae and bacteria, so that the energy consumption and the carbon source are saved, and the environmental pollution is reduced. Meanwhile, the sewage treatment effect is improved.

The invention discloses an anaerobic denitrifying bacterial agent as well as a preparation method and application thereof, and belongs to the technical field of water environment treatment. The anaerobic denitrifying bacterium agent is prepared from the following components in parts by weight: 15 to 30 parts of sterile water, 15 to 60 parts of normal saline, 5 to 10 parts of micro-capsule embedded anaerobic denitrifying bacteria, 5 to 20 parts of a porous composite modified carrier, 10 to 30 parts of a carbon source, 4 to 7 parts of nutrient elements, 2.5 to 4 parts of a buffering agent and 1 to 5 parts of a stabilizer, the micro-capsule embedded anaerobic denitrifying bacteria are obtained by embedding anaerobic denitrifying bacteria with an alginic acid gel solution and a calcium chloride solution; the porous composite modified carrier is obtained by crosslinking modified nano iron oxide, modified nano titanium dioxide, a functional polymer solution and glutaraldehyde. The anaerobic denitrifying bacterial agent provided by the invention can effectively improve the efficiency of treating nitrogen pollution of a water body.

The invention provides a method for treating nitrate wastewater through a three-dimensional electrode biological membrane, and belongs to the technical field of nitrate wastewater treatment. The method comprises the following steps: constructing a cylindrical three-dimensional electrode method bio-membrane reactor by taking activated carbon as a substrate, taking a cylindrical shape enclosed by a plurality of graphite rods as a cathode and taking a middle graphite rod as an anode; the reactor cathode generates H2 under the action of impressed current, autotrophic hydrogen type denitrifying bacteria grow and breed depending on H2 and are attached to the surface of a cathode graphite rod to form a biological membrane, nitrate nitrogen in water can be diffused into the biological membrane, and the biological membrane on the surface of the cathode graphite rod utilizes the generated H2 to reduce the nitrate nitrogen; cO2 is generated at the anode of the reactor and is further converted into carbonic acid, bicarbonate radicals and carbonate radicals, and a carbon source required by growth and reproduction is provided for the autotrophic hydrogen type denitrifying bacteria. According to the three-dimensional electrode bio-membrane reactor, a filling material is added in a two-dimensional reactor structure to serve as a supplementary electrode, and stronger wastewater treatment capacity is brought by a larger surface area.

The utility model discloses a kind of gradient porosity MABR membrane silk assembly structures, including tube sheet, the bottom of the tube sheet is fixedly installed with hydrophobic layer, the inner wall of the hydrophobic layer is fixedly attached with vertical support layer, the hydrophobic layer and vertical support layer are all perforated with air hole, the inside of the vertical support layer is perforated with through hole, the diameter of the straight hole of the one end of tube sheet close to through hole is larger by being set, the one end of tube sheet is gas inlet end, so the gas pressure of the one end of tube sheet close is smaller, the diameter of the through hole of far away gas inlet end is smaller, so the passage cross-sectional area of the one end of tube sheet close is reduced, gas compression leads to gas pressure greater than gas inlet end, so the oxygen content dissolved into external water in unit time will rise, compensate terminal biofilm due to biofilm thickening leads to dissolved oxygen content low Problem, the air hole density of gas outlet end is larger, enhance the oxygen diffusion capacity of terminal, compensate oxygen transfer attenuation due to biofilm thickening, avoid terminal anoxia, promote outer layer denitrifying bacteria enrichment.

The invention provides an electric arc furnace bottom blowing oxygen-containing multi-element gas clean smelting method, and relates to the field of metallurgy. The method comprises the following steps: starting smelting, inputting a standard safe pressure value Pf into a main control system, and inputting a standard safe temperature value Tf into the main control system; when the temperature T of the molten pool is smaller than 1500 DEG C, the electric arc furnace is subjected to bottom blowing through argon; and when the temperature T of the molten pool is larger than or equal to 1500 DEG C, argon and oxygen-containing gas including oxygen and carbon dioxide are adopted in the electric arc furnace for bottom blowing, and the proportion and flow of the oxygen-containing gas are adjusted according to the C content of the molten pool, the bottom blowing pressure and the temperature. According to the method, oxygen-containing gas reacts with elements in steel, the utilization efficiency of oxygen in the molten steel is improved, the stirring capacity of a molten pool is enhanced, dephosphorization and denitrification of the molten steel are promoted, and it is guaranteed that components of the molten steel reach the standard. Meanwhile, the influence of oxygen-containing gas on the service life of a bottom blowing element is relieved, the smelting period is shortened, the production efficiency is improved, the smelting cost is reduced, and efficient and clean smelting of the electric arc furnace is achieved.

The present application provides a kind of ecological purification method for treating aquaculture tail water, and is sequentially provided with multifunctional drainage ditch, ecological oxidation dam, stable sedimentation pond, continuous biological filter pond and composite purification bed along the direction of aquaculture tail water flow.The garbage intercepting device, ecological revetment and buffer zone are arranged in the multifunctional drainage ditch;The ecological weir, ecological frame, fixed pile, water collecting wall and lifting pump are arranged in the ecological purification dam;The floating plant area, multiple interception and purification devices and aeration device are arranged in the stable sedimentation pond;The culture area is arranged in the continuous biological filter pond, and after the water flow passes through multiple aeration biological filter areas, it enters the effluent area uniformly;The composite purification bed includes plants, improved substrate layer, purification layer, filtration and water collection layer, impermeable layer and effluent area.The method can effectively remove the refractory pollutants and toxic and harmful substances in aquaculture tail water, has low construction cost, small land area, low operation and maintenance cost, and the effluent can be resource utilization.

This invention relates to the field of water treatment technology, specifically disclosing a hydraulically driven continuous flow aerobic granular sludge-membrane filtration integrated device and its application. The device includes an influent system, an effluent system, a reactor shell, a membrane module, and an aeration module. A first baffle is installed inside the reactor shell, dividing the interior into an anoxic zone and an aerobic zone. A multi-stage flow guiding mechanism is vertically arranged within the anoxic zone to change the flow direction of the sludge-water mixture. The aeration module is located at the bottom of the aerobic zone, enabling the sludge-water mixture to circulate between the anoxic and aerobic zones. The membrane module is located within the aerobic zone and positioned above the nano-aeration disc. This invention achieves favorable hydraulic conditions under continuous flow, creating a driving force for granulation and enabling rapid formation and stable operation of aerobic granular sludge. The combination of aerobic granular sludge and membrane module filtration improves effluent quality, reduces membrane fouling, shortens the process flow, and reduces floor space requirements.

This invention discloses an integrated device and a method for rapid cultivation of aerobic granular sludge suitable for low-concentration domestic sewage, along with its application. The device comprises a batch reactor body integrating the following functional units: a full-area water distribution unit, including a main inlet pipe and distributed water distribution components; one end of the main inlet pipe is connected to the sewage source, and the other end extends to the bottom of the reactor cavity; the distributed water distribution components are connected to the main inlet pipe and equipped with multiple water distribution holes; a dual-zone aeration unit, including an air pump, a bottom aeration unit with a wide range of adjustable air volume, and a middle aeration unit with precise air volume control; a flow field optimization unit, located at the upper part of the reactor cavity and connected to the main inlet pipe; and a timing control unit, electrically connected to the full-area water distribution unit and the dual-zone aeration unit. The advantages of this invention are: by creating sedimentation selective pressure through dual-zone aeration to achieve sludge stratification, enhanced denitrification of heavy granular sludge, and removal of excess phosphorus from light flocculent sludge, it also has the advantages of shortening the cultivation cycle of aerobic granular sludge and highly efficient denitrification and phosphorus removal.

The present invention discloses a circulation type continuous flow aerobic granular sludge sewage treatment system, and relates to the technical field of sewage treatment, the circulation type continuous flow aerobic granular sludge sewage treatment system comprises a structure pool, the structure pool is provided with an inner cavity, and the inner cavity is divided into a deoxidation cavity, an anaerobic cavity, an anoxic laminar flow cavity and a composite cavity; one end of the water inlet mechanism is communicated with sewage, and the other end is communicated with the deoxidation cavity; one end of the water outlet mechanism is communicated with the composite cavity; an overflow port communicated with the anaerobic cavity is formed in the upper part of the deoxidation cavity; a communication port communicated with the anoxic laminar flow cavity is formed in the bottom of the anaerobic cavity; the anoxic laminar flow cavity is provided with a deep tank homogeneous circulation mixing module; the composite cavity is divided into a plurality of communicated sub-cavities, and the sub-cavities are respectively an aerobic cavity and a precipitation screening cavity; the anoxic laminar flow cavity is communicated with the aerobic cavity; the precipitation screening cavity is communicated with a water outlet mechanism, and a sludge interception screening device is arranged below the water outlet position of the precipitation screening cavity. The sewage treatment device has the effects of reducing the sewage treatment cost and improving the sewage treatment stability and efficiency.

The utility model provides a kind of high-efficiency preheating of scrap steel ladle heating device, the device includes top open ladle, ladle cover is covered on the ladle opening, heating burner is set on the ladle cover.The device further includes the retaining wall with closed shape in cross section.The top of the retaining wall is connected with the ladle cover, and the bottom of the retaining wall is close to the scrap steel material surface in the ladle.The internal area enclosed by the retaining wall constitutes the combustion zone of heating burner, and the area between the retaining wall and the side wall of the ladle forms the flue gas discharge channel.The heating burner is arranged on the ladle cover at the corresponding position of the combustion zone.A flue gas outlet is further arranged on the ladle cover at the corresponding position of the flue gas discharge channel.The utility model realizes the preheating of scrap steel by the way of high-temperature flue gas penetrating scrap steel, so that the high-temperature flue gas and scrap steel carry out convection heat transfer, thereby greatly improving the uniformity of preheating temperature and overall preheating temperature of scrap steel, and realizing the high-efficiency preheating of scrap steel.