KR100791351B1 - The treatment apparatus for recycle sludge from sewage - Google Patents

The treatment apparatus for recycle sludge from sewage Download PDF

Info

Publication number
KR100791351B1
KR100791351B1 KR1020070098707A KR20070098707A KR100791351B1 KR 100791351 B1 KR100791351 B1 KR 100791351B1 KR 1020070098707 A KR1020070098707 A KR 1020070098707A KR 20070098707 A KR20070098707 A KR 20070098707A KR 100791351 B1 KR100791351 B1 KR 100791351B1
Authority
KR
South Korea
Prior art keywords
sewage sludge
water content
water
drying
mixer
Prior art date
Application number
KR1020070098707A
Other languages
Korean (ko)
Inventor
서윤석
Original Assignee
주식회사 파스템
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 주식회사 파스템 filed Critical 주식회사 파스템
Priority to KR1020070098707A priority Critical patent/KR100791351B1/en
Application granted granted Critical
Publication of KR100791351B1 publication Critical patent/KR100791351B1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/127Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/02Odour removal or prevention of malodour
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/26Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Treatment Of Sludge (AREA)

Abstract

An apparatus for recycling sewage sludge is provided to reduce treatment cost substantially by efficiently producing solid granules with a water content of 5% from sewage sludge containing water, simplify structure of facilities by making it not necessary to install auxiliary heating equipment, and produce a supplementary fuel of high quality by reducing the salt concentration substantially. An apparatus for recycling sewage sludge comprises: a mixer(10) for uniformly mixing sewage sludge and supplying a mixed sewage sludge with a water content of 55 to 60%; a rotary impact type drying and pulverizing machine(20) for separating water and solid granules with a water content of 5% from the sewage sludge supplied from the mixer by the particle impaction process using high speed centrifugal force; a scrubber(30) for separating gas and liquid from water separated in the drying and pulverizing machine to discharge the gas and the liquid to the outside; and an odor remover(40) for purifying the gas separated in the scrubber using ozone and plasma to remove odor from the gas, wherein sewage sludge is supplied to the mixer such that the sewage sludge comprises sewage sludge with a water content of 75% and sewage sludge with a water content of 5% at a ratio of 3:1, and the sewage sludge with a water content of 5% is the solid granules separated in the drying and pulverizing machine.

Description

하수 슬러지 재활용 처리 장치{THE TREATMENT APPARATUS FOR RECYCLE SLUDGE FROM SEWAGE}Sewage Sludge Recycling Unit {TH TREATMENT APPARATUS FOR RECYCLE SLUDGE FROM SEWAGE}

본 발명은 하수 슬러지 재활용 처리장치 및 방법에 관한 것으로, 보다 상세하게는 하수처리장에서 발생되는 슬러지를 연소 가능한 미립 고형물과 수분으로 분리하여 미립 고형물은 석탄을 연료로 사용하는 화력발전소 등에서 보조연료로서 사용할 수 있도록 하고 수분은 물과 기체로 분리한 후, 기체는 악취를 제거하여 대기중으로 방출하고 물은 하수처리장으로 배출하는 하수 슬러지 재활용 처리장치 및 방법에 관한 것이다.The present invention relates to an apparatus and method for recycling sewage sludge, and more particularly, to separate sludge generated in a sewage treatment plant into combustible particulate solids and water so that the particulate solids can be used as auxiliary fuel in coal-fired power plants. The present invention relates to a sewage sludge recycling apparatus and method in which water is separated into water and gas, and gas is released to the atmosphere by removing odors and water is discharged to a sewage treatment plant.

하수처리장에서는 막대한 양의 하수 슬러지가 지속적으로 발생되고 있으며, 이러한 하수 슬러지를 처리함에 있어, 가장 일반적인 처리방식은, 황무지나 매립지에 매립하는 것이다.In sewage treatment plants, huge amounts of sewage sludge are continuously generated, and in treating such sewage sludge, the most common treatment method is landfilling in wasteland or landfill.

그러나 황무지나 매립지는 매립할 수 있는 면적이 한정되어 있기 때문에 매립이 자유롭지 못하고 매립 허가조건도 매우 까다롭다. 또한 다른 분야에서 발생하는 다량의 폐기물이 함께 매립되므로 매립할 수 있는 장소가 급속히 고갈되고 있는 실정에 있으며, 매립지 선정에도 많은 어려움이 있어 지역적 분쟁과 사회적 문제를 야기하고 있다.However, because the waste land and landfills have a limited landfill area, landfilling is not free and the landfill permit conditions are very demanding. In addition, since a large amount of waste from other fields is buried together, the place for landfill is rapidly depleted, and there are many difficulties in selecting landfill sites, causing local conflicts and social problems.

또한 하수 슬러지를 매립하기 전에 어느 정도 탈수 및 건조시키고는 있지만, 그래도 함수율이 높기 때문에, 매립시 악취와 유독가스를 유발하여 공기를 오염시키고 땅으로 스며드는 침출수는 지하수를 오염시키는 원인이 되고 있다.In addition, although the sewage sludge is dewatered and dried to some extent before being landfilled, the water content is still high, so that leachate that contaminates the air by causing odors and toxic gases during landfilling and penetrates to the ground causes contamination of groundwater.

따라서 본 발명은 상기한 종래의 문제점을 해결하기 위한 것으로, 그 목적은 수분을 함유한 하수 슬러지를 고속 원심력을 이용한 입자충돌의 운동에너지만으로 고액 분리하여 함수율 5%의 미립 고형분을 효율적으로 생산하는 것에 의해 에너지 효율 극대화로 처리비용을 획기적으로 절감할 수 있고, 가열에 따른 부대설비가 필요 없어 설비구성이 간결하고 2차 오염원 발생이 없으며, 설치면적이 기존 가열방식이나 기타 퇴비화, 고형화 설비에 비해 현저히 작은 하수 슬러지 재활용 처리시스템을 제공하는데 있다.Therefore, the present invention is to solve the above-mentioned problems, the object is to solid-liquid separation of sewage sludge containing water with only the kinetic energy of particle collision using a high-speed centrifugal force to efficiently produce particulate solids of 5% moisture content. By maximizing energy efficiency, the processing cost can be drastically reduced, and no additional equipment is required due to heating, so the equipment configuration is simple and there is no secondary pollution source, and the installation area is significantly higher than the existing heating method or other composting and solidifying equipment. It is to provide a small sewage sludge recycling treatment system.

또한 본 발명은 소요 에너지가 전력이고, 자동화 시스템으로 운영됨으로 운전 인력을 최소화할 수 있고, 설비의 유지보수가 매우 용이하여 유지보수비가 저렴하며, 염분농도를 현저히 감소시킴으로써 양질의 보조연료를 생산할 수 있는 하수 슬러지 재활용 처리시스템을 제공하는데 있다.In addition, the present invention can minimize the manpower as the energy required, the operation of the automated system, the maintenance cost of the equipment is very easy to maintain the maintenance cost is low, and the salinity can be significantly reduced to produce high quality auxiliary fuel To provide a sewage sludge recycling treatment system.

상기의 목적을 달성하기 위한 본 발명의 제1의 발명은, 공급되는 하수 슬러지를 균일하게 혼합하기 위한 믹서와, 상기 믹서로부터 공급된 하수 슬러지를 고속 원심력에 의한 입자충돌방식으로 미립 고형분과 수분으로 분리하는 회전충격식 건조 및 분쇄기와, 상기 회전충격식 건조 및 분쇄기에서 분리된 수분을 기체와 액체로 분리하여 각각 외부로 배출하는 스크러버를 포함하는 하수 슬러지 재활용 처리장치에 특징이 있다.The first invention of the present invention for achieving the above object is a mixer for uniformly mixing the supplied sewage sludge, and the sewage sludge supplied from the mixer in the form of fine particles and water in a particle collision method by a high-speed centrifugal force It is characterized by a sewage sludge recycling processing apparatus comprising a rotary impact drying and pulverizer to separate, and a scrubber to separate the water separated from the rotary impact drying and pulverizer into a gas and a liquid and discharge it to the outside, respectively.

제2의 발명은, 상기 스크러버에서 분리된 기체를 정화처리하여 대기로 방출하는 악취제거기를 더욱 포함하는 하수 슬러지 재활용 처리장치에 특징이 있다. According to a second aspect of the present invention, there is provided a sewage sludge recycling apparatus further comprising a odor remover for purifying the gas separated from the scrubber and releasing it to the atmosphere.

제3의 발명은, 상기 스크러버의 정화처리는 오존 및 플라즈마 처리인 하수 슬러지 재활용 처리장치에 특징이 있다. A third aspect of the present invention is the sewage sludge recycling treatment apparatus in which the scrubber purification process is ozone and plasma treatment.

제4의 발명은, 하수 슬러지를 믹서로 균일하게 혼합하여 함수율 55~60%가 되도록 하여 공급하는 전처리공정과, 상기 전처리공정을 거쳐 공급된 하수 슬러지를 고속 원심력에 의한 회전충격식 건조 및 분쇄기로 함수율 5%의 미립 고형분과 수분을 분리하는 건조 및 분쇄공정과, 상기 건조 및 분쇄공정에서 분리된 미립 고형분을 외부로 배출하는 반출공정과, 상기 건조 및 분쇄공정에서 분리된 수분을 기체와 액체로 분리하여 각각 외부로 배출하는 스크러버공정을 포함하는 하수 슬러지 재활용 처리방법에 특징이 있다.The fourth invention is a pretreatment step of uniformly mixing the sewage sludge with a mixer to reach a water content of 55 to 60% and a sewage sludge supplied through the pretreatment step by a high-speed centrifugal rotary drying and pulverizer. A drying and grinding step of separating particulate solids and water having a moisture content of 5%, a discharging step of discharging the particulate solids separated in the drying and grinding steps to the outside, and the water separated in the drying and grinding steps as a gas and a liquid. The sewage sludge recycling process includes a scrubber process that separates and discharges each to the outside.

제5의 발명은, 상기 스크러버공정에서 분리된 기체를 정화처리하여 대기로 방출하는 악취제거공정을 더욱 포함하는 하수 슬러지 재활용 처리방법에 특징이 있다.The fifth aspect of the present invention is characterized in that the sewage sludge recycling process further includes a odor removal step of purifying the gas separated in the scrubber process and releasing it to the atmosphere.

제6의 발명은, 상기 스크러버공정에서의 정화처리는 오존 및 플라즈마 처리인 하수 슬러지 재활용 처리방법에 특징이 있다.According to a sixth aspect of the present invention, the purification treatment in the scrubber step is characterized in that the sewage sludge recycling treatment method is ozone and plasma treatment.

제7의 발명은, 상기 전처리공정으로 공급되는 하수 슬러지는, 함수율 75%의 하수 슬러지와 함수율 5%의 하수 슬러지를 3:1의 비율이 되도록 공급하는 하수 슬러지 재활용 처리방법에 특징이 있다.According to a seventh aspect of the present invention, sewage sludge supplied in the pretreatment step is characterized by a sewage sludge recycling treatment method in which a sewage sludge having a water content of 75% and a sewage sludge having a water content of 5% are supplied at a ratio of 3: 1.

제8의 발명은, 상기 전처리공정으로 공급되는 함수율 5%의 하수 슬러지는 건조 및 분쇄공정에서 분리된 미립 고형분인 하수 슬러지 재활용 처리방법에 특징이 있다. The eighth invention is characterized in that the sewage sludge having a water content of 5% supplied to the pretreatment step is a sewage sludge recycling treatment method which is a particulate solid separated in a drying and grinding step.

본 발명에 따른 하수 슬러지 재할용 처리장치는,Treatment apparatus for sewage sludge recycling according to the present invention,

수분을 함유한 하수 슬러지를 매립하지 않고 고속 원심력을 이용한 입자충돌의 운동에너지만으로 고액 분리하여 연소가 가능한 함수율 5%의 미립 고형분을 생산할 수 있고, 이 미립 고형분을 화력발전소의 연료로 사용하는 석탄의 보조연료로 재활용함으로써 자연환경을 보호하면서 경제적인 이점을 함께 추구할 수 있는 효과가 있다.It is possible to produce fine solids with a water content of 5% that can be burned by solid-liquid separation only by kinetic energy of particle collision using high-speed centrifugal force, without reclaiming sewage sludge containing water, and using the fine solids as fuel for thermal power plants. Recycling as auxiliary fuel can protect the natural environment and pursue economic benefits together.

또한, 본 발명에 따른 하수 슬러지 재할용 처리장치는, In addition, the treatment apparatus for sewage sludge recycling according to the present invention,

미립 고형분의 생산방식이 고속 원심력을 이용한 입자충돌에 의해 분리 및 분쇄되므로 에너지 효율 극대화로 처리비용을 획기적으로 절감할 수 있으며, 가열에 따른 부대설비가 필요 없어 설비구성이 간결하고 설치면적이 기존 가열방식이나 기타 퇴비화, 고형화 설비에 비해 현저히 작은 효과가 있다.Since the production method of fine solids is separated and pulverized by particle collision using high-speed centrifugal force, the processing cost can be drastically reduced by maximizing energy efficiency. It has a significantly smaller effect compared to anticorrosive or other composting and solidifying plants.

또한, 본 발명에 따른 하수 슬러지 재할용 처리장치는, 소요 에너지가 전력이고 자동화 시스템으로 운영되므로 운전 인력을 최소화할 수 있고, 설비의 유지보수가 매우 용이하여 저렴한 유지보수비로 운용할 수 있는 효과가 있다. In addition, the treatment device for sewage sludge recycling according to the present invention has the effect that the required energy is electric power and operated as an automated system to minimize the manpower, and the maintenance of the equipment is very easy to operate at a low maintenance cost. have.

이하, 본 발명의 바람직한 실시예를 첨부도면에 의하여 상세하게 설명한다.Hereinafter, preferred embodiments of the present invention will be described in detail by the accompanying drawings.

우선 각 도면의 구성요소들에 참조부호를 부가함에 있어서, 동일한 구성요소 들에 대해서는 비록 다른 도면상에 표시되더라도 가능한 한 동일한 부호를 가지도록 하고 있음에 유의해야 한다. 또한, 본 발명을 설명함에 있어서, 관련된 공지 구성 또는 기능에 대한 구체적인 설명이 본 발명의 요지를 흐릴 수 있다고 판단되는 경우에는 그 상세한 설명은 생략한다.First of all, in adding reference numerals to the components of each drawing, it should be noted that the same reference numerals are designated as much as possible even if displayed on different drawings. In addition, in describing the present invention, when it is determined that the detailed description of the related well-known configuration or function may obscure the gist of the present invention, the detailed description thereof will be omitted.

도 1은 본 발명에 따른 하수 슬러지 재활용 처리장치를 나타낸 구성도이고, 도 2는 본 발명에 따른 하수 슬러지 재활용 처리장치에 의해서 하수 슬러지가 처리되는 공정을 도시한 공정도이다.1 is a block diagram showing a sewage sludge recycling treatment apparatus according to the present invention, Figure 2 is a process diagram showing a process for treating sewage sludge by the sewage sludge recycling treatment apparatus according to the present invention.

도 1에 도시된 바와 같이, 본 발명의 하수 슬러지 재활용 처리장치는 공급된 하수 슬러지를 균일하게 혼합하는 믹서(10)와, 상기 믹서(10)로부터 공급된 하수 슬러지를 미립 고형분과 수분으로 분리하기 위한 회전충격식 건조 및 분쇄기(20)와, 상기 히전충격식 건조 및 분쇄기(20)에서 분리된 수분을 기체와 액체로 분리하여 각각 외부로 배출하는 스크러버(30)와, 상기 스크러버(30)에서 분리된 기체를 정화처리하여 대기로 방출하는 악취제거기(40)를 구비하여 이루어진다.As shown in Figure 1, the sewage sludge recycling treatment apparatus of the present invention is to separate the sewage sludge supplied from the mixer 10 and the particulate solids and water uniformly mixed with the supplied sewage sludge. In the rotary impact drying and grinder 20, the scrubber 30 to separate the water separated from the electric shock-type drying and grinder 20 into a gas and a liquid and discharged to the outside, respectively, and in the scrubber 30 It comprises a odor remover 40 for purifying the separated gas to release to the atmosphere.

이러한 하수 슬러지 재활용 처리장치를 이용한 처리방법은, 도 2에 도시된 바와 같이 공급되는 하수 슬러지를 믹서(10)로 균일하게 혼합하는 전처리공정(100)과, 상기 전처리공정(100)에서 공급되는 하수 슬러지를 회전충격식 건조 및 분쇄기(20)로 미립 고형분과 수분으로 분리하는 건조 및 분쇄공정(200)을 수행하여 이루어진다.The treatment method using the sewage sludge recycling treatment apparatus includes a pretreatment step 100 for uniformly mixing the sewage sludge supplied to the mixer 10 as shown in FIG. 2, and the sewage water supplied from the pretreatment step 100. The sludge is made by performing a drying and grinding process 200 for separating the particulate solids and moisture into the rotary impact drying and milling machine 20.

전처리공정(100)에서는 재활용 처리하고자 하는 하수 슬러지를 건조 및 분쇄 공정을 위한 회전충격식 건조 및 분쇄기(20)에 투입하기 전에, 공급되는 하수 슬러지를 믹서(10)로 균일하게 혼합하여 함수율 55~60%가 유지되도록 하기 위한 것으로, 이는 회전충격식 건조 및 분쇄기(20)로 하수 슬러지를 처리함에 있어서 공급되는 하수 슬러지의 함수율이 55~60%일 때, 건조 및 분쇄효율이 가장 높고 함수율이 60% 이상에서는 건조 및 분쇄공정이 이루어지지 않기 때문이다.In the pre-treatment process 100, the sewage sludge to be recycled is mixed uniformly with the mixer 10 before being introduced into the rotary impact type drying and crusher 20 for drying and crushing, and the water content 55 ~. It is intended to maintain 60%, which is the highest drying and grinding efficiency and the water content is 60, when the moisture content of the sewage sludge supplied in the treatment of sewage sludge with rotary impact drying and mill 20 is 55 ~ 60% It is because a drying and a grinding | pulverization process are not performed at% or more.

건조 및 분쇄공정(200)을 위한 회전충격식 건조 및 분쇄기(20)는 고정외통 내에 고속 회전이 가능한 회전내통을 구비하여 회전내통의 고속회전에 의한 원심력 및 충격을 이용한 것으로, 하수 슬러지를 회전내통에 공급하여 고속 회전시키면, 하수 슬러지에 함유된 수분은 원심력에 의해 고정외통으로 분리되어 다음 스크러버공정(300)을 위해 스크러버(30)로 이송되고, 수분제거로 인해 함수율 5%인 하수 슬러지는 회전내통내에서의 회전충격에 의해 미세한 분말로 분쇄된 후 원심력에 의해 비산되어 외부로 배출됨으로써 하수 슬러지를 미립 고형물과 수분으로 분리할 수 있게 된다.The rotary impact drying and pulverizer 20 for the drying and crushing process 200 is equipped with a rotary inner cylinder capable of high-speed rotation in a fixed outer cylinder and uses centrifugal force and impact by high-speed rotation of the rotary inner cylinder, and sewage sludge is rotated in an inner cylinder. When supplied to the high-speed rotation, the water contained in the sewage sludge is separated into a fixed outer cylinder by centrifugal force and then transferred to the scrubber 30 for the next scrubber process 300, the sewage sludge having a moisture content of 5% due to water removal is rotated After being crushed into fine powder by rotational impact in the inner cylinder and scattered by centrifugal force and discharged to the outside, sewage sludge can be separated into particulate solids and water.

이때, 전처리공정(100)을 위해 믹서(10)로 공급되는 하수 슬러지는 함수율 75%의 하수 슬러지 1000㎏/h와, 함수율 5%의 하수 슬러지 500㎏/h를 공급, 즉 3:1의 비율로 공급하여 균일하게 혼합한 후, 함수율 55~60%의 하수 슬러지 1500㎏/h를 건조 및 분쇄공정(200)을 위한 회전충격식 건조 및 분쇄기(20)로 투입하는 것이 바람직하다.At this time, the sewage sludge supplied to the mixer 10 for the pretreatment process 100 supplies 1000 kg / h of sewage sludge with a water content of 75% and 500 kg / h of sewage sludge with a water content of 5%, that is, a ratio of 3: 1. After supplying uniformly and uniformly mixing, 1500 kg / h of sewage sludge having a water content of 55 to 60% is preferably introduced into the rotary impact drying and pulverizer 20 for the drying and crushing process 200.

또한, 상기 함수율 5%의 하수 슬러지는 건조 및 분쇄공정(200)에서 분리된 미립 고형분을 공급하는 것이 보다 효율적인 것으로, 회전충격식 건조 및 분쇄 기(20)에 의해 수행되는 건조 및 분쇄공정(200)에서는 믹서(10)로부터 공급된 1500㎏/h의 하수 슬러지를 처리하여 분리된 750㎏/h의 미립 고형물중 500㎏/h는 믹서(20)로 리턴시키고, 270㎏/h의 미립 고형물은 외부로 반출함으로써 연료로서 사용한다.In addition, the sewage sludge having a water content of 5% is more efficient to supply the particulate solids separated in the drying and grinding process 200, and the drying and grinding process 200 performed by the rotary impact drying and grinding machine 20. ), 500 kg / h of the separated 750 kg / h of the particulate solids treated by 1500 kg / h of sewage sludge supplied from the mixer 10 is returned to the mixer 20, and 270 kg / h of the particulate solids is It is used as fuel by carrying out to the outside.

한편, 상기 회전충격식 건조 및 분쇄기(20)에 의한 건조 및 분쇄공정(200)에서 분리된 수분은 기체, 약간의 미세분말 및 물입자를 포함하고 있으며, 이 수분은 스크러버(30)로 공급되어 스크러버공정(300)을 수행함으로써 기체와 슬러지를 포함하는 물로 분리처리되고, 이때, 스크러버(20)는 15N㎥/min의 처리능력을 가지는 것이 바람직하다. On the other hand, the water separated in the drying and grinding process 200 by the rotary impact drying and mill 20 contains a gas, some fine powder and water particles, this moisture is supplied to the scrubber 30 By performing the scrubber process 300 is separated into water containing gas and sludge, in this case, the scrubber 20 preferably has a processing capacity of 15Nm 3 / min.

이어서 상기 스크러버공정(300)에서 분리된 슬러지를 포함하는 물은 1.5Ton/h의 용량으로 배출되어 하수처리장에서 정화처리되고, 기체는 15N㎥/min으로 악취제거기(40)에 공급되어 악취제거공정(400)을 수행하게 되며, 이 악취제거공정(400)을 통해 정화되어 대기로 방출되는 것으로, 정화처리는 오존 및 플라즈마 처리하여 기체의 방출시 악취를 제거함과 동시에 대기의 오염을 방지할 수 있도록 한다.Subsequently, the water containing the sludge separated in the scrubber process 300 is discharged at a capacity of 1.5Ton / h and purified in a sewage treatment plant, and the gas is supplied to the odor remover 40 at 15 Nm3 / min to remove the odor. 400 to be carried out, and to be purified and discharged to the atmosphere through the odor removal step 400, the purification treatment is ozone and plasma treatment to remove odors during the release of gas and at the same time to prevent pollution of the atmosphere. do.

본 발명의 권리범위는 지금까지 설명된 실시예에 한정되는 것은 아니고, 본 발명의 기술적 사상과 특허청구범위 내에서 이 분야의 당업자에 의하여 다양한 변경, 변형 또는 치환이 가능할 것이며, 그와 같은 실시예들은 본 발명의 범위에 속하는 것으로 이해되어야 한다.The scope of the present invention is not limited to the embodiments described so far, and various changes, modifications, or substitutions may be made by those skilled in the art within the technical spirit and claims of the present invention, and such embodiments. Should be understood to fall within the scope of the present invention.

도 1은 본 발명에 따른 하수 슬러지 재활용 처리장치를 나타낸 구성도.1 is a block diagram showing a sewage sludge recycling treatment apparatus according to the present invention.

도 2는 본 발명에 따른 하수 슬러지 재활용 처리방법을 나타낸 공정도.Figure 2 is a process chart showing the sewage sludge recycling treatment method according to the present invention.

<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>

10 : 믹서 20 : 회전충격식 건조 및 분쇄기10: mixer 20: rotary impact drying and milling

30 : 스크러버 40 : 악취제거기 30: scrubber 40: odor remover

Claims (1)

공급되는 하수 슬러지를 균일하게 혼합하여 함수율이 55~60%가 되도록 하는 믹서;A mixer for uniformly mixing the supplied sewage sludge so that the moisture content is 55 to 60%; 상기 믹서로부터 공급된 하수 슬러지를 고속 원심력에 의한 입자충돌방식에 의해서 함수율 5%의 미립 고형분과 수분으로 분리하는 회전충격식 건조 및 분쇄기;A rotary impact drying and pulverizer for separating sewage sludge supplied from the mixer into particulate solids and water having a moisture content of 5% by a particle collision method by high speed centrifugal force; 상기 건조 및 분쇄기에서 분리된 수분을 기체와 액체로 분리하여 각각 외부로 배출하는 스크러버; 및A scrubber that separates the water separated from the drying and grinder into a gas and a liquid and discharges them to the outside; And 상기 스크러버에서 분리된 기체를 오존 및 플라즈마를 이용하여 정화함으로써 악취를 제거하는 악취제거기를 포함하고,A odor remover for removing odors by purifying the gas separated from the scrubber using ozone and plasma, 상기 믹서로 공급되는 하수 슬러지는, 함수율 75%의 하수 슬러지와 함수율 5%의 하수 슬러지를 3:1의 비율이 되도록 공급하고, 상기 믹서로 공급되는 함수율 5%의 하수 슬러지는 상기 건조 및 분쇄기에서 분리된 미립 고형분인 것을 특징으로 하는 하수 슬러지 재활용 처리장치.The sewage sludge supplied to the mixer is supplied so that the sewage sludge having a water content of 75% and the sewage sludge having a water content of 5% is 3: 1, and the sewage sludge having a water content of 5% supplied to the mixer is in the drying and grinder. Sewage sludge recycling treatment apparatus, characterized in that the separated particulate solids.
KR1020070098707A 2007-10-01 2007-10-01 The treatment apparatus for recycle sludge from sewage KR100791351B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020070098707A KR100791351B1 (en) 2007-10-01 2007-10-01 The treatment apparatus for recycle sludge from sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020070098707A KR100791351B1 (en) 2007-10-01 2007-10-01 The treatment apparatus for recycle sludge from sewage

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
KR1020060118389A Division KR100797574B1 (en) 2006-11-28 2006-11-28 The treatment method for recycle sludge from sewage

Publications (1)

Publication Number Publication Date
KR100791351B1 true KR100791351B1 (en) 2008-01-04

Family

ID=39216598

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020070098707A KR100791351B1 (en) 2007-10-01 2007-10-01 The treatment apparatus for recycle sludge from sewage

Country Status (1)

Country Link
KR (1) KR100791351B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101263098B1 (en) 2011-04-27 2013-05-09 김순영 Organic waste treatment system

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000061499A (en) 1998-08-21 2000-02-29 Toshiba Corp Sludge drying treatment system
KR200184520Y1 (en) 1999-11-03 2000-06-01 신성산건주식회사 Dryness system for crvsh type of shocks

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000061499A (en) 1998-08-21 2000-02-29 Toshiba Corp Sludge drying treatment system
KR200184520Y1 (en) 1999-11-03 2000-06-01 신성산건주식회사 Dryness system for crvsh type of shocks

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101263098B1 (en) 2011-04-27 2013-05-09 김순영 Organic waste treatment system

Similar Documents

Publication Publication Date Title
JP4438329B2 (en) Method for treating waste containing organic matter
JP6302612B2 (en) Waste treatment and energy production system and method including raw garbage or livestock manure
KR101066124B1 (en) Dry-wet serial anaerobic digestion device and method for producing biogas from high concentrated organic waste
CN104801528A (en) Domestic waste organic treatment method
CN104230086A (en) Method for recycling water-based paint detergent waste liquid
CN211056924U (en) Innocent treatment system of oily sludge
JP2011168694A (en) Method for producing solid fuel
KR100797574B1 (en) The treatment method for recycle sludge from sewage
KR100791351B1 (en) The treatment apparatus for recycle sludge from sewage
KR100791350B1 (en) The treatment method for recycle sludge from sewage
JP2005199132A (en) Inflammable garbage sorting system
KR102061159B1 (en) Method and apparatus for mixed thermal treatment of organic sludge and contaminated soil
CN112536313A (en) Treatment method of industrial waste salt containing organic pollutants
EP2268426B1 (en) Integrated plant for separation, recovery and re-use of solid domestic waste, with production of cement and/or bricks
JP2006315885A (en) Recycled fertilizer and method of producing the same
CN109500049A (en) A kind of daily-life garbage without environmental pollution recycling processing method utilized with effluent cycle
KR100645009B1 (en) Viscosity deactivating apparatus of sludge
JP4948235B2 (en) Incineration fly ash treatment method
RU2734832C1 (en) Incineration plant, device and method
CN211035778U (en) System equipment for producing humic acid by using low-calorific-value coal
KR20030026524A (en) System which combine sewage sludges with food wastes treatment on anaerobic digestion using automatic mill separator
CN112341490A (en) Method for thermochemical treatment and resource utilization of waste glyphosate salt
CN102380228B (en) Extracting agent for treating dioxin in flying ash and method for extracting dioxin by extracting agent
JP4062789B2 (en) Detoxification method for firebrick or mortar containing dioxins
TWI829579B (en) Methods of making derived fuels from waste

Legal Events

Date Code Title Description
A107 Divisional application of patent
A201 Request for examination
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20121205

Year of fee payment: 6

FPAY Annual fee payment

Payment date: 20131227

Year of fee payment: 7

FPAY Annual fee payment

Payment date: 20141229

Year of fee payment: 8

FPAY Annual fee payment

Payment date: 20151228

Year of fee payment: 9

LAPS Lapse due to unpaid annual fee