대용량 하폐수 처리장치
The present invention refers to wastewater treatment device relates to search, with different deadly affected source is provided having a large wastewater treatment device capable of high throughput regardless even with varying seasonal environment are disclosed. Generally house, apartment, restaurant, the fertility of discharged from a sewage, sludge, oil screen recorded in the sewage tank, plays critical role, oxidizer used, denitrification trillion etc., sewage and wastewater treatment device comprising a sedimentation tank sludge then sequentially river after being treated with factor while oil is discharged to the substrate. The bottom screen and screening the impurities contained in wastewater, sewage and waste water in which transfer plays critical role uniform amount, of nitrogen compounds and processing liquid oxidizer used drying and crushing processes and sewage, sludge precipitated and oxidizer used and denitrification tank is being treated in a stand-alone residual polyphosphoric acid number 2000. Related prior art call load is registered utility model 20 - 0290126 influx possibility of production over wastewater treatment system is operated intermittently according to the means by which called the disclosure. The temperature detector includes a wastewater treatment device, when the switching frequency of contaminant concentration is enhanced or sewage, or seasonal temperature even with varying according to the degree of processed in accordance with the indefinite, when contaminants alkali water and river water being supplied is made, this causes been from contaminating the ecosystem. In addition contains atmospheric air environment for altering the sewage processing degree value according to a, large overall processing elements used to speed dial setup. The present invention refers to said point is created in order to solve such as door number, house, apartment, restaurant, with different source increases caused a wastewater treatment device having a large number can be deadly affected high throughput intended. It is another object of the present invention, wastewater of contaminant concentration is constant or non-constant temperature even with varying altitude capable of processing a large wastewater treatment device according to seasonal number are disclosed. Such as in order to achieve said purposes, the present invention according to wastewater treatment device is large, the impurities contained in wastewater entering screen for screening of a tank (10); said screen tank (10) for transferring an amount next place via sewage consisting plays critical role (20); said plays critical role (20) transported from the denitrification deadly affected for the denitrification tank (30); said denitrification tank (30) number 1 of contaminants transported from the sewage which nitric acid oxidizer used (40); said oxidizer used (40) organic nitrogen for treating sewage and waste water transported from the expoxy-nitrogen, nitrate nitrogen or nitrite nitrogen first oxidation reaction trillion microorganism number 2 (50); this makes the remaining wastewater after which it comes sinkage trillion surplus excess sludge due to settling said number 2 nitric acid (70); said microorganism reaction trillion (50) remaining organics and nitrogen component number processed sewage and waste water transported from the stand-alone made number highly vessel (80); said highly vessel (80) disinfecting the water supplied to the sterilization process transported from the outer discharge trillion (90); and said plays critical role (20), oxidizer used (40), highly vessel (80) and disinfecting discharge trillion (90) a continuous air flow continuously bubbled (110); including a characterized substrate. In the present invention, said microorganism reaction trillion (50) provided with an air brush a discontinuous, said microorganism reaction trillion (50) is integrally formed with the bottom of the plurality of air holes (121a) formed (121) on, said microorganism reaction trillion (50) processed in wastewater containing microorganisms generating sensor measure a concentration corresponding microorganism concentration signal (122) on, microorganism concentration signal transmission part for transmitting the (121) discontinuous varying a supply of air supplied to the air pump (123) discontinuous consisting (120) further comprises. In the present invention, said oxidizer used (40) microorganism on reaction trillion (50) to define a flow path between said via and increasing temperature of the sewage wastewater is provided for, flat rectangular passage (131) having a pipe body (132) on, said rectangular passage (131) installed on the bottom of heating (133) consisting of a heater pipe (130) further comprises. In the present invention, said screen bath (10) includes, arranged at an upper recovery tank (11) on, said inlet pipe (10a) included in said recovery tank to said floating laundry wastewater inlet (11) and transporting the floating laundry transfer unit (12) on, said inlet pipe (10a) included in said recovery tank a precipitated laundry wastewater inlet (11) and transporting the transfer unit (13) on, sewage and waste water is temporarily stored number for reparing over floating laundry and temporary delaying portion (14) having a predetermined wavelength. In the present invention, said transfer unit (13) is, said screen tank (10) is integrally formed with the bottom side of said focusing discharging outlet (13a ') having a hopper (13a) on, said hopper (13a) of the lower side of screen tank (10) is integrally formed with said hopper to outlet (13a') precipitated impurities is collected through a collecting tank (13b) on, said collecting tank (13b) collected recovery tank (11) to and from the transfer pump (13c) on, said collecting tank (13b) is integrally formed with said bottom weight weight measurement stage for generating a signal for measuring the weight correspondingly (13d) and, said weight measurement stage (13d) weight is set when at least weight measured at said transfer pump (13c) pump operating an operating portion (13e) without using a tool. In the present invention, said transfer unit (13) is, said hopper outlet (13a ') oil is hopper outlet (13a') hopper valve selectively opens (13f) further comprises. In the present invention, said transfer unit (13) is, said hopper outlet (13a ') may be focused to said hopper (13a) whether applying vibration in vibration (13g) further comprises. In the present invention, said microorganism reaction trillion (50) includes said oxidizer used (40) of sewage and via an organic nitrogen and ammonia nitrogen, nitrate nitrogen or nitrite nitrogen for microorganisms derived from at least one first oxidation number 2 1 part (51) further includes; said microorganism derived from part (51) is, positioned on the front side and front pipe (51a) on, said front pipe (51a) to the back of the backside manner having inner diameter rear pipe (51b) on, said front pipe (51a) installed on the water pump (51c) on, said rear pipe (51b) of the inner peripheral surface radiation wing (51d ') as are secured by, front pipe (51a) hot and narrower diameter applying pipeline (51d) on, said sub pipe (51d) installed at the backside of a rear pipe (51b) exposed to the outside of the pipe (51e) and, said pipe (51e) contained in wastewater of organic material to decompose to microorganisms number provided for microbial carrier (51f) of 100. In the present invention, said microorganism derived from part (51) is, said sub pipe (51d) selectively water outlet (51g) further comprises. In the present invention, said highly vessel (80) is, said highly vessel (80) to bottom edge of (111) to the first edge with (81a) on, said edge (81a) of adhesive mixed with number 1 as supported sewage industry number 1 filter (81b ') with number 1 filter box (81b) on, said number 1 filter box (81b) is laminated on number 1 filter box (81b) expoxy adhesive via sewage industry a difference number 2 number 2 filter (81c') with number 2 filter box (81c) on, said surplus it comes sinkage trillion (70) are connected to said number 1, 2 filter box (81b) (81c) through the frame (81a) extending the inner space of sewage and waste water transfer pipe (81d) comprises. According to the present invention according to mass wastewater treatment device, denitrification tank is sequentially connected), oxidizer used, reaction trillion microorganisms, it comes sinkage trillion surplus, highly by treating, with different microorganisms from wastewater having source, nitrogen and phosphorus can be effectively number as well as a stand-alone permits high throughput. In addition perform the discontinuous and microorganism cycle processing unit installed microorganism, sewage and waste water to the concentration of the microorganisms through the carrier transmitted to make the amount of sewage can be treated and, in addition microorganism oxygen-saturated concentration of microorganism activity can be uniformly in an open state. Fluidic and a heater, so that a lens barrel inner heat insulating and FRP layer by employing microorganism, the microorganism as well as discharged exhaust delivered from an underground cold insulation reaction trillion (50) entering the bath temperature can be industrial wastewater by navigating. Figure 1 shows a surface configuration of the present invention according to also account for large wastewater treatment device, Figure 2 shows a screen tank by the ALIGN to explain agent of of Figure 1, Figure 3 shows a portion of the set up of Figure 2 also for the ALIGN , Figure 4 shows a finger print data by adding the microorganism to explain agent of of Figure 1, Figure 5 shows a microorganism derived from part to ALIGN for the set up of Figure 4 also, Figure 6 shows a highly by treating the finger print data to explain agent of of Figure 1, Figure 7 shows a discontinuous and heater pipe installed microorganism to account for agent of of Figure 1 surface, Figure 8 shows a pipe heater finger print data shown in the perspective view of Figure 7. Hereinafter, the present invention according to a reference mass wastewater treatment device attached drawing detailed as follows. In hereinafter, referred to as "upper" or "on" contact disclosed is a non-contact way may be a be formed on as well as on the can. Number 1, number 2 describes various components such as term can be used but, components are defined by terms don't substrate. Terms are used only one component object distinguished from other components. It is apparent that a single representation of the differently in order not providing language translators, comprising plurality of representation. In addition any components that "comprising" when any portion, particularly the opposite substrate number but without other components further can include other components which means that the other. In addition, a specification ".. Part "," module " term processing operation of at least one mobile communication unit by big. Figure 1 shows a configuration of the present invention according to mass wastewater treatment device and also to explain the drawing, Figure 2 shows a screen installed and set up to ALIGN for drawing, Figure 3 of Figure 2 for the portion of the ALIGN set up of Figure 1 are disclosed. As shown, large wastewater treatment device is herein of the invention, the impurities contained in wastewater entering, for example impurities suspended in the lower wastewater or sewage for screening of a screen produced by the laundry bath (10) on; screen tank (10) for transferring an amount next place via sewage consisting plays critical role (20) on; plays critical role (20) transported from the denitrification deadly affected for the denitrification tank (30) on; denitrification tank (30) number 1 of contaminants transported from the sewage which nitric acid oxidizer used (40) on; oxidizer used (40) organic nitrogen for treating sewage and waste water transported from the expoxy-nitrogen, nitrate nitrogen or nitrite nitrogen first oxidation reaction trillion microorganism number 2 (50) on; microorganism reaction trillion (50) a portion of the sewage in the denitrification tank number 2 nitric acid (40) and returning section (60) on; this makes the remaining wastewater after which it comes sinkage trillion surplus excess sludge due to settling said number 2 nitric acid (70) on; microorganism reaction trillion (50) remaining organics and nitrogen component number processed sewage and waste water transported from the stand-alone made number highly vessel (80) on; highly vessel (80) disinfecting the water supplied to the sterilization process transported from the outer discharge trillion (90) on; (10) and the residual it comes sinkage trillion (80) sludge generated in laundry and temporarily stores the laundry (100) on; plays critical role (20), oxidizer used (40), highly vessel (80), disinfecting discharge trillion (90) and laundry (100) for continuous air flow continuously bubbled (110) on; microorganism reaction trillion (50) with an air discontinuous aeration a discontinuous (120) on; oxidizer used (40) microorganism on reaction trillion (50) to define a flow path between the wastewater is conveyed via as denitrification apparatus for increasing temperature heater pipe (130); characterized by including a a. Wherein, continuous (110) is, plays critical role (20), oxidizer used (40), disinfecting discharge trillion (90) and laundry (100) installed in the bottom of the (111) on, (111) and joined with the line 24 supply the air all time continuous air pump (112) having a predetermined wavelength. Screen bath (10) contained the incoming wastewater is floating laundry or for screening of precipitated impurities are disclosed. The screens tank (10) is, as shown in fig. 2, arranged at an upper recovery tank (11) on, inlet pipe (10a) floating laundry wastewater inlet included in recovering tank (11) transferring the substrate into the floating laundry transfer unit (12) on, inlet pipe (10a) precipitated laundry wastewater inlet included in recovering tank (11) for transferring transfer unit (13) on, sewage and waste water is temporarily stored number for reparing over floating laundry and temporary delaying portion (14) having a predetermined wavelength. Floating laundry transfer unit (12) is, as shown in fig. 2, an inlet conduit (10a) of number 1 is inserted into the roller (12a) on, recovery tank (11) mounted on the upper side of the number 2 roller (12b) on, number 1, 2 roller (12a) (12b) formed as common impedance element caterpillar conveyed to non ear (12c) on, number 2 roller (12b) to be rotationally driven a drive motor (12d) having a predetermined wavelength. Due to this, an inlet conduit (10a) the wastewater inlet ear (12c) through screen pores of tank (10) and clean up, during this process wastewater is included among the floating laundry ear (12c) goes to after recovery tank (11) is transferred to an collected substrate. transfer unit (13) is, as shown in fig. 3, screen tank (10) is integrally formed with the bottom side of focusing discharging outlet (13a ') having a hopper (13a) on, hopper (13a) of the lower side of screen tank (10) is integrally formed with the hopper outlet (13a') precipitated impurities is collected through a collecting tank (13b) on, a collecting tank (13b) collected recovery tank (11) to and from the transfer pump (13c) on, a collecting tank (13b) is integrally formed with the bottom of the weight signal weight measurement stage for measuring the weight correspondingly km (13d) and, weight measurement stage (13d) weight is set when at least weight measured at said transfer pump (13c) pump operating an operating portion (13e) on, hopper outlet (13a ') oil is hopper outlet (13a') hopper valve selectively opens (13f) without using a tool. The hopper (13a) is rear view of, hopper outlet (13a ') may be focused to hopper (13a) whether applying vibration in vibration (13g) can be provided. Hopper (13a) is contained sewage collecting tank (13b) may be focused to worker. Transfer pump (13c) includes a weight measurement stage (13d) as measured by a transmission part for transmitting weight operate, a collecting tank (13b) on the recovery tank (11) through a hose (not shown) connecting transfer reaction chamber. Transfer pump (13c) is a collecting tank (13b) can be collected and lots of failure if, for example, weight measurement stage (13d) is measured in weight of 30 kg or more when transfer pump (13c) in order to actuate the pump operating portion (13e) can be setting. In this case, a collecting tank (13b) to 30 kg or more the collected weight measurement stage (13d) weight signal is output from the pump operations by part (13e) transmits, pump operating portion (13e) delivery (13c) operate the recovery tank (11) and to convey a, the collecting tank (13b) may be collected are emptied to other are disclosed. Hopper valve (13f) delivery pump (13c) is when operated as a hopper outlet (13a ') to close off a, the recovery tank (11) during wastewater is fed a collecting tank (13b) can be introduced into preventing are disclosed. Vibration in the area (13g) hopper (13a) by applying periodic aperiodically over a vibration, hopper outlet (13a ') focused and performed hopper (13a) stacked on the first surface of servicing the. Due to this. ear (12c) contained sewage through, for example such as fine head stone or engage hopper (13a) a collecting tank is suitable (13b) and collected into a, the collected transfer pump (13c) carried by a recovering tank (11) recovered in the UGT. Temporary delaying portion (14) includes a screen bath (10) within recovery tank (11) positioned underside, floating laundry wastewater for reparing over drain flow is temporarily stored before and number relative to the steamed while causes. Plays critical role (20) includes a screen bath (10) where the next sewage via a denitrification tank (30) returning to uniform transfer amount. Wherein plays critical role (20) installed (111) during the middle of sewage by aeration air sewage and waste water is simultaneously and for supplying oxygen to a microorganism itself, the microorganisms of the rotting servicing the organic wastewater to check. This plays critical role (20) of the wastewater feed pump (35) where the next by a denitrification tank (30) maintained a uniform conveying substrate. Denitrification tank (30) is plays critical role (20) is transported from the agitator for agitating for denitrification of sewage sludge from wastewater (45) having a predetermined wavelength. This denitrification tank (30) plays critical role in (20) or microorganism reaction trillion (50) transported from nitrate nitrogen or nitrite nitrogen gas contained in the wastewater are discharged into the atmosphere as substrates by replacement of the sewage to be established and other. The denitrification oxygen-free conditions by means of a carbon chain is active in the denitrification bacteria and excellent electron donor, packed in the resulting number encoded consumed denitrification process to recover the wetting ability. In addition outputted from the sewage itself denitrification composed using a carbon source, such as methanol processed ion when the external carbon source is equal to or higher, Oxidizer used (40) includes, denitrification tank (30) a first oxidation number 1 as a denitrification from contaminants in wastewater, sewage and waste water into the inside air for aeration (111) a semiconductor device is provided. (111) of air supplied through the wastewater ammonia oxidation bacteria or bacteria proliferated oxidation the pH, the pH of wastewater ammonia oxidation bacteria or organic nitrogen or nitrogen or nitric oxide bacteria to about pH animonia nitroge nitrate-nitrogen. Figure 4 shows a set up for drawing and adding microorganisms to ALIGN, Figure 5 shows a part of Figure 4 also derived from the microorganism to ALIGN for set up of Figure 1 are disclosed. As shown, reaction trillion microorganism (50) oxidizer used is (40) of sewage and via an organic nitrogen and ammonia nitrogen, nitrate nitrogen or nitrite nitrogen for microorganisms derived from at least one first oxidation number 2 1 part (51) is installed, microorganism derived from part (51) is reaction trillion microorganisms (50) provided on the bottom side of microorganism reaction trillion (50) circulating wastewater within microorganism can be mixed uniformly into sewage to other. Such microorganisms derived from part (51) is, as shown in fig. 5, located on the front side and front pipe (51a) on, front pipe (51a) to the back of the backside manner having inner diameter rear pipe (51b) on, front pipe (51a) installed on the water pump (51c) on, rear pipe (51b) of the inner peripheral surface radiation wing (51d ') as are secured by, front pipe (51a) hot and narrower diameter applying pipeline (51d) on, sub pipe (51d) installed at the backside of a rear pipe (51b) exposed to the outside of the pipe (51e) and, the pipe (51e) contained in wastewater of organic material to decompose to microorganisms number provided for microbial carrier (51f) on, sub pipe (51d) selectively water outlet (51g) without using a tool. Due to this, water pump (51c) operation of rear pipe (51b) wastewater entering the front pipe (51a) discharged after it passes through a fast acceleration, industrial wastewater reaction trillion (50) within the receiving sewage microorganism carrier (51f) microorganism from which ball number microorganism reaction trillion (50) causes uniform within. Wherein, microorganism reaction trillion (50) contamination of sewage entering the higher concentration valve (51g) open to each other. In this case rear pipe (51b) inside the pipe by the pressure difference (51d) in negative pressure generated, by such negative pressure pipe (51e) wastewater outside seat (51f) number after a steel that has passed the sub pipe (51d) rearwardly through pipe (51b) discharged into, then front pipe (51a) following expulsion through microbial reaction trillion (50) are circulating. The microbial carrier (51f) by a large amount of wastewater is passed microorganism reaction trillion (50) inside the distribution of large quantities of microorganisms to be coated. The wastewater contamination of higher concentration can save when effective number 2 via the network. On the contrary, microorganism reaction trillion (50) is transmitted with a predetermined denitrification contaminant concentration, valve (51g) closes the other. The subcarriers are pipeline (51d) exit of the closed wastewater is microbial carrier (51f) does not pass through and , the microbial carrier layer formed on an corresponding to servicing the microorganisms. Microbial carrier (51f) is, numerous small internal non organic materials filled with polyester opening formed microorganisms have the form. On the other hand, reaction trillion microorganism (50) the inner circumference so that a lens barrel is insulating (52) and, insulating layer (52) closed the surface of portions of the FRP layer (53) formed therein. The FRP layer (53) are covered with an insulating (52) by, and discharged at the exhaust delivered from an underground cold insulation, an operator microorganism reaction trillion (50) even if internal excluding one another insulating layer (52) connected to the front plate can be prevent. Section (60) includes a microorganism reaction trillion (50) a portion of the sewage in the denitrification tank number 2 nitric acid (30) provided and returning, microorganism reaction trillion (50) denitrification tank (30) connecting transfer tube (61) and, transfer tube (61) which is mounted on the pump (62) consists of to. This section (60) through the denitrification tank (30) is carried on a number 2 nitrate nitrogen N2 gas of nitrogen or nitric acid in livestock wastewater pH encoded denitrification are reduced. Surplus it comes sinkage trillion (70) where the residual nitric acid remaining after the selected number 2 is sewage sludge as due to settling, surplus sludge hopper has a narrower downwardly so as to be capable effectively precipitated form. Figure 6 shows a highly by treating the finger print data to explain agent of of Figure 1 are disclosed. As shown, highly vessel (80) includes a microorganism reaction trillion (50) remaining organics and nitrogen processed sewage and waste water transported from the number of activated carbon unit for making a stand-alone component number (81) a semiconductor device is provided. This high processing unit (81) is, highly vessel (80) to bottom edge of (111) to the first edge with (81a) on, edge (81a) of adhesive mixed with number 1 as supported sewage industry number 1 filter (81b ') with number 1 filter box (81b) on, number 1 filter box (81b) is laminated on number 1 filter box (81b) expoxy adhesive via sewage industry a difference number 2 number 2 filter (81c') with number 2 filter box (81c) on, surplus it comes sinkage trillion (70) are connected to a number 1, 2 filter box (81b) (81c) through the frame (81a) extending the inner space of sewage and waste water transfer pipe (81d) comprises. The higher concentration be treated wastewater nitrogen or phosphorous, other filter box number 2 filter box (81c) of top side that can be laminated to disclosed. Edge (81a) inner (111) is connected with another, number 1, 2 filter box (81b) (81c) to which the closing by, said wastewater feed conduit (81d) outlet of the number 1, 2 filter (81b) through (81c) with each other. Number 1 filter box (81b) porous mineral materials provided including, the porous minerals elvan, pozzolan (pozzolan), number it rises, light, loess, and combinations thereof selected from the group consisting used for substrate. This number 1 filter (81b ') is finely prolong while nitrogen, used such as components to each other. Number 2 filter box (81c) entering is that a microorganism including food, food absorbent large fasteners, in which the high pressure liquid coolant such as water-soluble extract content using processes of edema can be number. The food 3 to 7 mm, or 5 to 7 mm in size cup powder encapsulated in a stand-alone number then the signal processing, a vacuum impulse drying furnace is placed sap component number range of pigment can be a stand-alone. This number 2 filter box (81c) microorganism to supported, ammonia can be oxidized nitrosomonas eutropha (nitrosomonas), knit with pak (nitrobacter) aerobic microorganisms such as either independent nutritional (aerobic autotrophic micro-a organism), nitric acid ions capable of reducing flow rate pylori (aerobacter), bacillus (bacillus), or microphone LOCOS cathode (micrococcus) of Heterotrophic microorganism (heterotrophic micro-a oranism) can be used. Disinfecting discharge trillion (90) is highly vessel (80) transported from the water supplied to the outer sterilization process such as a fabric, is supplying disinfecting number therein disinfecting number supply (91) a semiconductor device is provided. Laundry (100) includes a screen tank (10) and the residual it comes sinkage trillion (70) sludge generated in laundry and temporary store. The laundry (100) for aeration air bottoms of the (111) is installed, air brush for the temporary storage and control quantity servicing the staling of sludge. Figure 7 shows a drawing to explain the discontinuous and heater pipe installed microorganism and, Figure 8 shows a pipe heater of Figure 7 of Figure 1 also shown to ALIGN sensors mounted thereon are disclosed Discontinuous (120) is, microorganism reaction trillion (50) is integrally formed with the bottom of a plurality of air holes are arranged in a matrix (121a) formed (121) on, microorganism reaction trillion (50) processed in wastewater containing microorganisms generating sensor measure a concentration corresponding microorganism concentration signal (122) on, microorganism concentration signal transmission part for transmitting the (121) discontinuous varying a supply of air supplied to the air pump (123) having a predetermined wavelength. Heater pipe (130) has a flat rectangular passage (131) having a pipe body (132) on, rectangular passage (131) installed on the bottom of heating (133) to consists of. The according to the present invention, sequentially connected denitrification tank (30), oxidizer used (40), microorganism reaction trillion (50), surplus it comes sinkage trillion (70), highly vessel (80) by a, house, apartment, restaurant, caused the fertility of deadly affected over and having processed with different source 2 difference, the method for removing nitrogen from wastewater effectively number can be a stand-alone and permits high throughput. In addition reaction trillion microorganism (50) which is mounted on the discontinuous (120) and microorganism derived from part (51) by employing, sewage and waste water to the concentration of the microbial carrier (51f) through the variable amount of sewage can be treated and there is efficient, in addition reaction trillion microorganism (50) makes a uniform saturation of oxygen concentration can be uniformly activity of microorganism. And a heater pipe (130) on, microorganism reaction trillion (50) so as to cover the inner peripheral surfaces of the heat insulating (52) and FRP layer (53) by employing, as well as the discharged exhaust delivered from an underground cold insulation microorganism reaction trillion (50) entering the bath temperature can be industrial wastewater by navigating. The present invention refers to drawing is but one in the embodiment described with reference to an exemplary shown in a and a are in, art therefrom if various deformation and equally in the embodiment is enabling other person with skill in the art will understand. 10.. Screen tank 10a.. Inlet pipe 11.. Recovery tank 12.. Floating laundry transfer unit 12A.. Number 1 roller 12b.. Number 2 roller 12C.. Ear 12d .. Drive motor 13.. transfer unit 13a.. Hopper 13A '.. Hopper outlet 13b.. A collecting tank 13C.. Transfer pump 13d.. Weight measurement stage 13E.. Pump working part 13f.. Hopper valve 13G.. Vibration in the area 14.. Temporary delaying portion 20.. 30 Plays critical role.. Denitrification tank 40.. Oxidizer used 50.. Reaction trillion microorganisms 51.. Microorganism cycle processing unit 51a.. Front pipe 51B.. Rear conduit 51c.. Water pump 51D.. Sub conduit 51d '.. Radiation wing 51E.. The pipe 51f.. Microbial carrier 51G.. Valve 60.. Conveying parts 61.. Transfer tube 62.. Pump 70.. It comes sinkage trillion surplus 80.. Highly vessel 81.. Disposal plant unit 81a.. Edge 81B.. Number 1 filter box 81b '.. Number 1 filter 81C.. Number 2 filter box 81c '.. Number 2 filter 90.. Disinfecting discharge trillion 100.. Laundry 110.. Continuous 111.. 112.. Air pump 120.. Discontinuous 121.. 122 .. Sensor 123.. Air pump 130.. Heater pipe The present invention relates to a large-capacity wastewater treatment apparatus capable of treating a large quantity of wastewater. The large-capacity wastewater treatment apparatus comprises: a screen tank (10) to filter out impurities contained in inflow wastewater; a flow adjustment tank (20) to transport wastewater passing through the screen tank (10) to a next place in a uniform amount; a denitrification tank (30) to denitrify wastewater transported from the flow adjustment tank (20); a nitrification tank (40) to firstly nitrify contaminants in wastewater transported from the denitrification tank (30); a microorganism reaction tank (50) to secondly nitrify organic nitrogen and ammonia nitrogen remaining in wastewater transported from the nitrification tank (40) into nitrite nitrogen or nitrate nitrogen; a surplus sludge settling tank (70) in which surplus sludge remaining in wastewater after the second nitrification process settles; an advanced treatment tank (80) to remove organic matters and nitrogen components remaining in wastewater transported from the microorganism reaction tank (50) to make treatment water; a sterilization discharge tank (90) to sterilize the treatment water transported from the advanced treatment tank (80) to discharge the sterilized treatment water to the outside; and a continuous aeration unit (110) to continuously supply air to the flow adjustment tank (20), the nitrification tank (40), the advanced treatment tank (80), and the sterilization discharge tank (90).<br>COPYRIGHT KIPO 2019<br> The impurities contained in wastewater entering screen for screening of a tank (10); said screen tank (10) for transferring an amount next place via sewage consisting plays critical role (20); said plays critical role (20) transported from the denitrification deadly affected for the denitrification tank (30); said denitrification tank (30) number 1 of contaminants transported from the sewage which nitric acid oxidizer used (40); said oxidizer used (40) organic nitrogen for treating sewage and waste water transported from the expoxy-nitrogen, nitrate nitrogen or nitrite nitrogen first oxidation reaction trillion microorganism number 2 (50); this makes the remaining wastewater after which it comes sinkage trillion surplus excess sludge due to settling said number 2 nitric acid (70); said surplus it comes sinkage trillion (70) remaining organics and nitrogen component number processed sewage and waste water transported from the stand-alone made number highly vessel (80); said highly vessel (80) disinfecting the water supplied to the sterilization process transported from the outer discharge trillion (90); and said plays critical role (20), oxidizer used (40), highly vessel (80) and disinfecting discharge trillion (90) a continuous air flow continuously bubbled (110); and, said microorganism reaction trillion (50) includes said oxidizer used (40) nitrogen via an organic nitrogen for treating sewage and waste water, nitrate nitrogen or nitrogen for at least one first oxidation number 2 1 pH unit derived from microorganisms (51) wherein; said microorganism derived from part (51) is, positioned on the front side and front pipe (51a) on, said front pipe (51a) to the back of the backside manner having inner diameter rear pipe (51b) on, said front pipe (51a) installed on the water pump (51c) on, said rear pipe (51b) of the inner peripheral surface radiation wing (51d ') as are secured by, front pipe (51a) side may be narrower diameter applying pipeline (51d) on, said sub pipe (51d) installed at the backside of a rear pipe (51b) exposed to the outside of the pipe (51e) and, said pipe (51e) contained in wastewater of organic material to decompose to microorganisms number provided for microbial carrier (51f) characterized in including a large wastewater treatment device. According to Claim 1, said microorganism reaction trillion (50) provided with an air brush a discontinuous, said microorganism reaction trillion (50) is integrally formed with the bottom of the plurality of air holes (121a) formed (121) on, said microorganism reaction trillion (50) processed in wastewater containing microorganisms generating sensor measure a concentration corresponding microorganism concentration signal (122) on, microorganism concentration signal transmission part for transmitting the (121) discontinuous varying a supply of air supplied to the air pump (123) discontinuous consisting (120) characterized in further including large wastewater treatment device. According to Claim 1, said oxidizer used (40) microorganism on reaction trillion (50) to define a flow path between said via and increasing temperature of the sewage wastewater is provided for, flat rectangular passage (131) having a pipe body (132) on, said rectangular passage (131) installed on the bottom of heating (133) consisting of a heater pipe (130) characterized in further including large wastewater treatment device. According to Claim 1, said screen bath (10) includes, arranged at an upper recovery tank (11) on, inlet pipe (10a) included in said recovery tank to said floating laundry wastewater inlet (11) and transporting the floating laundry transfer unit (12) on, said inlet pipe (10a) included in said recovery tank a precipitated laundry wastewater inlet (11) and transporting the transfer unit (13) on, sewage and waste water is temporarily stored number for reparing over floating laundry and temporary delaying portion (14) including a large wastewater treatment device characterized. According to Claim 4, said transfer unit (13) is, said screen tank (10) is integrally formed with the bottom side of said focusing discharging outlet (13a ') having a hopper (13a) on, said hopper (13a) of the lower side of screen tank (10) is integrally formed with said hopper to outlet (13a') precipitated impurities is collected through a collecting tank (13b) on, said collecting tank (13b) collected recovery tank (11) to and from the transfer pump (13c) on, said collecting tank (13b) is integrally formed with said bottom weight weight measurement stage for generating a signal for measuring the weight correspondingly (13d) and, said weight measurement stage (13d) weight is set when at least weight measured at said transfer pump (13c) pump operating an operating portion (13e) characterized in including a large wastewater treatment device. According to Claim 5, said transfer unit (13) is, said hopper outlet (13a ') oil is hopper outlet (13a') hopper valve selectively opens (13f) characterized in further including large wastewater treatment device. According to Claim 6, said transfer unit (13) is, said hopper outlet (13a ') may be focused to said hopper (13a) whether applying vibration in vibration (13g) characterized in further including large wastewater treatment device. Back number According to Claim 1, said microorganism derived from part (51) is, said sub pipe (51d) selectively water outlet (51g) characterized in further including large wastewater treatment device. According to Claim 1, said highly vessel (80) is, said highly vessel (80) to bottom edge of (111) to the first edge with (81a) on, said edge (81a) of adhesive mixed with number 1 as supported sewage industry number 1 filter (81b ') with number 1 filter box (81b) on, said number 1 filter box (81b) is laminated on number 1 filter box (81b) expoxy adhesive via sewage industry a difference number 2 number 2 filter (81c') with number 2 filter box (81c) on, said surplus it comes sinkage trillion (70) are connected to said number 1, 2 filter box (81b) (81c) through the frame (81a) extending the inner space of sewage and waste water transfer pipe (81d) characterized in including a large wastewater treatment device.
