KR20010002287A - An apparatus and method for drying sludge - Google Patents
An apparatus and method for drying sludge Download PDFInfo
- Publication number
- KR20010002287A KR20010002287A KR1019990022026A KR19990022026A KR20010002287A KR 20010002287 A KR20010002287 A KR 20010002287A KR 1019990022026 A KR1019990022026 A KR 1019990022026A KR 19990022026 A KR19990022026 A KR 19990022026A KR 20010002287 A KR20010002287 A KR 20010002287A
- Authority
- KR
- South Korea
- Prior art keywords
- belt
- drum
- sludge
- drums
- drying apparatus
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/123—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using belt or band filters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/02—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/04—Agitating, stirring, or scraping devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/18—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact
- F26B3/20—Drying solid materials or objects by processes involving the application of heat by conduction, i.e. the heat is conveyed from the heat source, e.g. gas flame, to the materials or objects to be dried by direct contact the heat source being a heated surface, e.g. a moving belt or conveyor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/18—Sludges, e.g. sewage, waste, industrial processes, cooling towers
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Microbiology (AREA)
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
본 발명은 슬러지 건조장치 및 건조방법에 관한 것이다. 보다 구체적으로 스팀에 의해 가열되는 드럼 사이에 두 개의 벨트를 걸고 그 사이로 슬러지를 통과시켜 슬러지가 드럼의 표면에 접촉하면서 건조되도록 한 슬러지 건조장치 및 건조방법에 관한 것이다.The present invention relates to a sludge drying apparatus and a drying method. More specifically, the present invention relates to a sludge drying apparatus and a drying method in which two belts are sandwiched between drums heated by steam, and the sludge is passed therebetween so that the sludge is dried while contacting the surface of the drum.
슬러지는 활성오니법으로 폐수를 정화처리하는 과정에서 대량 발생되는 유기성 폐기물로써 그 자체는 높은 열량을 갖고 있으며, 일반적으로 산업체에서 배출되는 각종 산업폐기물 중 고형 폐기물은 재래식 소각설비로도 비교적 쉽게 연소가 가능하므로 대부분 자체 소각 처리하여 폐열 회수 등 에너지 자원으로 재활용하고 있으나, 많은 양의 수분을 포함하고 있는 슬러지의 경우는 수분 때문에 소각이 매우 어려운 실정이다.Sludge is an organic waste that is generated in a large amount in the process of purifying wastewater by the activated sludge method, and it has a high calorie value.In general, solid waste among various industrial wastes discharged from the industry is relatively easily burned by conventional incineration facilities. Most of them are incinerated and recycled as energy resources such as waste heat recovery. However, in case of sludge containing a large amount of water, incineration is very difficult due to moisture.
현재 대다수의 산업체에서는 농축된 슬러지에 탈수가 잘 되도록 고분자 응입제 등 화학약품을 첨가하여 벨트 프레스 등 기계식 탈수방식을 사용하여 함수율 70-80% 까지는 탈수가 가능하나 자체 연소가 가능한 30% 미만으로의 탈수는 불가능한 상태이다. 따라서 대부분의 산업체 또는 하수종말처리장에서 발생된 슬러지들은 아직 자체소각 처리하지 못하고 폐기물 처리 전문 업체에 용역을 주어 매립처리하고 있는 실정이다. 그러나, 이는 환경문제에 대한 사회 전반적인 인식과 매립처리시설의 한계로 인해 많은 처리비용을 부담하게 되었고 이러한 현상은 점점 더 심화되고 있다.Currently, most industries add chemicals such as polymer coagulants to dewater the concentrated sludge and use mechanical dehydration method such as belt press to dehydrate up to 70-80% of water content but to less than 30% of self-combustion. Dehydration is impossible. Therefore, the sludge generated in most industrial or sewage treatment plants has not been incinerated yet, but has been serviced by a waste disposal company for landfill treatment. However, due to the general social awareness of environmental problems and the limitations of landfill facilities, this has caused a lot of treatment costs, and this phenomenon is getting worse.
최근 일부 대기업에서는 소각로에서 소각시 발생된 배기가스를 이용한 로타리 킬른식 건조기로 슬러지를 열풍 건조후 소각시키는 시스템을 설치하고 있다. 그러나 이는 설비 규모가 대형이어서 설치 면적이 크고, 수입품으로 거액의 설비비가 소요되며, 비싼 고분자 응집제를 필수적으로 첨가해야 하는 등 유지관리비가 많이 드는 문제가 있다.Recently, some large corporations have installed a system to incinerate sludge after hot air drying by rotary kiln type dryer using exhaust gas generated in incinerator. However, this is a large installation size, the installation area is large, a large amount of equipment costs as imports, there is a problem that a lot of maintenance costs, such as the need to add expensive polymer flocculant essential.
본 발명의 목적은 건조 효율이 우수하고 스팀 폐열을 이용할 수 있어 에너지 절약에 유리한 슬러지 건조장치 및 건조방법을 제공하는 것이다.An object of the present invention is to provide a sludge drying apparatus and a drying method which is excellent in drying efficiency and can use steam waste heat, which is advantageous for energy saving.
본 발명의 다른 목적은 슬러지의 건조과정에서 발생하는 불쾌한 공기를 유출시키지 않고 내부에서 순환할 수 있도록 하여 쾌적한 환경을 유지할 수 있고, 슬러지의 건조를 위한 공기를 사전에 건조 및 가열시켜 건조 효율을 향상시킬 수 있는 슬러지 건조장치 및 건조방법을 제공하는 것이다.Another object of the present invention is to maintain a pleasant environment by allowing the inside of the sludge to circulate without the unpleasant air generated during the drying process of the sludge, to improve the drying efficiency by drying and heating the air for drying the sludge in advance It is to provide a sludge drying apparatus and a drying method that can be.
도1은 본 발명의 슬러지 건조장치의 개념도이다.1 is a conceptual diagram of a sludge drying apparatus of the present invention.
도2는 본 발명의 슬러지 건조장치와 슬러지 건조장치에 공급하는 공기의 건조 및 가열을 위한 장치가 같이 설치된 슬러지 건조 시스템의 개념도이다.2 is a conceptual view of a sludge drying system in which the sludge drying apparatus and the apparatus for drying and heating the air supplied to the sludge drying apparatus are installed together.
<도면의 부호에 대한 간단한 설명><Short description of the symbols in the drawings>
1: 제1드럼 2a-2f: 제2드럼1: first drum 2a-2f: second drum
3a, 3b: 벨트 4: 스크레이퍼3a, 3b: belt 4: scraper
5: 건조실 6: 중간벽5: drying chamber 6: middle wall
7: 수평벽 8: 배기팬7: horizontal wall 8: exhaust fan
9: 급기팬 10: 냉각기9: supply fan 10: cooler
11: 방열기11: radiator
도면에 따라 본 발명을 설명한다. 도 1은 본 발명의 슬러지 건조장치의 개념도이다.The present invention will be described with reference to the drawings. 1 is a conceptual diagram of a sludge drying apparatus of the present invention.
본 발명의 슬러지 건조장치는 스팀에 의해서 가열되는 다수개의 제1드럼(1)과 상기 제1드럼(1) 사이에서 회전하는 두 개의 벨트(3a,3b)와 상기 벨트(3a,3b)를 지지하고 벨트(3a,3b)의 장력을 조정하기 위한 다수개의 제2드럼(2a-2f)과 배출구에서 상기 벨트(3a,3b)에 부착된 슬러지를 긁어내는 스크레이퍼(4)로 구성되는 것을 특징으로 한다.The sludge drying apparatus of the present invention supports a plurality of first drums 1 and two belts 3a and 3b rotating between the first drums 1 and the belts 3a and 3b which are heated by steam. And a plurality of second drums 2a-2f for adjusting the tension of the belts 3a and 3b and a scraper 4 which scrapes the sludge attached to the belts 3a and 3b from the discharge port. do.
드럼은 스팀에 의해 가열되는 직경이 큰 다수개의 제1드럼(1)과 상기 제1드럼(1) 사이에 끼어 회전하는 벨트(3a,3b)를 지지하고 벨트(3a,3b)의 장력을 조정하기 위한 직경이 작은 6개의 제2드럼(2a-2f)으로 구성된다. 제1드럼(1)은 양단부가 폐쇄된 원통의 형상으로 중앙에 중심축이 관통하여 중심축을 중심으로 회전하고, 양단부에 각각 스팀 유입구와 배출구가 설치되어 스팀에 의해 가열된다. 다수개의 제1드럼(1)은 슬러지 건조장치의 중앙부에 수평으로 평행하게 상하로 교대로 설치된다. 제2드럼(2a-2f)은 상기 제1드럼(1)의 좌우측으로 각각 제1드럼의 상부에 두 개(2a,2b), 제1드럼의 하부에 두 개(2c,2d), 그 아래쪽으로 다시 두 개(2e,2f)가 설치되며, 상부와 하부의 제2드럼(21,2b,2e,2f)중 하나씩은 위치를 이동하여 고정할 수 있도록 되어 있어 벨트의 장력을 조정할 수 있다.The drum supports a plurality of first drums 1 having a large diameter heated by steam and the belts 3a and 3b which are rotated between the first drums 1 and adjust the tension of the belts 3a and 3b. It consists of six 2nd drums 2a-2f of small diameter for this purpose. The first drum 1 has a cylindrical shape in which both ends are closed, and a central axis penetrates in the center thereof to rotate about the central axis, and steam inlets and outlets are respectively installed at both ends and heated by steam. The plurality of first drums 1 are alternately installed in the center of the sludge drying apparatus horizontally and parallelly up and down. The second drums 2a-2f are two (2a, 2b) at the top of the first drum, two (2c, 2d) at the bottom of the first drum, and the lower side of the first drum (1) at the left and right sides, respectively. Two (2e, 2f) is installed again, one of the upper and lower second drum (21, 2b, 2e, 2f) is to be fixed by moving the position can adjust the tension of the belt.
벨트는 제1벨트(3a)와 제2벨트(3b)로 구성되고 제1드럼(1)과 제2드럼(2a-2f) 사이에 끼워져 드럼의 회전에 따라 같이 회전하게 된다. 제1벨트(3a)는 상부와 중간 제2드럼(2a-2d)을 거쳐 제1드럼(1) 사이에 끼워지고, 제2벨트(3b)는 하부와 중간 제2드럼(2c-2f)을 거쳐 제1드럼(1)에 끼워진다. 따라서 제1드럼(1)과 중간의 제2드럼(2c,2d)에는 제1벨트(3a)와 제2벨트(3b)가 같이 끼워져서 두 개의 벨트가 겹쳐서 회전하게 된다.The belt is composed of a first belt (3a) and a second belt (3b) is sandwiched between the first drum 1 and the second drum (2a-2f) is to rotate together with the rotation of the drum. The first belt 3a is sandwiched between the first drum 1 via the upper and middle second drums 2a-2d, and the second belt 3b is connected to the lower and middle second drums 2c-2f. It is fitted to the first drum (1). Accordingly, the first belt 3a and the second belt 3b are fitted together in the first drum 1 and the middle second drums 2c and 2d so that the two belts overlap and rotate.
벨트는 촘촘한 그물망을 사용하며 그물코를 통해 슬러지의 건조 과정에서 발생하는 수증기가 쉽게 증발할 수 있고, 슬러지가 벨트에서 미끄러져 이탈되지 않고 제1벨트(3a)와 제2벨트(3b) 사이에 끼워져서 드럼 주위를 회전할 수 있다. 벨트는 수분의 흡수가 가능하며 200℃까지 견딜 수 있어야 하고 수축이 ±5% 이내가 되어야 한다.The belt uses a dense mesh and can easily evaporate water vapor generated during the drying process of the sludge through the mesh. The belt is sandwiched between the first belt 3a and the second belt 3b without slipping off the belt. Can be rotated around the drum. The belt must be able to absorb moisture, be able to withstand temperatures up to 200 ° C and shrink within ± 5%.
슬러지는 제1벨트(3a)와 제2벨트(3b)의 사이로 투입되어 제1드럼(1)의 표면을 따라 회전하게 되며 스팀에 의해 가열된 제1드럼(1)의 표면에서 전달되는 열에 의해 건조된다. 슬러지 투입구 쪽에서는 중간 제2드럼(2d)과 하부 제2드럼(2f)은 평행한 상태로 설치되어 그 사이를 회전하는 제2벨트(3b) 위로 슬러지가 투입되며, 배출구 쪽에서는 하부 제2드럼(2e)이 중간 제2드럼(2c)보다 레벨이 낮게 설치되어 슬러지가 아래쪽으로 배출된다. 배출구 쪽에서는 제1벨트(3a)와 제2벨트(3b)의 표면에서 슬러지를 긁어내기 위한 두 개의 스크레이퍼(4)가 설치된다. 따라서, 투입구에서 투입된 슬러지는 제1벨트(3a)와 제2벨트(3b) 사이에 끼워져서 제1드럼(1)의 표면을 따라 회전하면서 건조되고 배출구에서 스크레이퍼(4)에 의해 긁혀져서 아래쪽으로 투하된다.The sludge is introduced between the first belt 3a and the second belt 3b to rotate along the surface of the first drum 1 and is transferred by the heat transferred from the surface of the first drum 1 heated by steam. To dry. At the sludge inlet side, the middle second drum 2d and the lower second drum 2f are installed in parallel and sludge is introduced onto the second belt 3b rotating therebetween, and at the outlet side, the lower second drum 2e is set at a lower level than the intermediate second drum 2c, and the sludge is discharged downward. On the outlet side, two scrapers 4 are provided for scraping off the sludge from the surface of the first belt 3a and the second belt 3b. Therefore, the sludge introduced from the inlet is sandwiched between the first belt 3a and the second belt 3b, dried while rotating along the surface of the first drum 1, and scraped downward by the scraper 4 at the outlet. It is dropped.
슬러지는 1차로 벨트식 탈수기에서 탈수가 된 후 본 발명의 슬러지 건조장치로 투입되며, 벨트식 탈수기는 본 발명의 슬러지 건조장치와 연동하여 가동된다.The sludge is first dewatered in the belt type dehydrator and then introduced into the sludge drying apparatus of the present invention, and the belt type dehydrator is operated in conjunction with the sludge drying apparatus of the present invention.
도 2는 본 발명의 슬러지 건조장치의 성능을 더욱 향상시키기 위하여 건조공기를 공급하기 위한 것으로 슬러지 건조장치에서 발생하는 공기를 외부로 배출시키지 않고 건조시켜 다시 순환시킴으로써 건조 효율의 향상은 물론 슬러지 건조과정에서 발생하는 냄새의 유출을 막을 수 있는 장점이 있다.Figure 2 is to supply the drying air in order to further improve the performance of the sludge drying apparatus of the present invention to improve the drying efficiency by drying and circulating again without discharging the air generated in the sludge drying apparatus to the outside as well as the sludge drying process There is an advantage that can prevent the outflow of odor generated from.
도2에 도시된 바와 같이 밀폐된 건조실(5)에 중간벽(6)을 설치하여 두 개의 방으로 분리하고, 한쪽 방에 본 발명의 슬러지 건조장치를 설치한다. 다른쪽 방은 중간에 수평벽(7)을 설치하되 수평벽(7)의 단부를 개방하여 공기가 자유로이 순환할 수 있도록 한다. 상기 중간벽(6)에는 상부에는 배기팬(8)이 하부에는 급기팬(9)이 각각 설치된다. 배기팬(8)의 앞쪽에는 냉동기(10)가 설치되며, 슬러지 건조장치에서 슬러지가 건조되면서 발생한 습한 공기가 냉각기(10)를 통과하면서 냉각되면서 수분을 잃게된다. 냉각기(10)를 거치면서 건조된 공기는 수평벽(7)을 한바퀴 돌아 아래쪽으로 이동하며 급기팬(9)의 앞쪽에 설치된 스팀 방열기(11)에 의해 다시 가열된다. 급기팬(9)으로 공기를 공급하기 전에 공기를 가열함으로써 슬러지 건조장치에서 슬러지의 건조 효율을 향상시킬 수 있다.As shown in FIG. 2, the intermediate wall 6 is installed in the sealed drying chamber 5 to be separated into two rooms, and the sludge drying apparatus of the present invention is installed in one room. The other room is provided with a horizontal wall (7) in the middle to open the end of the horizontal wall (7) so that air can be freely circulated. The middle wall 6 is provided with an exhaust fan 8 at the top and an air supply fan 9 at the bottom, respectively. The refrigerator 10 is installed in front of the exhaust fan 8, and the wet air generated as the sludge is dried in the sludge drying apparatus is cooled while passing through the cooler 10 to lose moisture. The air dried while passing through the cooler 10 is moved by the steam radiator 11 installed in front of the air supply fan 9 by moving the horizontal wall 7 downward. By heating the air before supplying air to the air supply fan 9, the sludge drying efficiency of the sludge drying apparatus can be improved.
본 발명은 스팀에 의해 가열된 드럼에 직접 슬러지가 접촉하면서 가열되므로 건조 효율이 우수하며, 드럼을 가열시키기 위한 스팀은 소각로나 기타 열원에서 발생하는 폐열을 이용할 수 있어 에너지 절약에 유리하다.The present invention is excellent in drying efficiency because the sludge is directly in contact with the drum heated by steam is heated, the steam for heating the drum can use the waste heat generated in the incinerator or other heat source is advantageous for energy saving.
또한, 종래의 슬러지 건조장치는 슬러지의 건조 과정에서 불쾌한 냄새가 발생하는 문제가 있었으나, 본 발명의 슬러지 건조장치는 폐쇄된 건조실에 슬러지 건조장치를 설치하고 건조과정에서 발생하는 습한 공기를 건조시켜 순환시킬 수 있도록 함으로써 악취가 외부로 누출되지 않는 장점이 있다. 또한, 슬러지 건조장치에 공기를 공급하기 전에 가열함으로써 건조 효율을 극대화시킬 수 있다.In addition, the conventional sludge drying apparatus has a problem that an unpleasant smell occurs in the drying process of the sludge, the sludge drying apparatus of the present invention is installed in a closed drying chamber, the sludge drying apparatus is installed and the wet air generated in the drying process to dry the circulation By making it possible, there is an advantage that odor does not leak to the outside. In addition, it is possible to maximize the drying efficiency by heating before supplying air to the sludge drying apparatus.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019990022026A KR20010002287A (en) | 1999-06-14 | 1999-06-14 | An apparatus and method for drying sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1019990022026A KR20010002287A (en) | 1999-06-14 | 1999-06-14 | An apparatus and method for drying sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
KR20010002287A true KR20010002287A (en) | 2001-01-15 |
Family
ID=19592045
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019990022026A KR20010002287A (en) | 1999-06-14 | 1999-06-14 | An apparatus and method for drying sludge |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR20010002287A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012021012A2 (en) * | 2010-08-13 | 2012-02-16 | 주식회사 에이케이인터내셔널 | Dehydration and drying device for handling waste water sludge |
CN110156296A (en) * | 2018-02-11 | 2019-08-23 | 北京市水利规划设计研究院 | Mud drying device and sludge drying method |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55109415A (en) * | 1979-02-15 | 1980-08-22 | Ebara Infilco Co Ltd | Sludge form matter dehydrating apparatus |
JPS57175439A (en) * | 1981-04-20 | 1982-10-28 | Hitachi Kiden Kogyo Ltd | Dehydration vehicle |
JPS58163499A (en) * | 1982-03-23 | 1983-09-28 | Nippon Furnace Kogyo Kaisha Ltd | Apparatus for heating and dehydrating sewage sludge |
JPS58183998A (en) * | 1982-04-21 | 1983-10-27 | Towa Kucho Kk | Method for drying sludge |
JPS59197399A (en) * | 1983-04-22 | 1984-11-08 | Toshio Sasaoka | Transfer type filtering dehydrating and drying machine |
JPS63149097A (en) * | 1986-12-12 | 1988-06-21 | Kawaguchi Seisakusho:Kk | Belt press type dehydrator |
KR19990074993A (en) * | 1998-03-17 | 1999-10-05 | 박광진 | Apparatus and method for treating sludge from sewage treatment plant |
-
1999
- 1999-06-14 KR KR1019990022026A patent/KR20010002287A/en not_active Application Discontinuation
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55109415A (en) * | 1979-02-15 | 1980-08-22 | Ebara Infilco Co Ltd | Sludge form matter dehydrating apparatus |
JPS57175439A (en) * | 1981-04-20 | 1982-10-28 | Hitachi Kiden Kogyo Ltd | Dehydration vehicle |
JPS58163499A (en) * | 1982-03-23 | 1983-09-28 | Nippon Furnace Kogyo Kaisha Ltd | Apparatus for heating and dehydrating sewage sludge |
JPS58183998A (en) * | 1982-04-21 | 1983-10-27 | Towa Kucho Kk | Method for drying sludge |
JPS59197399A (en) * | 1983-04-22 | 1984-11-08 | Toshio Sasaoka | Transfer type filtering dehydrating and drying machine |
JPS63149097A (en) * | 1986-12-12 | 1988-06-21 | Kawaguchi Seisakusho:Kk | Belt press type dehydrator |
KR19990074993A (en) * | 1998-03-17 | 1999-10-05 | 박광진 | Apparatus and method for treating sludge from sewage treatment plant |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012021012A2 (en) * | 2010-08-13 | 2012-02-16 | 주식회사 에이케이인터내셔널 | Dehydration and drying device for handling waste water sludge |
WO2012021012A3 (en) * | 2010-08-13 | 2012-05-10 | 주식회사 에이케이인터내셔널 | Dehydration and drying device for handling waste water sludge |
CN110156296A (en) * | 2018-02-11 | 2019-08-23 | 北京市水利规划设计研究院 | Mud drying device and sludge drying method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2020093256A (en) | Dehydrating device and dehydrating method | |
JP6639330B2 (en) | Dehydration system and dehydration method | |
JP2016107227A (en) | Sludge dehydration method and sludge dehydrator | |
CN110040934A (en) | A kind of sludge drying dehumidification system and method based on absorption heat pump | |
WO2013157427A1 (en) | Organic sludge and organic waste disposal device | |
CN210601633U (en) | Industrial waste treatment system | |
KR20010002287A (en) | An apparatus and method for drying sludge | |
KR20010109933A (en) | Sludge drier using wasting heat | |
JP3609636B2 (en) | Sludge drying equipment | |
KR20110044700A (en) | Sludge treating apparatus | |
CN212640266U (en) | Closed paddle stirring sludge drying system | |
CN212152053U (en) | Sludge electroosmosis deep dehydration coupling dehumidification drying device | |
CN211664944U (en) | Waste heat recovery drying system | |
KR100430073B1 (en) | A drying machine for waste water and sludge | |
KR100289436B1 (en) | High concentration wastewater treatment method | |
KR101843316B1 (en) | Combined Drying Apparatus for Sludge | |
KR102021731B1 (en) | Sludge Dehydration and Drying Equipment | |
JP2771445B2 (en) | Sludge treatment equipment | |
JPH06218397A (en) | Method and device for drying and firing sludge | |
CN211999432U (en) | Novel sludge drying and incineration device | |
CN214360958U (en) | Low-temperature sludge drying and burning combined device | |
KR102001847B1 (en) | Drying device for waste disposal | |
KR200185258Y1 (en) | A sludge drying machine of washing system for inductrial | |
KR200193163Y1 (en) | Double drum having heat exchanging spiral structure for drying sludge | |
KR20030072872A (en) | A method and apparatus for drying organic waste |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
E601 | Decision to refuse application |