Background technology
Water pollution problems sharply worsens with industrialized propelled at high velocity, northern Haihe River, Huaihe River and Liaohe River blackout foul, almost become super blowdown ditch, and southern Taihu Lake, Chaohu and Dian Chi are owing to having received a large amount of organic pollutant, cause serious eutrophication, often lose use value because of alga eruption.And, water pollutions still in deterioration, from Zhi Liuxiang master stream, from city to rural area, from earth's surface to underground, spread development from land to ocean.
The administering method that the surface water such as lake, usual river adopt has peripheral doses technology, chemical remediation technology and bioremediation technology.Physical method comprises dredges bed mud, machinery except algae, aeration, diversion erosion and deposition etc., and this method is simple to operate, and cost is low, but often cures the symptoms, not the disease; Chemical redemption adds redox potential, pH in chemical agent and sorbent material change water body, adsorption precipitation Suspended Matter in Water matter and organic matter, utilize the chemical reaction of pollutent to be separated, the objectionable impurities reclaimed in sewage, or make it be converted into harmless material, although chemical process instant effect, but chemical agent need be added in a large number, cost intensive, easily cause secondary pollution simultaneously, and, the general sewage work that need introduce administers, and quantities is large, troublesome poeration; Biological restoration be utilize plant, animal, microorganism to carry out under certain conditions absorbing, degrade, the pollutent transformed in water body, high with the enrichment degree of this method to metal ion and difficult degradation toxic organic compound matter, biologic chain terminal meeting enriched in metals ion and toxic organic compound, and the life condition that biological growth needs is harsh, some water pollution is too serious, biological being difficult to grows, some adds biological function bacterium, but function yeast proliferative speed is slow, on average need more than 24h, and sewage difficulty is up to standard after process, also easily introduce external bacterial classification pollution problem.
Summary of the invention
The purpose of this utility model be to provide a kind of easy for installation do not need civil engineering can the floating on water mobile processing device of the contaminated water bodies of rivers and lakes of fast processing.
For solving the problems of the technologies described above, the technical scheme that the utility model provides is:
A kind of water bodies of rivers and lakes purification treatment equipment that may float on the water surface, comprise oxygenerator, ozonizer, ejector, catalyticreactor, plate-type heat exchanger, recycle pump, pure water tank and swash plate catalytic reactor, above-mentioned each equipment is connected by technical process by pipeline, integrated installation is in modular casing, and be placed in and float on the water surface and on moveable platform, platform surrounding arranges railing or breast board, railing breast board adopts the artistic design similar to surrounding landscape, forms floatability moveable water bodies of rivers and lakes purification treatment equipment; Also comprise filtering net and submerged pump, filtering net is placed under water, and the water inlet pipe of described submerged pump stretches in underwater filtration net;
Described oxygenerator, ozonizer, ejector, catalyticreactor, interchanger, recycle pump and submerged pump are equipped with import and outlet;
The outlet of described oxygenerator is connected by pipeline with the import of ozonizer; The outlet of described ozonizer is connected by pipeline with the first import of ejector, and the second import of ejector is connected by pipeline with the outlet of submerged pump; The import of described submerged pump passes into the sewage after net filtration after filtration, and the outlet of ejector is connected by pipeline with catalyticreactor;
Described catalyticreactor is connected by pipeline with the import of swash plate catalytic reactor; The outlet of described swash plate catalytic reactor is connected by pipeline with the first import of plate-type heat exchanger, the cooling room of ozonizer is connected by pipeline with the second import of described interchanger, recycle pump and pure water tank is also provided with between the cooling room and described interchanger of ozonizer, circulation pure water is driven to form recuperated cycle with recycle pump, heat ozonizer work produced passes to sewage by the pure water of circulation through interchanger, heat is taken away, saves a large amount of water coolants or because of the energy that expends of cooling ozonizer.
Described ejector is Venturi ejector, and the overcurrent material of described Venturi ejector is the material of resistance to ozone corrosion.The described material of resistance to ozone corrosion is stainless steel, tetrafluoroethylene, EDPM(terpolymer EP rubber) or fluorine-containing rubber.
Described casing is that steel construction or plastic construction are made.
Further, described catalyticreactor is a catalyticreactor, or by multiple catalyticreactors that pipeline is in series, adopts multiple catalyticreactors of series connection can extend the catalyzed reaction time, ensure treatment effect.
Further, described casing is one or more, is connected between multiple casing by pipeline or cable.
Further, described heat exchanger surface scribbles catalytic material, accelerates the oxidizing reaction of water and ozone.
Filtering net is set before submerged pump, the impurity in filtered water, prevents pump and line clogging.
The described outward appearance floating on the platform of the water surface adopts the design with the identical style of surrounding River Landscape scenic belt, forms the scape with scenic belt harmony.
Described catalyticreactor inner array tube-surface and the sheet surface of plate-type heat exchanger all scribble catalytic material, accelerate the catalytic oxidation of water and ozone, described catalytic material is one or more materials in inertia precious metal catalytic material gold (Au) silver (Ag) platinum (Pt) palladium (Pd) rhodium (Rh) iridium (Ir) osmium (Os) ruthenium (Ru).
The sheet surface of described plate-type heat exchanger has multiple concavo-convex, and enlarge active surface and heat interchanging area only need a small amount of plate just can be effective, effectively can save energy, reduces equipment volume.
Beneficial effect:
(1) oxygenerator, ozonizer, Venturi ejector, catalyticreactor, interchanger, recycle pump etc. are connected by technical process by pipeline by the water bodies of rivers and lakes purification treatment equipment that may float on the water surface of the present utility model, and integrated installation forms surface water treatment equipment in the casing that steel construction is made together with submerged pump.According to earth's surface water treatment capacity, equipment can be made one or more modular casing, connected by pipeline or cable between casing, aforementioned device is placed on floatable surface platform, switch on power and just can realize the quick improvement of surface water, this equipment can move at floating on water, do not need civil engineering, easy for installation, conveniently moving, simple to operate, Fast Installation can be realized come into operation fast, process position can be moved in use procedure, be applicable to the improvement of large regions river and lake water.
(2) this equipment is placed on floatable surface platform, switches on power and just can realize the quick improvement of surface water.This equipment can the larger molecular organics such as efficient degradation tensio-active agent, reduces the total phosphorous in water body and ammonia nitrogen, and algae, mushroom material fast, makes water body Non-toxic, innoxious, recovers biological self cleaning function.River after improvement can continuous flow expansion, promotes river dilution on the one hand and continues oxygenating, can also play plug-flow on the one hand and improve the effect of water quality.
(3) outward appearance of raft can adopt the design with the identical style of surrounding River Landscape scenic belt, forms the scape with scenic belt harmony, is conducive to landscaping.
Embodiment
Below in conjunction with specific embodiment, the utility model is described in further detail.
A kind of water bodies of rivers and lakes purification treatment equipment that may float on the water surface comprises oxygenerator 1, ozonizer 2, Venturi ejector 3, catalyticreactor 5, plate-type heat exchanger 7, recycle pump 9, pure water tank 8 and swash plate catalytic reactor 6, above-mentioned each equipment is connected by technical process by pipeline, integrated installation is in modular casing, and be placed in and float on the water surface and on moveable platform, platform surrounding arranges railing or breast board, railing breast board adopts the artistic design similar to surrounding landscape, forms floatability moveable water bodies of rivers and lakes purification treatment equipment; Also comprise filtering net and submerged pump 4, filtering net is placed under water, and the water inlet pipe of described submerged pump 4 stretches in underwater filtration net; Described oxygenerator 1, ozonizer 2, Venturi ejector 3, catalyticreactor 5, interchanger 7, recycle pump 9 and submerged pump 4 are equipped with import and outlet; The outlet of described oxygenerator 1 is connected by pipeline with the import of ozonizer 2; The outlet of described ozonizer 2 is connected by pipeline with the first import of Venturi ejector 3, and the second import of Venturi ejector 3 is connected by pipeline with the outlet of submerged pump 4; The import of described submerged pump 4 passes into the sewage after net filtration after filtration, and the outlet of Venturi ejector 3 is connected by pipeline with catalyticreactor 5; Described catalyticreactor 5 is connected by pipeline with the import of swash plate catalytic reactor 6; The outlet of described swash plate catalytic reactor 6 is connected by pipeline with the first import of plate-type heat exchanger 7, the cooling room of ozonizer 2 is connected by pipeline with the second import of described interchanger 7, recycle pump 9 and pure water tank 8 is also provided with between the cooling room and described interchanger 7 of ozonizer 2, circulation pure water is driven to form recuperated cycle with recycle pump 9, the heat produced that worked by ozonizer 2 passes to sewage by the pure water of circulation through interchanger 7, heat is taken away, saves a large amount of water coolants or because of the energy that expends of cooling ozonizer 2.Described ejector is Venturi jet 3 device, and the overcurrent material of described Venturi jet 3 device is the material of resistance to ozone corrosion.The described material of resistance to ozone corrosion is stainless steel, tetrafluoroethylene, EDPM(terpolymer EP rubber) or fluorine-containing rubber.Described casing is that steel construction or plastic construction are made.Described catalyticreactor 5 is a catalyticreactor 5, or by multiple catalyticreactors 5 that pipeline is in series, adopts multiple catalyticreactors 5 of series connection can extend the catalyzed reaction time, ensure treatment effect.Described casing is one or more, is connected between multiple casing by pipeline or cable.Described catalyticreactor 5 inner array tube-surface and the sheet surface of plate-type heat exchanger 7 all scribble catalytic material, accelerate the catalytic oxidation of water and ozone.Described catalytic material is inertia precious metal catalytic material.Described inertia precious metal is one or more materials in gold (Au) silver (Ag) platinum (Pt) palladium (Pd) rhodium (Rh) iridium (Ir) osmium (Os) ruthenium (Ru).The sheet surface of described plate-type heat exchanger 7 has multiple concavo-convex, and enlarge active surface and heat interchanging area only need a small amount of plate just can be effective, effectively can save energy, reduces equipment volume.
The above; it is only preferred embodiment of the present utility model; not any pro forma restriction is done to the utility model; any those skilled in the art; do not departing within the scope of technical solutions of the utility model; according to technical spirit of the present utility model, any simple amendment that above embodiment is done, equivalently replace and improve, within the protection domain all still belonging to technical solutions of the utility model.