KR20100026079A - The method of manufacturing the high purity bio-diegel fuel with rancid oil - Google Patents
The method of manufacturing the high purity bio-diegel fuel with rancid oil Download PDFInfo
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- KR20100026079A KR20100026079A KR1020080084924A KR20080084924A KR20100026079A KR 20100026079 A KR20100026079 A KR 20100026079A KR 1020080084924 A KR1020080084924 A KR 1020080084924A KR 20080084924 A KR20080084924 A KR 20080084924A KR 20100026079 A KR20100026079 A KR 20100026079A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/42—Catalytic treatment
- C10G3/44—Catalytic treatment characterised by the catalyst used
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G7/00—Distillation of hydrocarbon oils
- C10G7/006—Distillation of hydrocarbon oils of waste oils other than lubricating oils, e.g. PCB's containing oils
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/003—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- 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
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Fats And Perfumes (AREA)
Abstract
Description
폐식용유를 원료로 하여 메탄올과 알카리촉매를 동시에 첨가하여 반응한 후 글리세린층 분리공정을 거친 다음 알콜을 제거하여 물로 세정 탈수하여 바이오디젤을 제조생산에 관한 것이다.Waste oil is used as a raw material, and methanol and alkali catalysts are added at the same time to react, and then the glycerin layer separation process is performed.
석유자원 고갈에 대한 위기가 고조됨에 따라 대체연료의 개발에 대한 관심이 높아지고 있다 바이오 디젤은 환경친화형이고 자원의 고갈 문제가 없다는 장점이 있다 또한 기존 차량에 직접 사용이 가능하고 현재 설치된 주유소에서 공급가능하므로 인프라 시설이 필요 없다. 식물성 기름의 에스테르화 반응에 의해 생산 가능한 바이오디젤은 경유에 비해 환경 오염 물질의 배출이 월등히 낮아 EU와 미국등 에서는 1990년대 초부터 실용화하여 차량연료로 사용하고 있다. 현재 바이오디젤은 유지작물로부터 축출한 식용유를 원료로 생산하고 있으며 그 결과 바이오 지젤의 총 생산비의 약 70%이상이 원료비 이다. 따라서 바이오디젤의 생산단가를 낮추기 위해서는 보다 값싼 원료의 확보가 필요하다 특히 국내에서는 식용유 생산이 거의 없다는 점을 고려할 때 바이오 디젤을 생산하기 위해서는 석유와 마찬가지로 원료를 해외 자원에 의존해야 한다는 문제점이 있다. 이러한 문제점을 해결할 수 있는 방안으로 국내에서 배출되는 폐식용유를 바이오 디젤 원료로서 활용은 매우 중요하다. 폐식용유의 필요성에 비해 종래의 기술은 유지식물로부터 추출한 식용유와 달리 다양한 불순물이 포함되어 있으며 그 결과 바이오디젤 생산시 품질을 떨어뜨리는 직접적인 원인이 된다. 여러 특허와 논문이 발표되고 있으나 기존의 제조방법은 낮은 생산수율, 낮은 순도 ,필터 막힘점 및 유동점이 높아 품질규격에 못미치는 바이오디젤을 생산하는 단점이 있다.There is a growing interest in developing alternative fuels as the crisis of oil resource depletion rises. Biodiesel has the advantages of being environmentally friendly and free of resources depletion. It can also be used directly on existing vehicles and supplied at currently installed gas stations. It does not require infrastructure. Biodiesel produced by esterification of vegetable oil has much lower environmental pollutants than diesel, and has been used as a vehicle fuel in the EU and US since the early 1990s. Biodiesel currently produces edible oil extracted from oil crops as a raw material. As a result, more than 70% of the total production cost of biodiesel is raw material. Therefore, in order to lower the production cost of biodiesel, it is necessary to secure cheaper raw materials. In particular, considering that there is little cooking oil production in Korea, there is a problem in that raw materials, like petroleum, have to depend on overseas resources for raw materials. In order to solve this problem, it is very important to utilize waste cooking oil discharged from Korea as a biodiesel raw material. Compared to the need for waste cooking oil, the conventional technology includes various impurities, unlike cooking oil extracted from oil and fat, which is a direct cause of deterioration in biodiesel production. Although several patents and papers have been published, the existing manufacturing method has the disadvantage of producing biodiesel that is less than the quality standard due to low production yield, low purity, filter plugging point and pour point.
기존의 폐식용유로 이용한 제조방법의 생산수율을 높이며 기존 단점으로 부각된 바이오디젤의 후처리 공정의 폐수가 발생하지 않음으로 처리비용감소및 공해를 방지하며 바이오디젤에 함유된 불순물로 인해 품질 규격 미만 및 폐식용유의 단점인 필터막힘점및 유동점을 2차증류 공정으로 인해 99%이상의 고순도 바이오 디젤 제조생산하는데 목적이 있다.Increases the production yield of conventional waste cooking oil and prevents wastewater in the post-treatment process of biodiesel, which has been highlighted as a disadvantage, prevents reduction of processing costs and pollution, and is less than quality standards due to impurities contained in biodiesel. And the filter plugging point and the pour point, which are disadvantages of the waste cooking oil, are aimed at producing 99% or more of high purity biodiesel due to the secondary distillation process.
1. 공지기술에 의해 제조된 고순도 바이오디젤은 폐식용유를 원료로 사용한 바이오디젤보다 고순도(지방산메칠 에스테르함량 99%) 이며 유동점을 낮추는 이점이있다.1. The high purity biodiesel manufactured by the known technology has higher purity (99% fatty acid methyl ester content) and lower pour point than biodiesel using waste cooking oil as a raw material.
2. 조 바이오디젤을 수세 없이 불순물및 염기를 제거하여 환경친화적이고 환경오염을 방지한다.2. Crude biodiesel is environmentally friendly and prevents environmental pollution by removing impurities and bases without washing with water.
3. 폐식용유를 이용하여 원가절감과 폐기물 처리및 청정대체연료를 생산함으로써 경제적 파급 효과를 가져오고 증류부산물을 보일러 연료로 사용하여 제조공정 비용을 절감한다.3. Cost reduction, waste treatment and clean alternative fuel are produced using waste cooking oil to bring economic ripple effect, and distillation by-product is used as boiler fuel to reduce manufacturing process cost.
본 발명을 첨부된 도면을 참조하여 상세히 설명하면 다음과 같다Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
도1 은 폐식용유를 이용한 바이오디젤 제조 공정으로써 폐식용유 투입시 필터링하여 (1) 호퍼용 침전조및온도 예열기에 투입하여 원료온도를 80~90℃로 맞추 어 (2) 반응기에 60torr진공상태에서 원료를 투입하여 폐식용유에 포함된 수분을 완전 건조한다. (3)의 촉매탱크(소듐 메톡사이드(원료대비 0.9~1%)+메탄올)에서 원료대비 1:9 몰비로 반응조에 투입시킨다. (2)반응조에서 75~80℃ 온도에서 약 45~60분 정도 반응시키면서 속도를 최대 150rpm으로 회전시키며 순환펌프를 이용하여 반응을 촉진시킨다. 반응이 끝난 제품을(4) 침전조에 이송한 다음 1~2시간정도 침전한 후 1차 글리세린및 불순물를 자연침전으로 제거하고 (5) 원심분리기를 통해 2차 글리세린 및 불순물을 제거한다. (5)를 통해 이송된 조 바이오디젤을 1차 증류기로 이송하여 내부에 포함된 메탄올을 65~75℃에서 진공 60torr로 메탄올을 증류하여 저장탱크로 이송하여 재이용된다.(6)에서 조바이오디젤의 염기 및 불순물을 제거하기위해 산성백토를 1~2%를 첨가하여 온도 80~90℃에서 진공상태에서 20분간 150rpm으로 회전한다. 필터링을 거쳐 2차 불순물을 제거 한 다음 (8)2차 증류기에 투입된다 증류온도는 200~240℃ 진동도 10~30torr정도 설정하여 무색의 고순도 바이오디젤을 생산한다 (9) 5~7% 정도의 증류잔유물이 나오는데 보일러 연료로 사용할 수 있어 제조비용을 절감 할 수 있다.1 is a biodiesel manufacturing process using waste cooking oil, which is filtered during the input of waste cooking oil (1) into a hopper settling tank and a temperature preheater to adjust the raw material temperature to 80 to 90 ° C (2) a raw material in a 60torr vacuum state in a reactor Dry the water contained in the waste cooking oil by adding. In the catalyst tank of (3) (sodium methoxide (0.9 ~ 1% of the raw material) + methanol) is added to the reaction tank in a 1: 9 molar ratio of the raw material. (2) Rotate the speed up to 150rpm while reacting for about 45 ~ 60 minutes at 75 ~ 80 ℃ temperature in the reactor and promote the reaction by using circulation pump. After completion of the reaction, the product (4) is transferred to the settling tank and settled for 1 ~ 2 hours, and then the primary glycerin and impurities are removed by natural precipitation, and (5) the secondary glycerin and impurities are removed through a centrifuge. The crude biodiesel transferred through (5) is transferred to the first still, and the methanol contained therein is distilled into methanol by distilling methanol into a storage tank at 60 to 60 ° C at 65 to 75 ° C. The crude biodiesel is reused in (6). To remove the base and impurities, add 1 ~ 2% of acid clay and rotate at 150rpm for 20 minutes in vacuum at 80 ~ 90 ℃. After filtering, the secondary impurities are removed and then (8) input to the secondary distiller. Distillation temperature is set at 200 ~ 240 ℃ vibration and 10 ~ 30torr to produce colorless high purity biodiesel (9) about 5 ~ 7% The distillation residues of can be used as boiler fuel can reduce the manufacturing cost.
도1 폐식용유을 원료로하여 바이오디젤 제조공정 도면1 is a biodiesel manufacturing process drawing from waste edible oil as raw material
도2 2차증류과정으로 유동점 및 순도 향상 도표Figure 2 Pour point and purity improvement chart by the second distillation process
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102154058A (en) * | 2011-03-11 | 2011-08-17 | 江苏恒顺达生物能源有限公司 | Process for carrying out pretreatment on waste oil |
KR20160097875A (en) * | 2015-02-10 | 2016-08-18 | 주식회사 오일텍 | Apparatus and method for refinning waste oil |
KR20160097876A (en) * | 2015-02-10 | 2016-08-18 | 주식회사 오일텍 | Apparatus for refinning waste oil |
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- 2008-08-29 KR KR1020080084924A patent/KR20100026079A/en not_active Application Discontinuation
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102154058A (en) * | 2011-03-11 | 2011-08-17 | 江苏恒顺达生物能源有限公司 | Process for carrying out pretreatment on waste oil |
KR20160097875A (en) * | 2015-02-10 | 2016-08-18 | 주식회사 오일텍 | Apparatus and method for refinning waste oil |
KR20160097876A (en) * | 2015-02-10 | 2016-08-18 | 주식회사 오일텍 | Apparatus for refinning waste oil |
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