정수 슬러지 처리장치

28-03-2017 дата публикации
Номер:
KR0101720048B1
Контакты:
Номер заявки: 00-14-102083511
Дата заявки: 04-07-2014

[1]

The invention relates to a potable water treatment process for sludge generated during sludge sludge processing apparatus for processing a detergent are disclosed.

[2]

In particular it is a pulverized product producing drinking water during process occurs. The integer unit processes (aggregation, precipitation, filtration) sludge in precipitation of the flocs, generations spinal cord found in consists of residue or the like. High density sludge sewage and organic sludge sludge generated in red as compared to higher mineral content. Also, very low organic matter content and reduce water purification sludge and sludge volume rather than studies first of all at the time of is coming in now.

[3]

For red is essentially concentrated sludge generated correlation between volume and reduce (concentration) process, improved (conditioning) and dehydration (dewatering) process substrate. In residual main treatment sludge, but somewhat different red operation environment to experiences, commonly precipitation→of sewage→sludge tanks (1 difference pus building)→pus building (2 pus building)→→→disposal such as a storage tank dehydration followed by a substrate.

[4]

The most reuse of sludge generated from time cycle which does not initially have been embedded soil majority, then a portion of calcium has been discarded, certifying direct sale lip forbidden terms is set 2000 permeation rate is rapidly increased to the latest marine withdrawals cover is fixed marine market rely on the disclosed. Some of for recycling sludge compost, landscape architecture and a method used for recycling the waste or like space larger than the earthworm extremely rate data in a database are disclosed.

[5]

Waste sludge by quality control method while also limiting vent hole marine to obtain an and, minimize the sludge in a sewage treatment process and development expansion for recycling sludge etc. can be ranked.

[6]

Soil is for recycling sludge, solid fuel, construction materials, production, but as to the resource recovery, such sludge and sludge is an effective pre-processing essentially very low client requesting still Haven for recycling sludge rate are disclosed.

[7]

For example, 10 - 0802163 registered Patent Publication discloses a first call (user it will be a notification: 2008. 02. 11) water purification sludge in using and adsorbing and a production method thereof wherein, 10 - 0663235 registered Patent Publication discloses a first call (user it will be a notification: 2007. 01. 02) and the materials construction to water purification sludge in compositions and a method for manufacturing a gpon.

[8]

The variously sludge recycling organic inorganic anodizing order biochemical stabilizing, removing pathogens hygienic safety shoes, preventing the remaining sludge is eliminated will be required.

[9]

[Prior art document]

[10]

10 - 2014 - 0021353 public Patent Publication discloses a first call (public date: 2014. 02. 20)

[11]

10 - 0802163 registered Patent Publication discloses a first call (user it will be a notification: 2008. 02. 11)

[12]

10 - 0663235 registered Patent Publication discloses a first call (user it will be a notification: 2007. 01. 02)

[13]

The invention relates to such known device is that, particularly for potable water treatment process for sludge generated during sludge sludge processing device for processing a detergent broadcast receiver.

[14]

To achieve this object according to the present invention for the equipment for treating sludge, sludge ozone into contact with the ozone treatment tub; ozone treated sludge concentrated pus building and precipitating; the pus building of sludge in the three group dehydration apparatus; wherein, the triangular, moving direction of the moving part is installed for sludge drying chamber and to maintain its high temperature atmosphere; high temperature environment can be put on the horizontal transfer section cast into the sludge discharge extruder; without using a tool.

[15]

In preferably according to the invention, the bottom surface or the ozone, ultraviolet generating ultraviolet lamps further comprises.

[16]

Preferably in the present invention, the drying chamber, gas combustion type heat source connected with a combustion chamber, a horizontal transfer section for dry sludge room partitioned by the partition wall is disposed got dry sludge characterized.

[17]

In more preferably according to the invention, combustion gas generated in the combustion chambers so that heated air supplied to the drying air exchanging heat between the heat exchange section 1; further comprises.

[18]

In more preferably according to the invention, the condensing of the steam connected to the closing member in which there is a condenser; the condensed water discharged in a condenser air exchanging heat between heated so that final dry air discharged sludge fed 2 further comprises first heat exchange section.

[19]

In more preferably according to the invention, the condensation heat exchange heat exchange section 2 from being transferred to the process bath made integer integer number is not characterized.

[20]

In more preferably according to the invention, the generated in a condenser to separate moisture air discharging air from; the cyclone separator discharge air connected tn the blower further comprises supplied air.

[21]

In preferably according to the invention, the an extruder, sludge is supplied the supply part may be provided on the combining hollow; the rotation in the body portion and an auxiliary, heat internal heat generation member is provided a screw; the screw tip 13a formed body extending integrally molded stone tile; drive motor for rotationally driving the screw; without using a tool.

[22]

According to the invention the equipment for treating sludge, wherein the water purification sludge generated in potable water treatment process of sterilizing and odor, low organic content building function rate to water purification sludge can be equal to or less than the lower part.

[23]

Figure 1 shows a equipment for treating sludge of the overall arrangement according to the invention, Figure 2 shows a in sludge treatment apparatus according to the invention, in a preferred embodiment of the dewatering device, Figure 3 shows a in sludge treatment apparatus according to the invention, the dehydrated in another embodiment of the automation device.

[24]

Embodiments of the present invention that are presented in a specific structure functional disclosure only the concept of the invention in accordance with the present are described for the purpose of obtaining that example, embodiments according to the concept of the invention can be in various forms. Also provided in described embodiments not limited and interpreted, the inventive idea and techniques all changing range of water, should it will so that uniform water to replacement.

[25]

Below, embodiments of the present invention with reference to appended herewith detailed described as follows.

[26]

With reference to the 1 also, the sludge treatment apparatus of the present invention, ozone sludge into contact with ozone treatment tank (103) on; ozone treated sludge concentrated pus building precipitating (104) on; the pus building (104) of sludge in the three group dehydration apparatus (200); without using a tool.

[27]

Preferably, integer integer process bath (101) in the three sludge settling difference 2 (102) precipitating excess sludge discharged again in the ozone treatment tank (103) can be made to dissolve in and a solubilizer.

[28]

2 difference in a precipitation bath (102) is in the activated sludge mixed liquor is transmitted residence time tank precipitation, separation so that a processing water activated sludge separation of combustion chamber.

[29]

Ozone treatment tank (103) is ozone ozone generating device and a sludge settles, the decomposed slime layer while a large amount of foam are generated, parcel took for ozone treatment tank (103) includes a spray manner sludge liquid circulation ozone injection according to a lathering inhibiting or suppressing ozone bath agitating liquid can be lathering by mouth.

[30]

Ozone treatment tank (103) in a continuous manner and can be either batch or continuous ozone injection, while oxidized organic material in ozone to reduce implantation are eluted. The amount after the ozone treatment and the like will inspection and dissolved organic is incremented. This elution process micro fine particles is not precipitate that is available through the integer integer is returned to the process bath washes processing organics are nitrogen, removing carbon won be utilized as required without additional treatment facility can be achieved on the feeling made reduced in treating biological sludge.

[31]

Preferably, ozone treatment tank (103) is provided through the disinfection effect can be ultraviolet radiation ultraviolet lamp height.

[32]

pus building (104) in ozone treatment tank (103) solubilized in residual sludge or carbonate decomposition gas pipe is if not to increase concentration of the sludge volume and a reduction in amount of high solids reducing, e.g. sludge enrichment is precipitated and compacted using gravity based on the gravity-fed, sleep fine bubbles floating solids by the buoyancy of the water particles with cutting unit is attached to the frame a levitation, or using a centrifuge and through holes are concentrated to induce a centrifugal separation type concentrated method etc..

[33]

On the other hand pus building (104) being interposed between the treatment process after precipitation sludge in potable water treatment tank (101) can be introduced into the, the treatment process ozone treatment tank (103) are performed or the micro-particles excellent in biodegradability including solubilized in water purification treatment tank (101) won carbon can be used.

[34]

Dehydration apparatus (200) includes a certain degree or less moisture removal and many sludge moisture reduction in diameter are effected. On the other hand dewatering device (200) is installed with proper amount of aggregation agent sludge can be input.

[35]

Dehydration apparatus (200) in order to remove the dehydrated cake mop which in may be made finally building material are disclosed.

[36]

Figure 2 shows a in sludge treatment apparatus according to the invention, in a preferred embodiment of the dewatering device are disclosed.

[37]

Dehydration apparatus (200) includes a horizontal transfer section for dry sludge (210) is provided to maintain a high temperature atmosphere drying chamber (220) on, sludge is provided to put on high temperature environment horizontal transfer unit (210) by an exhaust fan extrusion to the extruder (230) having a predetermined wavelength.

[38]

Horizontal transfer unit (210) made the invention relates to a rotationally driven by the drive roller (211) on, drive roller (211) on endless track type belt (213) connected by its rotation to a driven roller (212) having a predetermined wavelength.

[39]

Drive roller (211) portion of the horizontal transfer section (210) speed of sludge can be conveyed along block, sludge take-off speed extruder (230) can be properly determined demonstrates the exiting of sludge.

[40]

Preferably, belt (213) includes a plurality of hole (213a) is formed belt (213) and transfers a horizontal atop the sludge (10) increasing the exposed surface of the sludge (10) helps evaporation of.

[41]

Drying chamber (220) is as long linear length of chamber, preferably maintains the temperature of the heat insulating material is employed inside, one end of the extruder (230) is assembled which contain sludge, drying is complete other dehydrated cake is discharged lower discharge (221) is provided of an upper inner peripheral (223) is provided in a drying chamber (220) internal pressure of down exhaust (222) is pair of substrates.

[42]

Preferably a discharge part (221) comprising a plurality of coffee grinder is formed rotation the crushing part (224) is provided in a dehydrated cake can be grinding during a transfer passage.

[43]

Drying chamber (220) in the horizontal transfer section (210) along the upper and/or lower heating member (225) are arranged in the drying chamber (220) which is heated inside the, e.g. heating members (225) can be a PCB comprising an electric by energy limited to heat are not correct.

[44]

Heating members (225) includes a horizontal transfer unit (210) for efficient evaporation from the sludge moved along which carries a sludge and is disposed adjacent the interference does not occur within a range that will.

[45]

Drying chamber (220) includes a horizontal transfer unit (210) in the vicinity of the end of the constant to have cutting plate (226) are provided and, horizontal transfer unit (210) is continuously conveyed along its sludge is cutting plate (226) while broken by discharge length unit (221) can be discharged.

[46]

Extruder (230) horizontal transfer unit (210) between the extruder (230) sludge exiting the horizontal transfer unit (210) to a predetermined inclination signal to dry can be made into a guide plate (227) can be provided.

[47]

Extruder (230) is fed at the top with a sludge supply (231a) is provided hollow-shaped body portion (231) on, body portion (231) for rotation in driving its short forms of screw (232) on, screw (232) integrally end body (231) extending 13a formed of molded 220. (233) on, screw (232) drive motor for rotationally driving the (234) having a predetermined wavelength.

[48]

Supply (231a) sludge kiln body (231) and a screw on (232) is compressed (solide bed) with space formed continuous extruded solid body (231) through a conical discharge combustion chamber.

[49]

On the other hand body portion (231) provided a compressing of the molded 220. (233) discharged by sludge (10) includes a hollow portion (11) is formed, the sludge (10) includes a horizontal transfer unit (210) moving along more large surface area exposed to the high temperature the amount of sludge that is evaporation can be induced. In particular, hollow section (11) is formed sludge (10) includes a hollow portion (11) is placed in a side of the gas expansion and the process can be achieved and pores at a lightweight dehydration cake formed on a surface of the mini microporous adsorbent such as product is a slumber disclosed.

[50]

Screw (232) and a drive motor (234) between the belt (235) mediated driving force such as number of the deceleration appropriate have a screw (232) rotating drive can be made.

[51]

Preferably, screw (232) includes a second internal hollow heating members 2 (232a) is provided in a extruder (230) in the compression side of the dome to sludge during hot minor axis length is 1. The, sludge is extruder (230) 13a of 100 °C or more made to each other until the heated exiting the first heating part 2 (232a) of heating a temperature preferably.

[52]

The printed circuit board and method for dehydration of a (200) includes a horizontal transfer unit a high temperature atmosphere (210) before being discharged into extruder (230) in the compression in the process where the first heating part 2 (232a) previously heated by hot, extruder (230) in most applications are significantly less dehydrated emulsion ink which state the horizontal transfer section 13a is a scrambler (210) of belt (213) to prevent sticking of the polyester can be. The invention also relates and method for dehydration of (200) includes dampers (223) through operation of drying chamber (220) and vapor pressure 5 inside the elastic, the drying chamber (220) sludge in sludge moisture saturated vapor exiting the inner peripheral zone of combustion reaction with air content and minimize sludge drying process can be prevented.

[53]

Figure 3 shows a in sludge treatment apparatus according to the invention, the dehydrated device as another embodiment of high, also 2 are identical in configuration identical to the description to make it possible to use a redundant cotton code about the difference in the described substrate.

[54]

Also with reference to the 3, the dewatering apparatus comprises an extruder (230) sludge is supplied through a horizontal transfer unit (210) dewatering is moving along in that case in aforementioned coping equal, in the present embodiment drying chamber (310) has a partition wall (311) by combustion chamber (310a) and drying chamber (310b) can be partitioned into, combustion chamber (310a) in gas burner (312) can be connected with a high temperature heat source is provided. Drying chamber (310b) in the horizontal transfer section (210) is located and that the, drying chamber (310b) the combustion chamber (310a) of sludge generated in splice loss across the weld can be made disclosed.

[55]

Combustion chamber (310a) combustion gas generated in the first heat exchange section 1 (320) via a ventilator (331) expelled out through, 1 while a second heat exchange section (320) has a blower 1 (332) heat exchange with external cold air and combustion gas supplied through anti-heating external air combustion chamber (310a) of combustion gas fed into the outer vessel is filled with waste-heat recovery can be made. On the other hand, drying chamber (310b) is separated from the external air introduced into the sludge is in flow along a plurality of guide plates diodes (313) can be provided.

[56]

On the other hand, drying chamber (310b) through pipe condenser (341) and connected, drying chamber (310b) vapor in closing part (310b) discharged into the other.

[57]

Condenser (341) integer treatment tank (101) pump (342) connected to the spray nozzle (341a) with a condenser (341) introduced into the vapor spray nozzle (341a) are cooled below 100 °C while being injected at through a condensation combustion chamber.

[58]

Condenser (341) number in the first condensation heat exchange section 2 (350) via its tank (101) and to move to a, 2 and the first heat exchange section (350) first blower in 2 (361) introduced through the external exchanging heat between the outside and a relatively high temperature state so that powders in high temperature of outer air is storage tank (362) are fed to a final drying and right in terms of prolapsing.

[59]

On the other hand condenser (341) second blower air in 3 (372) by the action of the cyclone separator (371) and to move to a, cyclone separator (371) air are separated from each other in the area where the waste combustion chamber air moisture are removed (310a) connected with combustion air in separate heat exchange section 2 is absorbed (350) via its tank (101) are supported.

[60]

The dewatering of sludge dewatering device according to an embodiment constructed as a solution of sludge are electrically utilize...copyright 2001.

[61]

Than the invention relates to the aforementioned embodiments and appended drawing that are not defined by and, within a range that the technical idea of the present invention from a heavy various substituted, modified change is vertical this invention is apparent to consultation with knowledge of will.

[62]

101: tank for potable water treatment tank 102:2 difference 103: ozone treatment tank 104: pus building 200: dehydration device 210: horizontal transfer unit 220, 310: drying chamber 230: extruder 310a: combustion chamber 310b: drying chamber 311: partition 312: gas burner



[63]

The present invention relates to a sludge treatment apparatus for sterilizing and deodorizing sludge for recycling the water purification sludge generated in a water purification process, comprising: an ozone treating tank (103) making sludge come in contact with ozone; a concentration tank (104) concentrating and depositing the ozone-treated sludge; and a dehydrating device (200) dehydrating the sludge deposited in the concentration tank (104), wherein the dehydrating device (200) includes a drying chamber (220) having a horizontal transfer part (210) for horizontally transferring the sludge, and maintaining a high temperature condition; and an extruder (230) extruding and discharging the input sludge to the horizontal transfer part (210) in a high temperature condition.



Ozone sludge into contact with ozone treatment tank (103) on, sludge is provided to concentrated ozone precipitating pus building (104) on, the pus building (104) of sludge in the three group dehydration apparatus (200) in sludge treatment apparatus comprising, the dewatering device (200) is, gas combustion type heat source connected with a combustion chamber (310a) and, said combustion chamber (310a) and polarization plate (311) therein with a horizontal transfer section for dry sludge (210) is provided room got dry sludge (310b) to maintain a high temperature atmosphere including drying chamber (310) on; high temperature environment the horizontal transfer section cast into the sludge (9990 000744999) extrusion to the extruder by an exhaust fan (230) on; said combustion chamber (310a) so that combustion gas and the outside air exchanging heat between heated air in the drying (310b) supplied to the heat exchange section 1 (320) on; the drying chamber (310b) connected to the condensing of the steam take-up condenser (341) on; a condenser (341) separating moisture in air to a body of a cyclone separator (371) on; the cyclone separator (371) connected to discharge air to the combustion chamber (310a) of fuel supplied to the blower (372) on; the cyclone separator (371) condensed water so that the heated air exiting the air exchanging heat between the first heat exchange section 2 provision of final dry discharged sludge (350); wherein, the drying chamber (310) is as long linear length of chamber, one end extruder (230) is assembled which contain sludge, drying is complete other dehydrated cake is discharged lower discharge (221) are provided and, the horizontal transfer unit (210) installed to upper or lower part along a plurality of 1 (225) is arranged, the extruder (230) is fed at the top with a sludge supply (231a) is provided hollow-shaped body portion (231) on, body portion (231) for rotation in driving 999000095099 9 hollow shape screw (232) on, the screw (232) end integrally formed with the body portion (231) extending 13a formed of molded 220. (233) on, the screw (232) of sludge is compressed to the inner side of the dome to 2 may be exposed to high temperature during the first heating part (232a) on, the screw (232) drive motor for rotationally driving the (234) including sludge treatment apparatus.

According to Claim 1, the bottom surface or the ozone, ultraviolet generating ultraviolet lamps further comprising sludge treatment apparatus.

Deletion

Deletion

Deletion

According to Claim 1, the condensation heat exchange heat exchange section 2 made from being transferred to the integer number integer processing is done the process bath characterized sludge treatment apparatus.

Deletion

Deletion