KR0141359B1 - Organic garbage disposer - Google Patents
Organic garbage disposerInfo
- Publication number
- KR0141359B1 KR0141359B1 KR1019920025997A KR920025997A KR0141359B1 KR 0141359 B1 KR0141359 B1 KR 0141359B1 KR 1019920025997 A KR1019920025997 A KR 1019920025997A KR 920025997 A KR920025997 A KR 920025997A KR 0141359 B1 KR0141359 B1 KR 0141359B1
- Authority
- KR
- South Korea
- Prior art keywords
- fermentation tank
- organic waste
- fermentation
- mixing
- heat supply
- Prior art date
Links
- 239000010813 municipal solid waste Substances 0.000 title description 3
- 238000000855 fermentation Methods 0.000 claims abstract description 50
- 230000004151 fermentation Effects 0.000 claims abstract description 50
- 239000010815 organic waste Substances 0.000 claims abstract description 27
- 238000002156 mixing Methods 0.000 claims abstract description 11
- 238000002485 combustion reaction Methods 0.000 claims abstract description 8
- 239000003054 catalyst Substances 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- 239000003546 flue gas Substances 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000003912 environmental pollution Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- 239000002341 toxic gas Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- 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
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
- Treatment Of Sludge (AREA)
- Fertilizers (AREA)
Abstract
본 발명은 폐기물 처리장치에 관한 것으로 상부에 유기성 쓰레기를 투입하는 투입구와 하부에 배출구를 갖는 발효조와, 상기 발효조 내부에서 유기성 쓰레기를 섞어주는 혼합수단과, 상기 초고주파에 의해 발효조에 필요한 열을 공급하는 열공급수단과, 상기 발효조내에 발생된 유해가스를 촉매와 연소에 의해 외부로 배출하는 가스배출수단과, 상기 혼합수단, 열공급수단, 가스배출수단을 제어하는 제어수단을 포함하여 발효조내에 미생물균주에 의한 발효로 폐기물을 처리하는 유기성 폐기물 처리장치이다.The present invention relates to a waste treatment apparatus, and a fermentation tank having an inlet for injecting organic waste at an upper portion and an outlet at a lower portion thereof, a mixing means for mixing organic waste in the fermentation tank, and supplying heat required for the fermentation tank by the ultra-high frequency. A heat supply means, gas discharge means for discharging harmful gas generated in the fermentation tank to the outside by catalyst and combustion, and control means for controlling the mixing means, heat supply means, and gas discharge means, It is an organic waste treatment device that treats waste by fermentation.
Description
제 1도는 본 발명 유기성 폐기물 처리장치의 구성을 나타낸 종단면도.1 is a longitudinal sectional view showing the configuration of the organic waste treatment apparatus of the present invention.
제 2도는 본 발명 유기성 폐기물 처리장치의 우측면도.2 is a right side view of the organic waste treating apparatus of the present invention.
*도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings
10:발효조 12:투입구10: fermentation tank 12: inlet
15:배출구 22:축15: outlet 22: shaft
24:암 26:모터24: Arm 26: Motor
32:마그네트론 34:도파관32: magnetron 34: waveguide
36:급전구 40:연도36: Light bulb 40: Year
41:배기공 42,42':촉매41: exhaust hole 42, 42 ': catalyst
43:배기팬 45:연소실43: exhaust fan 45: combustion chamber
50:제어수단50: control means
본 발명은 폐기물 처리장치에 관한 것으로 특히 미생물 균주에 의한 발효로 폐기물을 처리하는 유기성 폐기물 처리장치에 관한 것이다.The present invention relates to a waste treatment apparatus, and more particularly, to an organic waste treatment apparatus for treating waste by fermentation by microbial strains.
근대산업의 발달과 급속한 인구증가로 인한 쓰레기 배출량의 증가는 심각한 환경오염요인으로 대두되어 왔다.Increasing waste emissions due to the development of modern industry and rapid population growth has been a serious environmental pollution factor.
특히 대도시에 집중된 인구로 수많은 쓰레기를 도시내에서 소화하지 못하여 외지까지 실어나르는 실정이었다.In particular, as a population concentrated in large cities, many garbage could not be digested in the city, and it was carried to the outside.
그중 전체쓰레기의 약 28%를 차지하는 음식물 쓰레기는 유기성 쓰레기로 부패하기 쉬운 성질을 가졌다.Food wastes, which account for about 28% of the total waste, are organic wastes.
이와같은 부패성 쓰레기는 심한 악취는 물론 수분함량이 높고 장마철이나 우천시 하수도를 통해 하천으로 흘러들어 물의 부영양화(負營養化)를 촉진시켜 물이 썩어가는 원인이 되어 왔다.Such decaying trash has a bad smell, high moisture content, flows into the river through the rainy season or rainy season sewage, and promotes eutrophication of water, causing water to decay.
또한, 이러한 쓰레기는 수거 및 운반처리가 까다로울뿐 아니라 소각처리하기 어려워 거의 매립하는 실정이었다.In addition, these wastes are difficult to collect and transport, as well as difficult to incinerate, so they are almost landfilled.
따라서, 부패성 쓰레기를 효율적으로 수거 처리하여 환경오염을 줄이고 자원화하는 방안이 촉구되는 실정이었다.Therefore, there is a need for a method of efficiently collecting and treating perishable waste to reduce environmental pollution and to resourceize it.
본 발명은 상기와 같은 문제점들을 해소하기 위한 것으로 부패하기 쉬운 유기성쓰레기를 이용하여 사료나 비료로 재활용할 수 있도록한 유기성 쓰레기 처리장치를 제공하는데 있다.The present invention is to solve the above problems to provide an organic waste disposal apparatus that can be recycled to feed or fertilizer using organic perishable organic waste.
상기 목적을 달성하기 위한 본 발명의 특징으로는 상부에 유기성 쓰레기를 투입하는 투입구와 하부에 발효된 이 쓰레기를 배출하는 배출구를 갖는 발효조와;Features of the present invention for achieving the above object is a fermentation tank having an inlet for injecting organic waste at the top and an outlet for discharging the waste fermented at the bottom;
상기 발효조 내부에서 유해성 쓰레기를 섞어주는 혼합수단과, 상기 발효조에 필요한 열을 제공하는 열공급수단과; 상기 혼합수단, 열공급수단, 가스배출수단을 제어하는 제어수단을 포함한다.Mixing means for mixing hazardous waste in the fermentation tank, and heat supply means for providing heat required for the fermentation tank; And control means for controlling the mixing means, heat supply means, and gas discharge means.
본 발명의 구성 및 작용효과를 첨부된 도면에 따라서 상세히 설명하면 다음과 같다.The configuration and effect of the present invention will be described in detail with reference to the accompanying drawings.
제 1도는 본 발명 유기성 폐기물 처리장치의 전체적구성을 나타낸 단면도이고 제 2도는 제 1도의 우측면도를 나타낸 것이다.1 is a cross-sectional view showing the overall configuration of the organic waste treatment apparatus of the present invention, and FIG. 2 is a right side view of FIG.
상부에 유기성 폐기물 투입구(12)와 하부에 배출구(15)를 갖는 발효조(10)를 형성한다.A fermentation tank 10 having an organic waste inlet 12 and an outlet 15 in the lower portion is formed.
상기 발효조(10) 내부에는 상기 유기성 폐기물을 섞어주는 날개(24a)를 포함하는 복수개의 암(24)이 상기 발효조(10)를 관통하는 모터(26)에 연결된 축(22)에 소정 간격과 회전각을 두고 고정된다.In the fermentation tank 10, a plurality of arms 24 including wings 24a for mixing the organic wastes are rotated at predetermined intervals and rotated on the shaft 22 connected to the motor 26 passing through the fermentation tank 10. It is fixed at an angle.
상기 발효조(10) 내부에 열공급수단으로 이 발효조(10) 일측에 고정된 마그네트론(32)과, 상기 마그네트론의 초고주파를 유도하는 도파관(34)과, 이 발효조 상부에 형성된 급전구(36)로 형성한다.The magnetron 32 fixed to one side of the fermentation tank 10 as a heat supply means in the fermentation tank 10, a waveguide 34 for inducing ultra-high frequency of the magnetron, and a feed hole 36 formed on the fermentation tank. do.
상기 발효조(10) 내부에서 발생되는 유독성 가스를 배출하기 위한 가스배출수단으로는 상기 발효조(10) 상부에 소정크기의 복수개의 배기공(41)을 형성하고, 이 배기공(41)에 연결된 연도(40)를 포함한다.As a gas discharge means for discharging the toxic gas generated in the fermentation tank 10, a plurality of exhaust holes 41 of a predetermined size are formed on the fermentation tank 10, and the flue is connected to the exhaust hole 41. And 40.
상기 연도(40)는 상부 일단에 고정된 배기팬(43)과, 상기 배기팬(43) 양측에 고정된 촉매(42,42 )와, 상기 촉매(42,42 ) 사이에 형성된 연소실(45)로 구성한다.The flue 40 includes an exhaust fan 43 fixed to an upper end, a catalyst 42 and 42 fixed to both sides of the exhaust fan 43, and a combustion chamber 45 formed between the catalysts 42 and 42. It consists of.
상기 연소실(45) 내부에는 유해가스를 태울 수 있도록 히터(46)와, 상기 연소실(45) 내부에 공기를 유입하기 위해 상기 마그네트론(32)을 식히는 냉각팬(47)에 연결된 덕트(48)로 구성한다.In the combustion chamber 45 to the duct 48 connected to the heater 46 and the cooling fan 47 to cool the magnetron 32 to introduce air into the combustion chamber 45 to burn harmful gas. Configure.
상기 혼합수단, 열공급수단, 가스배출수단은 상기 발효조(10) 내에 고정된 온도센서(54)와, 상기 연도(40)의 하부에 고정된 습도센서(52)에서 얻어진 정보를 통해 제어수단에 의해 제어된다.The mixing means, the heat supply means, and the gas discharge means are controlled by the control means through the information obtained from the temperature sensor 54 fixed in the fermentation tank 10 and the humidity sensor 52 fixed to the lower part of the flue 40. Controlled.
미설명부호 17은 공기흡입구이고 36a는 도파관(34) 내부로 유해가스의 유입을 막기 위한 급전구 덮개이다.Reference numeral 17 is an air inlet and 36a is a feeder cover for preventing the introduction of harmful gas into the waveguide 34.
상기와 같은 구성으로 된 본 발명의 작용효과를 보면 다음과 같다.Looking at the effect of the present invention having the configuration as described above are as follows.
먼저 투입구(12)의 뚜껑을 열어 발효조(10) 내부로 유기성 쓰레기를 투입하고 제어수단(50)에 의해 모터(26)와 마그네트론(32)을 가동한다.First, the organic waste is introduced into the fermentation tank 10 by opening the lid of the inlet 12, and the motor 26 and the magnetron 32 are operated by the control means 50.
상기 마그네트론(32)은 발효에 필요한 열을 공급하기 위해 상기 유기성 쓰레기내의 물분자를 진동시키기 위한 초고주파를 발생시킨다.The magnetron 32 generates very high frequency to vibrate the water molecules in the organic waste to supply heat required for fermentation.
마그네트론(32)에서 발생된 초고주파는 도파관(34)을 통해 유도되어 급전구(36)에 의해 발효조(10) 내부로 조사된다.The ultra-high frequency generated by the magnetron 32 is guided through the waveguide 34 and irradiated into the fermentation tank 10 by the feed port 36.
초고주파는 전자파의 특성상 발효조내부 공간에 전체적으로 골고루 퍼져 있게 되며, 발효조내부의 어느 지점에서나 이 초고주파에 노출되는 유기성 쓰레기의 물분자를 진동시킴으로써 열을 발생시켜 발효에 필요한 온도와 습도를 유지시켜 주는 역할을 한다.Ultra-high frequency spreads evenly throughout the fermentation tank due to the characteristics of electromagnetic waves, and generates heat by vibrating water molecules of organic wastes exposed to this microwave at any point in the fermentation tank to maintain temperature and humidity necessary for fermentation. do.
종래의 경우, 열을 공급하기 위해 히터를 열원으로 사용하기 때문에 복사열의 특성상 열의 세기는 열원인 히터를 중심으로 거리의 제곱에 반비례하여 약해지게 된다. 따라서 열원으로부터 가까운 곳은 온도가 충분히 가열되나 거리의 차이에 따라 가열되는 온도가 다르므로 열효율과 그에 따른 발효효율이 미비했으나, 본 발명에 의한 초고주파에 의해 열을 공급하면 이러한 문제점을 해결하게 되므로 열효율 및 발효효율이 상승되어 고속발효처리가 가능하게 된다.In the conventional case, since the heater is used as a heat source for supplying heat, the intensity of heat is weakened in inverse proportion to the square of the distance around the heater as the heat source. Therefore, the temperature close to the heat source is sufficiently heated, but the heating temperature is different according to the difference in distance, the thermal efficiency and the fermentation efficiency accordingly is insufficient, but supplying heat by the ultra-high frequency according to the present invention solves these problems, thermal efficiency And the fermentation efficiency is increased to enable a high speed fermentation treatment.
상기 초고주파를 받는 유기성 폐기물은 모터(26)의 구동에 따라 축(22)에 형성된 암(24)의 날개(24a)에 의해 골고루 섞이게 된다.The organic waste subjected to the ultra-high frequency is evenly mixed by the blades 24a of the arm 24 formed on the shaft 22 as the motor 26 is driven.
상기와 같이 반복되는 건조과정은 수분함유량이 75∼85% 정도에 이르던 유기성 폐기물이 습도센서(52)에 의해 감지되어 발효에 최적인 조건인 수분함유율 50∼60%에 이를때까지 계속된다.The repeated drying process as described above is continued until the organic waste having a water content of about 75 to 85% is detected by the humidity sensor 52 and reaches a water content of 50 to 60%, which is an optimal condition for fermentation.
상기 유기성 폐기물의 수분함유율이 50∼60%가 되도록 건조되면 상기 제어수단(50)에 의해 모터(26)나 마그네트론(32)의 동작이 중지되고 부저음이나 점등램프를 통해 미생물균주의 투여시기를 외부로 알리게 된다.When the organic waste is dried to have a water content of 50 to 60%, the operation of the motor 26 or the magnetron 32 is stopped by the control means 50, and the timing of administration of the microbial strain through the buzzer or the lamp is external. Will be announced.
이때 상기 투입구(12)를 열어 유기성 폐기물 처리량의 0.4%에 해당하는 미생물 균주를 발효조(10) 내부로 투입하고 전원을 인가하여 발효과정이 시작된다.At this time, by opening the inlet 12, the microbial strain corresponding to 0.4% of the organic waste treatment amount is introduced into the fermentation tank 10 and power is applied to start the fermentation process.
상기 제어수단(50)에 의해 모터(26)와 마그네트론(32)이 동작하게 되고 발효에 필요한 공기는 공기투입구(17)에 의해 유입된다.The motor 26 and the magnetron 32 are operated by the control means 50, and the air necessary for fermentation is introduced by the air inlet 17.
발효과정시 상기 발효조(10) 내부의 온도는 발효의 최적조건인 50∼60℃를 유지하도록 온도센서(54)에 의해 감지되어 제어수단(50)을 통해 마그네트론(32)의 출력을 조절한다.During the fermentation process, the temperature inside the fermenter 10 is sensed by the temperature sensor 54 to maintain 50-60 ° C., the optimum condition for fermentation, and adjusts the output of the magnetron 32 through the control means 50.
상기 건조과정과 발효과정을 거치는 동안 상기 발효조(10) 내부에서 발생되는 암모니아나 이산화탄소가 함유된 유해가스는 배기공(41)에 연결된 연도(40)내의 배기팬(43)에 의해 강제 배기된다.During the drying process and the fermentation process, harmful gas containing ammonia or carbon dioxide generated in the fermentation tank 10 is forcedly exhausted by the exhaust fan 43 in the flue 40 connected to the exhaust hole 41.
상기 연도(40)내를 통과하는 과정에서 유해가스는 1차로 촉매(42)를 통해 탈취되고 2차로 연소실(45)의 히터(46)에 의해 탈연.탈취된후 3차로 촉매(42 )를 통과하여 외부로 배출된다.In the course of passing through the flue 40, the noxious gas is first deodorized through the catalyst 42 and secondly desmoked and deodorized by the heater 46 of the combustion chamber 45, and then passes through the third catalyst 42. Is discharged to the outside.
상기와 같은 작용으로 상기 유기가스는 3차에 걸쳐 탈취되어 무해한 가스로 방출되게 된다.By the above action, the organic gas is deodorized over three times and released as a harmless gas.
이렇게 함으로써 종래의 경우 배기팬만 설치되어 재처리없이 유독성 가스를 대기중으로 배출함으로써 발생되던 대기오염의 문제점을 해결할 수 있게 된다.In this case, only the exhaust fan is installed in the related art, and thus it is possible to solve the problem of air pollution generated by releasing toxic gas into the atmosphere without reprocessing.
상기 발효과정은 상기 유기물 폐기물의 수분함유율이 20%에 이를때까지 계속 진행되며 습도센서(52)에서 얻어지는 정보에 의해 제어수단(50)이 모든 동작을 멈추어 공정이 완료된다.The fermentation process continues until the water content of the organic waste reaches 20%, and the control means 50 stops all operations by the information obtained from the humidity sensor 52, thereby completing the process.
상기 과정을 거쳐 발효 처리된 유기성 폐기물은 배출구(15)를 통해 꺼내어 가축의 사료나 비료, 퇴비로 사용하여 재활용 할 수 있다.The organic waste fermented through the above process can be taken out through the discharge port 15 and used as livestock feed, fertilizer, compost and recycled.
상기 발효과정은 유기성 폐기물의 종류에 따라 다소 시간의 차이는 있으나 보통 20∼40시간 정도이면 발효가 완료된다.The fermentation process is slightly different depending on the type of organic waste, but usually 20 to 40 hours to complete the fermentation.
상기와 같은 작용으로 본 발명은 병원, 식당, 군부대, 공장과 같은 집단 취사를 하는 장소는 물론 아파트단지와 같은 공공장소에 설치되어 사용할 수 있다.By the above operation, the present invention can be installed and used in a public place such as an apartment complex, as well as a place for group cooking such as a hospital, restaurant, military unit, and factory.
따라서, 본 발명은 폐기물을 수거하여 소각 폐기 매립시 발생되는 인력과 시간의 낭비와 환경오염을 줄이고 비공해 물질로 변환시켜 재활용함으로써 환경오염과 폐기물 양을 줄일 수 있고, 발효시 초고주파에 의한 가열로서 고속발효 처리가 가능하며, 발효시 발생되는 유해성 가스를 재처리하여 무해한 가스로 방출함으로 대기환경보호에 커다란 이점이 있다.Therefore, the present invention can reduce the environmental pollution and waste amount by collecting waste and reducing the waste of manpower and time and environmental pollution generated by incineration landfill, and converting and recycling to non-polluting materials, and as a heating by ultra-high frequency during fermentation High-speed fermentation is possible, and the harmful gas generated during fermentation is reprocessed and released as a harmless gas, which has a great advantage in protecting the atmosphere.
Claims (2)
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1019920025997A KR0141359B1 (en) | 1992-12-29 | 1992-12-29 | Organic garbage disposer |
| JP33791493A JP2601623B2 (en) | 1992-12-29 | 1993-12-28 | Waste treatment method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1019920025997A KR0141359B1 (en) | 1992-12-29 | 1992-12-29 | Organic garbage disposer |
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| Publication Number | Publication Date |
|---|---|
| KR940013634A KR940013634A (en) | 1994-07-15 |
| KR0141359B1 true KR0141359B1 (en) | 1998-06-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR1019920025997A KR0141359B1 (en) | 1992-12-29 | 1992-12-29 | Organic garbage disposer |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP2601623B2 (en) |
| KR (1) | KR0141359B1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100361089B1 (en) * | 1999-04-27 | 2002-11-18 | 닛폰 고칸 가부시키가이샤 | Method for disposing a waste |
| KR101224286B1 (en) * | 2012-03-19 | 2013-01-21 | 김경아 | Fermentation machine for fordder |
| KR101224252B1 (en) * | 2012-06-21 | 2013-01-22 | 김경아 | Fermentation machine for fordder |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08188491A (en) * | 1995-01-10 | 1996-07-23 | Nec Corp | Treatment of garbage and its apparatus |
| KR100521125B1 (en) * | 1997-11-28 | 2006-01-27 | 파로마 고교 가부시키 가이샤 | Food waste handler |
| KR100244389B1 (en) * | 1997-12-31 | 2000-02-01 | 구자홍 | Microwave garbage processor |
| KR100512100B1 (en) * | 1998-08-11 | 2005-11-24 | 엘지전자 주식회사 | Apparatus for disposing wet waste using microwave which has a mechanism for automatically removing disposed waste therefrom |
| JP4732708B2 (en) * | 2004-05-19 | 2011-07-27 | 樋野 明人 | Deodorization treatment method and deodorization treatment apparatus for used paper diaper fermentation treatment |
| JP5796855B2 (en) * | 2011-04-01 | 2015-10-21 | ジーエネックス株式会社 | Compost production system and compost production method |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52154775A (en) * | 1976-06-16 | 1977-12-22 | Fuji Kaki Kouji Kk | Apparatus for fermentating livestock manure |
| JPS62126337U (en) * | 1985-12-11 | 1987-08-11 | ||
| JPS62246892A (en) * | 1986-04-17 | 1987-10-28 | 鈴木 敏勝 | Manufacture of organic fertilizer |
| JPH02257833A (en) * | 1988-12-27 | 1990-10-18 | Kawasaki Steel Corp | Method for fermentation and apparatus therefor |
-
1992
- 1992-12-29 KR KR1019920025997A patent/KR0141359B1/en not_active IP Right Cessation
-
1993
- 1993-12-28 JP JP33791493A patent/JP2601623B2/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100361089B1 (en) * | 1999-04-27 | 2002-11-18 | 닛폰 고칸 가부시키가이샤 | Method for disposing a waste |
| KR101224286B1 (en) * | 2012-03-19 | 2013-01-21 | 김경아 | Fermentation machine for fordder |
| KR101224252B1 (en) * | 2012-06-21 | 2013-01-22 | 김경아 | Fermentation machine for fordder |
Also Published As
| Publication number | Publication date |
|---|---|
| KR940013634A (en) | 1994-07-15 |
| JPH06256080A (en) | 1994-09-13 |
| JP2601623B2 (en) | 1997-04-16 |
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