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164results about How to "Solve the bloat problem" patented technology

Sewage treatment process and special-purpose one-piece sewage treatment plant

The invention discloses a sewage treatment process and a special-purpose one-piece sewage treatment plant. The process comprises the following steps: 1) arrangement of a water inlet system: sewage input from an inlet pipe and pretreated by thick and fine gratings and a vortex-type grit chamber is sent into a biological reaction system; 2) arrangement of the biological reaction system: the biological reaction system is divided into an anoxic area, an anaerobic area, an aerobic area and a sedimentation area, and activated sludge in each area utilizes katabolism of microbes to converse organic matters into inorganic matters to realize nitrogen and phosphorus removal; 3) arrangement of the sedimentation basin: sludge and water in the treated sewage can be separated, so that the water outlet is clarified; and 4) arrangement of a disinfection tank: the treated water from the step 3) is disinfected to kill pathogenic organisms and then discharged through an outlet pipe. The invention also discloses a one-piece sewage treatment plant. The invention has the advantages of small land occupation, small investment, compact mechanism, low loss of a water head, low investment for the engineering project, optimized, stable and mature technology, good nitrogen and phosphorus removal effect and good organic pollutant removal effect.
Owner:王胜初

Treatment process for bearing production wastewater

The invention discloses a treatment process for bearing production wastewater. The treatment process comprises the following steps: firstly, enabling bearing production wastewater to enter an oil-separation adjusting tank; separating floating oil in the wastewater and agitating uniformly; then lifting the wastewater into a cavitation air floatation system to remove suspension matters and petroleum in the wastewater; conveying the wastewater treated by the cavitation air floatation system into an iron-carbon micro-electrolysis reactor and carrying out a Fenton reagent and iron-carbon micro-electrolysis combined oxidation reaction to reduce chemical oxygen demand and improve the ratio value of biochemical oxygen demand / chemical oxygen demand of the wastewater; conveying the wastewater reacted in the iron-carbon micro-electrolysis reactor into a coagulation precipitation tank, adjusting the pH (Potential of Hydrogen) and carrying out a coagulation and flocculation reaction; enabling reacted liquid supernatant to flow into a middle water pond to sequentially enter a UASB (Up-flow Anaerobic Sludge Bed / Blanket) anaerobic reaction tank, a CASS (Cyclic Activated Sludge System) reaction tank and a water discharging tank and filtering by a multi-medium filter; discharging after the water reaches standards. The treatment process is simple in management and good in wastewater treatment effect; a sludge expansion problem which usually and easily occurs in a traditional active sludge method is overcome; the water can be discharged after the water quality reaches the standards and the treatment process is good for protecting the ecological environment.
Owner:ANHUI GREEN TITAN ENVIRONMENTAL TECH

Novel sewage treatment process utilizing ferrate oxidization to reduce sludge quantity

A novel sewage treatment process utilizing ferrate oxidization to reduce sludge quantity comprises the steps that a emical treatment unit effectively removes and converts organic pollutants into inorganic small molecular substance through microorganism in a biochemical treatment system, and the certain sludge concentration in the biochemical treatment unit is maintained; in a sediment unit, sewage produced after the treatment of the biochemical treatment unit enters a secondary sedimentation tank to perform sludge-water separation, a part of subsided sludge is excess sludge, the rest is returned sludge, and two third of returned sludge directly enters the biochemical treatment unit; in a ferrate oxidization treatment unit, one third of returned sludge enters a sludge reaction tank to react with input ferrate for 10-30 minutes, wherein the mass ratio of the ferrate to the excess sludge is 0.2:1; and a sludge dewatering unit performs filter pressing or centrifugal dewatering of the excess sludge. The novel sewage treatment process can reduce 35-45% of excess sludge quantity, has the advantages of being simple in devices, few in investment, free of pollution, convenient to operate and manage, low in operation cost and the like, and is suitable for application of industrial municipal sewage treatment plants.
Owner:NINGBO UNIVERSITY OF TECHNOLOGY

Alkaline zinc-manganese dioxide cell

The invention relates to the field of alkaline zinc-manganese dioxide cells, and specifically relates to an alkaline zinc-manganese dioxide cell. The alkaline zinc-manganese dioxide cell comprises a positive electrode cap (1), a positive electrode ring (2), a steel shell (3), a current collector copper nail (4), a negative electrode zinc gel (5), diaphragm paper (6), a sealing ring (7), a supportring (8) and a negative electrode bottom (9); the positive electrode ring (2) is composed of electrolytic manganese dioxide, conductive agent graphite and electrolyte; and the negative electrode zincgel (5) comprises zinc powder, a binding agent, an expanding agent, an electrolyte potassium hydroxide solution and polyethylene glycol 2000. According to the alkaline zinc-manganese dioxide cell provided by the invention, the discharge performance of the alkaline zinc-manganese dioxide cell is not influenced or even slightly improved, and the problem of expansion of the zinc gel is effectively solved; and meanwhile, the hydrogen content of the cell is remarkably reduced, and the liquid leakage risk of the cell is greatly reduced, therefore, the discharge performance of the cell is effectivelyimproved, the storage life of the cell is prolonged, and the safety performance of the cell is remarkably improved.
Owner:GUANGDONG LIWANG NEW ENERGY

Process for separation of acid and salt in salt-containing waste acid

The invention discloses a process for separation of acid and salt in salt-containing waste acid. The process includes: subjecting salt-containing waste acid to multi-period adsorption-elution treatment by an acid adsorption resin column, during adsorption, passing waste acid return liquid, residual waste acid liquid and a salt-containing waste acid stock solution obtained in a previous period sequentially through acid adsorption resin from the bottom up for acid adsorption, collecting residual elution water, deacidified salt-containing liquid and waste acid return liquid successively, stoppingliquid feeding after the volume meeting the requirement, completely feeding salt-containing waste acid in the first period, during elution, passing elution water return liquid, residual elution waterand elution water obtained in a previous period through acid adsorption resin from top to bottom in sequence for elution, and collecting residual waste acid liquid, desalted acid-containing liquid and elution water return liquid successively, stopping water inflow after the volume meets the requirement, completely feeding elution water in the first period, and performing repetition till completing treatment of the salt-containing waste acid. The process disclosed by the invention can be used for separation of various acids and cations, has good separation effect, is not limited by the heightof the resin column, does not generate volume expansion, and has wide applicability.
Owner:CHANGSHA HASKY ENVIRONMENTAL PROTECTION TECH DEV CO LTD

Filamentous sludge bulking recovery method based on non-nitrification A/O (anaerobic/aerobic) biological phosphorus removal process

The invention relates to a filamentous sludge bulking recovery method based on a non-nitrification A / O (anaerobic / aerobic) biological phosphorus removal process, and belongs to the field of urban domestic sewage treatment and regeneration. In virtue of an A / O biological phosphorus removal reactor, filamentous bulking is recovered in two stages, and the filamentous sludge bulking recovery method comprises the following steps: firstly keeping load at 0.40-0.50kg COD (chemical oxygen demand) / kg MLSS (mixed liquor suspended solid) / d, regulating reflux ratio to 75%-85%, controlling the aeration of an aerobic stage to form DO (dissolved oxygen) gradient aeration of 1.4mg / L-1.6mg / L, 0.9mg / L-1.0mg / L and 0.9mg / L-1.0 mg / L to eliminate filamentous fungi, reducing the reflux ratio to 45%-55% when an SVI (sludge volume index) value is reduced into the range of 180mL / g-250mL / g, and reducing the aeration to form the DO gradient of 0.9mg / L-1.1mg / L, 0.4mg / L-0.6mg / L and 0.4mg / L-0.6mg / L. Under the operation parameter conditions, the filamentous bulking caused by the DO and high-load impact (1.54kg COD / kg MLSS / d) can be recovered rapidly, the SVI is reduced from 569.8mL / g to below 150mL / g, and the recovery time of bulking of the lighter filamentous fungi is shorter.
Owner:BEIJING UNIV OF TECH

Ammonia-cooled ammonia reclamation method and mating device thereof

The invention discloses an ammonia-cooled ammonia reclamation method and a mating device thereof. Gas phase ammonia in purge gas is condensed into liquid ammonia by using the principle of ammonia decompressed evaporation and refrigeration, and the separated liquid ammonia is used as a refrigerant for continuously cooling the gas phase ammonia in the purge gas, over and over again. The eliminated high-pressure equipment and pipelines which still can be continuously used in the ammonia synthesis process are used for decompression to form an ammonia-cooled ammonia reclamation device, wherein the device comprises a purge gas pipeline, a cold and heat exchanger, an ammonia evaporation condenser and a liquid ammonia storage tank; and the formed ammonia-cooled separation circulating process in the purge gas is characterized in that: the liquid ammonia prepared from the purge gas is conveyed into the ammonia evaporation condenser and evaporated into gaseous ammonia so as to obtain a large amount of cold energy, and the gaseous ammonia in the purge gas is continuously cooled so as to fulfill the purpose of separating the gas phase ammonia in the purge gas. The device has the advantages of energy conservation, low investment and good usability.
Owner:甘肃金昌化学工业集团有限公司

Biomass double-shaft screw pyrolysis device

The invention discloses a biomass double-shaft screw pyrolysis device. The biomass double-shaft screw pyrolysis device comprises a hollow cylindrical enclosure with a U-shaped cross section, wherein an opening of the hollow cylindrical enclosure is sealed by a seal cover of a machine cover, thereby forming a sealed reaction region; the reaction region formed in the enclosure in the axial direction is sequentially divided into a plurality of individual pyrolysis sub regions; the cylinder wall of the enclosure is of a hollow sandwiched structure so as to act as a flue gas channel; the enclosure is centrally provided with double-shaft screw packing augers which penetrate through the reaction region axially; the rotation directions of the two packing augers are opposite; biomass entering from a biomass inlet is mixed and conveyed by the double-shaft screw packing augers, is baked in the baking sub regions sequentially, and is respectively subjected to catalytic gasification and reforming in gasification sub regions and reforming sub regions, so that high-quality synthesized gas products are generated and are discharged from a pyrolysis gas outlet. The biomass double-shaft screw pyrolysis device intensifies the material mixing and heat transferring and mass transferring effects; biomass is gasified efficiently by adopting the inner and outer thermal combination and catalytic effect, so that the problem of axial and radial breathing of the screw pyrolysis device in running at high temperature is solved.
Owner:HUAZHONG UNIV OF SCI & TECH

UPS (Uninterrupted Power Supply) storage battery detection device

The invention provides a UPS (Uninterrupted Power Supply) storage battery detection device. The UPS storage battery detection device comprises an MCU (Main Control Unit) control module (1), a sensor module (2), a key input module (3), an LCD display module (4), a wireless communication module (5) and an I / O reserved port (6),wherein the MCU control module takes the Charge Time Measurement Unit (CTMU) embedded in PIC series single chips of a Microchip Company, works in cooperation with an A / D (Analogue / Digital) converter, and can be used for accurately measuring time, capacitance and relative change of the capacitance, the sensor module (2) is provided with a high-precision capacitive touch sensor for data acquisition and used for converting micro-deformation caused by the swelling of the UPS storage battery into the variable quantity of the capacitance, and the I / O reserved port (6) is used for driving a peripheral circuit. The UPS storage battery detection device is capable of effectively improving the accuracy and the speed of detection on the UPS storage battery, and has the characteristics of simple structure, low price and the like. The problem of battery swelling resulting from bad battery protection circuit, poor performance of a charger and the like is solved, the current situation of difficult maintenance of the UPS storage battery is improved, and meanwhile, potential safety hazards are avoided.
Owner:SHANGHAI UNIV

Oxidation ditch process with functions of preventing and controlling activated sludge bulking

The invention relates to an oxidation ditch process with functions of preventing and controlling activated sludge bulking. The oxidation ditch process is characterized by comprising the following steps of: making sewage enter an anaerobic zone; mixing the sewage with sludge output from a hypoxic preconditioning zone for reacting in the anaerobic zone; making a mixed solution output from the aerobic zone enter an oxidation ditch; reacting the mixed solution in the oxidation ditch, and making the reacted mixed solution enter a secondary precipitation basin through an outflow channel of the oxidation ditch for sludge-water separation; discharging supernatant produced in the secondary precipitation basin from a water outlet; refluxing a part of sludge produced in the secondary precipitation basin into a pre-concentration basin; discharging the residual sludge out of a system; conveying high-concentration sludge formed at the bottom of the pre-concentration basin to a hypoxic preconditioning basin; and conveying supernatant formed on the upper part of the pre-concentration basin to the outflow channel of the oxidation ditch through a supernatant conveying pipeline, mixing with outflow of the oxidation ditch, and making the mixed solution enter the secondary precipitation basin. Due to the adoption of the process, high sludge concentration can be kept in the system, the pollutant removing rate can be remarkably increased, and the common problem of activated sludge bulking existing in the oxidation ditch can be effectively prevented and controlled.
Owner:SHANGHAI MUNICIPAL ENG DESIGN INST GRP +1
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