KR101272171B1 - Heavy oil emulsifier and method for preparing emulsified heavy oil - Google Patents

Heavy oil emulsifier and method for preparing emulsified heavy oil Download PDF

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KR101272171B1
KR101272171B1 KR1020100040183A KR20100040183A KR101272171B1 KR 101272171 B1 KR101272171 B1 KR 101272171B1 KR 1020100040183 A KR1020100040183 A KR 1020100040183A KR 20100040183 A KR20100040183 A KR 20100040183A KR 101272171 B1 KR101272171 B1 KR 101272171B1
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heavy oil
alcohol
water
oil
ethoxylate
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KR1020100040183A
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KR20110120671A (en
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김문찬
이경희
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이엔에프씨 주식회사
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/195Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/196Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/026Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/14Function and purpose of a components of a fuel or the composition as a whole for improving storage or transport of the fuel
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2250/00Structural features of fuel components or fuel compositions, either in solid, liquid or gaseous state
    • C10L2250/08Emulsion details
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/34Applying ultrasonic energy

Abstract

본 발명은 유화제 성분으로 폴리옥시에틸렌 알코올 중에서 선택된 하나 이상의 화합물(A)과 알킬폴리에틸렌 폴리프로필렌 블록공중합 물질중에서 선택된 하나 이상의 화합물(B)를 1 : 100 ∼ 100 : 1 의 중량비율로 혼합하여 유화제로 사용하는 것을 특징으로 한다. 폴리옥시에틸렌 알코올에서 알코올 성분으로는 노닐페놀에톡시레이트, 옥틸페놀에톡시레이트, 라우릴알코올에톡시레이트, 세틸알코올에톡시레이트, 올레일알코올에톡시레이트, 스테아릴알코올에톡시레이트, 트리데실알코올에톡시레이트, 소르비탄에스테르 등이 있다. 알킬폴리에틸렌 폴리프로필렌 블록공중합 물질에서 알킬성분으로는 노닐페놀, 라우릴알코올, 글리세롤스테아레이트, 브랜치드데실알코올등이 있다. 이렇게 제조된 유화제를 A중유 또는 B중유 또는 C중유 또는 원유와 물이 중량비로 1 ∼ 60%로 혼합된 연료에 중량비로 0.01% ∼ 15%를 첨가하고 기계적인 유화 또는 초음파를 사용하여 유화시켜 물의 입경이 0.1 ∼ 20㎛로 되도록 세절화시켜 물 주위에 A중유, B중유, 또는 C중유가 감싸게 유화시키거나, 원유의 입경이 1 ∼ 1,000㎛로 되도록 하여 원유 주위를 물로 둘러싸게 만들어 지는 것을 특징으로 한다. 이러한 유화제를 초음파나 기계적으로 유화시켜 유화된 중질유 연료를 제조하여, 엔진 내부에서 연소시 중질유 내부에 미세 입자화된 물이 미세폭발을 함으로써 완전연소에 가깝게 만들어줌으로써 배출되는 질소산화물과 매연을 감소시켜주어 대기환경 개선에 크게 기여하며 물을 사용하는 대체연료로서 온실가스인 이산화탄소 배출 저감에 기여하는 특징이 있다.In the present invention, at least one compound (A) selected from polyoxyethylene alcohol and at least one compound (B) selected from alkylpolyethylene polypropylene block copolymer materials as an emulsifier component are mixed at a weight ratio of 1: 100 to 100: 1 to form an emulsifier. It is characterized by using. Alcohol components in polyoxyethylene alcohol include nonylphenol ethoxylate, octylphenol ethoxylate, lauryl alcohol ethoxylate, cetyl alcohol ethoxylate, oleyl alcohol ethoxylate, stearyl alcohol ethoxylate, tridecyl Alcohol ethoxylate, sorbitan ester, and the like. Alkyl polyethylene polypropylene block copolymer The alkyl component in the nonyl phenol, lauryl alcohol, glycerol stearate, branched decyl alcohol and the like. The emulsifier thus prepared is added to 0.01% to 15% by weight in a fuel in which A heavy oil or B heavy oil or C heavy oil or crude oil and water are mixed at a weight ratio of 1 to 60% by weight, and emulsified by mechanical emulsification or ultrasonic wave. It is emulsified to have a particle diameter of 0.1 to 20 μm to emulsify A heavy oil, B heavy oil, or C heavy oil around the water, or to make the particle diameter of the crude oil 1 to 1,000 μm to surround the crude oil with water. It is done. Ultrasonic or mechanical emulsification of these emulsifiers to produce emulsified heavy oil fuel, and when the combustion inside the engine finely exploded in the fine oil inside the heavy oil to make it close to the complete combustion by reducing the nitrogen oxides and soot emissions As a result, it greatly contributes to the improvement of the atmospheric environment, and has the characteristics of contributing to the reduction of carbon dioxide emission which is a greenhouse gas as an alternative fuel using water.

Description

중질유 유화제 및 유화중질유의 제조방법 {HEAVY OIL EMULSIFIER AND METHOD FOR PREPARING EMULSIFIED HEAVY OIL}Heavy oil emulsifier and manufacturing method of emulsified heavy oil {HEAVY OIL EMULSIFIER AND METHOD FOR PREPARING EMULSIFIED HEAVY OIL}

본 발명은 A중유, B중유, C중유, 원유 등의 중질유분을 물과 기계적 또는 초음파를 사용하여 혼합하여 유화연료를 만들어 이송을 원활하게 하고, 연소시 대기오염물질인 검뎅(soot)과 질소산화물을 줄여서 대기환경을 개선하고자 하며, 또한 원유와 물을 에멀젼화시켜 이송시 점도를 낮추어 이송을 원활하게 하여 에너지를 절약하며, 물을 혼합한 만큼 중질유의 소비를 감소시켜 에너지를 절약하는 방법에 관한 것이다.In the present invention, heavy oils such as A heavy oil, B heavy oil, C heavy oil, crude oil, etc. are mixed with water and mechanical or ultrasonic to make an emulsion fuel to smoothly transport, soot and nitrogen, which are air pollutants during combustion. In order to improve the atmospheric environment by reducing oxides, and to emulsify crude oil and water to reduce the viscosity during transportation, it is possible to save energy by facilitating the transfer, and to save energy by reducing the consumption of heavy oil by mixing water. It is about.

압축점화 디젤기관은 가솔린 엔진에 비해 희박연소를 한다는 특성으로 인해 질소산화물(NOx)과 입자상물질의 배출량이 많으며 이는 심각한 도시공해의 주범으로 지적되고 있다. 질소산화물은 태양광선에 의해 광화학반응을 일으켜 오존발생을 야기하여 호흡기질환 등을 유발하며, 미세먼지는 입자의 크기가 10㎛ 이하의 작은 먼지로서 호흡기에 쉽게 침투하여 폐에 흡착됨으로써 기관지 영향과 폐암을 유발하는 것으로 알려지고 있다. 특히 우리나라 대도시지역 특성상 인구가 밀집되어 있고, 차량정체 시간이 길며, 도로주변과 거주지역의 이격거리가 짧고, 대형버스 및 트럭 등 경유 차량의 운행이 빈번하여 시민들이 느끼는 체감 오염도는 더욱 높아 대책이 시급한 실정이다.Compressive ignition diesel engines emit more nitrous oxide (NOx) and particulate matter due to their lean burning characteristics than gasoline engines. Nitrogen oxides cause photochemical reactions by sunlight to cause ozone, causing respiratory diseases, etc. Fine dust is small particles with a particle size of 10 ㎛ or less that easily penetrates into the respiratory tract and is adsorbed into the lungs. It is known to cause. In particular, due to the characteristics of Korea's metropolitan areas, populations are concentrated, traffic jams are long, distances between roads and residential areas are short, and the operation of diesel vehicles such as large buses and trucks is frequent. It is urgent.

저 NOx화 기술로는 연료의 전처리 및 연소설비를 개선하는 전처리 방법으로서 연료분사시기 지연, 연소실 형상 개조, 연료분사계 개선, 배기재순환(EGR), 물 분사법, 디젤유-물의 유화(emulsion) 연료사용 등과 배출가스 중에 포함된 NOx를 제거하는 후처리 방법으로서 촉매분해, 촉매환원, 흡수, 흡착 등을 들 수 있다.The low NOx technology includes pretreatment methods to improve fuel pretreatment and combustion equipment. Fuel injection timing delay, combustion chamber shape modification, fuel injection system improvement, exhaust recirculation (EGR), water injection method, diesel oil-water emulsion Examples of post-treatment methods for removing NOx contained in fuel use and exhaust gas include catalytic decomposition, catalytic reduction, absorption, and adsorption.

이중 물을 액체연료와 함께 유화상태로 사용하는 방법은 열효율을 거의 저하시키지 않고도 NOx, particulate, CO 및 HC를 동시에 저감시킬 수 있는 기술로 최근 새롭게 주목 받고 있다. 이와 같은 효과가 생기는 주요 요인으로서 물 첨가에 의한 화염온도의 저하, 물의 급격한 증발에 의한 화염온도의 저하, 물의 급격한 증발에 의한 유적의 마이크로폭발, 분무관통력의 증가에 따른 주위공기 혼입량 증대 등이 고려될 수 있다.The use of water together with liquid fuel in an emulsified state has recently attracted new attention as a technology that can simultaneously reduce NOx, particulates, CO, and HC without substantially reducing thermal efficiency. The main factors that contribute to this effect include lowering the flame temperature by adding water, lowering the flame temperature by the rapid evaporation of water, microexplosion of oil droplets due to the rapid evaporation of water, and increasing the amount of ambient air due to the increase in spray penetration. Can be.

또한, 원유를 이송할때에 높은 점도로 인하여 많은 에너지 손실을 가져오게 되는데, 물과 에멀젼화시킴으로 인하여 이송을 간편하게 하여 에너지를 줄일 수 있다.In addition, the high viscosity when transferring the crude oil brings a lot of energy loss, it is possible to reduce the energy by simplifying the transfer by emulsifying with water.

한편, 선박의 경우 2016년에 Tier3가 발효되면 현재에 비해 약 80% 이상의 NOx를 줄여야 하는데 여기에 대한 해결방법으로도 중질유의 에멀젼 연료화가 대두되고 있다.On the other hand, ships are expected to reduce NOx by more than 80% when Tier 3 takes effect in 2016. As a solution to this, emulsion fuel of heavy oil is emerging.

본 발명은 종래의 에멀젼 기술로는 시간이 경과함에 따라 에멀젼의 분산상태가 오래 지속되지 못하고 물입자 끼리 재결합하여 물입자의 결정 성장으로 유수분리 현상이 일어나 연료로서 사용이 불가능한 것을 유화제를 사용하여 초음파나 기계적인 방법으로 유화시켜 물과 A중유, B중유, C중유, 원유등 중질유분과 에멀젼연료로 만들어 유수분리 현상이 일어나지 않는 안정한 상태의 연료를 제공함을 목적으로 하며 또한 이와같은 에멀젼 연료를 사용하여 대기오염물질인 검뎅(soot)이나 질소산화물을 줄여 대기오염을 개선하는 방법을 제공하는데 그 목적이 있다.According to the present invention, the emulsion state does not last long with the conventional emulsion technology and the water particles are recombined with each other and the oil and water separation phenomenon occurs due to the crystal growth of the water particles. B. Emulsify by mechanical method and make heavy oil and emulsion fuel such as water, A heavy oil, B heavy oil, C heavy oil and crude oil to provide stable fuel without oil and water separation. The purpose of the present invention is to provide a method for improving air pollution by reducing soot or nitrogen oxide, an air pollutant.

본 발명은 유화제 성분으로 폴리옥시에틸렌 알코올중에서 선택된 하나 이상의 화합물(A)과 알킬폴리에틸렌 폴리프로필렌 블록공중합 물질중에서 선택된 하나 이상의 화합물(B)를 A : B = 1 : 100 ∼ 100 : 1 의 중량비율로 혼합하여 유화제로 사용하는 것을 특징으로 한다. 화합물A 또는 화합물B가 2종 이상일때에는 화합물A의 합과 화합물B의 합의 비가 1 : 100 ∼ 100 : 1 의 중량비율이 되도록 혼합한다. 폴리옥시에틸렌 알코올에서 폴리옥시에틸렌의 반복단위(중합도)는 1∼30인 것을 특징으로 하며, 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위(중합도)는 1∼30인 것을 특징으로 한다. 그리고, 폴리옥시에틸렌 알코올에서 알코올 성분으로는 노닐페놀에톡시레이트, 옥틸페놀에톡시레이트, 라우릴알코올에톡시레이트, 세틸알코올에톡시레이트, 올레일알코올에톡시레이트, 스테아릴알코올에톡시레이트, 트리데실알코올에톡시레이트, 소르비탄에스테르등이 있다. 알킬폴리에틸렌 폴리프로필렌 블록공중합 물질에서 알킬성분으로는 노닐페놀, 라우릴알코올, 글리세롤스테아레이트, 브랜치드데실알코올 등이 있다.In the present invention, at least one compound (A) selected from polyoxyethylene alcohol and at least one compound (B) selected from alkylpolyethylene polypropylene block copolymer materials as an emulsifier component is used in a weight ratio of A: B = 1: 1-100-100: 1. It is characterized by being used as an emulsifier by mixing. When compound A or compound B is 2 or more types, it mixes so that the ratio of the sum of compound A and the sum of compound B may be a weight ratio of 1: 100-100: 1. The polyoxyethylene alcohol is characterized in that the repeating unit (polymerization degree) of polyoxyethylene is 1 to 30, and the repeating unit (polymerization degree) of the alkylpolyethylene polypropylene block copolymer is characterized in that 1 to 30. In the polyoxyethylene alcohol, alcohol components include nonylphenol ethoxylate, octylphenol ethoxylate, lauryl alcohol ethoxylate, cetyl alcohol ethoxylate, oleyl alcohol ethoxylate, stearyl alcohol ethoxylate, Tridecyl alcohol ethoxylate, sorbitan ester, and the like. The alkyl component in the alkyl polyethylene polypropylene block copolymer is nonylphenol, lauryl alcohol, glycerol stearate, branched decyl alcohol, and the like.

이렇게 제조된 유화제를 A중유 또는 B중유 또는 C중유 또는 원유와 물이 중량비로 1 ∼ 60%로 혼합된 연료에 중량비로 0.01% ∼ 15%를 첨가하고 기계적인 유화 또는 초음파를 사용하여 유화시켜 물의 입경이 0.1 ∼ 20㎛로 되도록 세절화시켜 물 주위에 A중유, B중유, 또는 C중유가 감싸게 유화시키거나, 원유의 입경이 1 ∼ 1,000㎛로 되도록 하여 원유 주위를 물로 둘러싸게 만들어 지는 것을 특징으로 한다. 첨가되는 유화제의 양이 0.01%보다 작으면 유화가 잘 안 일어나며, 15%보다 크게 되면 경제성이 없어지며 A중유, B중유, C중유, 원유의 물성에 영향을 가져오게 된다. 초음파를 사용할 때에는 진폭이 5 ∼ 200㎛로 하며 5㎛보다 진폭이 작으면 유화가 안 일어나며, 200㎛보다 클경우에는 너무 강한 에너지가 주입되어 기화가 일어나 오히려 유화에 방해가 되는 특징이 있다.The emulsifier thus prepared is added to 0.01% to 15% by weight in a fuel in which A heavy oil or B heavy oil or C heavy oil or crude oil and water are mixed at a weight ratio of 1 to 60% by weight, and emulsified by mechanical emulsification or ultrasonic wave. It is emulsified to have a particle diameter of 0.1 to 20 μm to emulsify A heavy oil, B heavy oil, or C heavy oil around the water, or to make the particle diameter of the crude oil 1 to 1,000 μm to surround the crude oil with water. It is done. If the amount of added emulsifier is less than 0.01%, emulsification does not occur well, and if it is larger than 15%, the economic efficiency is lost, and the properties of A heavy oil, B heavy oil, C heavy oil, and crude oil are affected. When using ultrasonic waves, the amplitude is 5 to 200 μm, and when the amplitude is smaller than 5 μm, emulsification does not occur. When it is larger than 200 μm, too strong energy is injected to vaporize the oil, which is rather hindering the emulsification.

본 발명은 여름철 높은 저장온도에서도 물과 A중유 또는 B중유 또는 C중유 또는 원유와의 상분리 문제가 없어서 사용할 수가 있으며, 또한 장기간 저장에서도 물과 A중유, B중유, C중유, 원유와의 상분리 문제를 완전히 극복할 수가 있다. 또한 A중유 또는 B중유 또는 C중유의 경우 물 주위를 A중유 또는 B중유 또는 C중유등의 중질유를 감싸고 있어서 연료탱크, 연료공급 시스템의 부식문제가 없으며, 디젤엔진이나 선박용엔진 또는 보일러 내부에서 연소시 A중유 또는 B중유 또는 C중유 내부에 미세 입자화된 물이 미세폭발을 함으로써 완전연소에 가깝게 만들어줌으로써 배출되는 일산화탄소와 탄화수소를 감소시켜주어 대기환경 개선에 크게 기여하며 대체연료로서 온실가스인 이산화탄소 배출 저감에 기여한다. 원유의 경우 원유주위를 물이 둘러싸고 있어서 점도를 낮추어 이송시 에너지를 절감하게 된다.The present invention can be used because the phase separation of water and A heavy oil or B heavy oil or C heavy oil or crude oil even at high storage temperature in summer, and also the phase separation problem of water and A heavy oil, B heavy oil, C heavy oil, crude oil even in long-term storage Can be overcome completely. Also, in case of A heavy oil, B heavy oil or C heavy oil, the heavy oil such as A heavy oil, B heavy oil or C heavy oil is wrapped around the water, so there is no corrosion problem of fuel tank, fuel supply system, and combustion in diesel engine, marine engine or boiler. The fine-grained water inside A heavy oil, B heavy oil, or C heavy oil makes explosives close to complete combustion, reducing carbon monoxide and hydrocarbons and contributing to the improvement of the atmospheric environment. Contribute to emission reduction In the case of crude oil, water is surrounded by crude oil, which reduces the viscosity and saves energy during transportation.

본 발명을 배출가스 저감인 실시예와 비교예를 들어 상세히 설명하면 다음과 같다. 하지만 이러한 실시예에 의하여 본 발명의 권리 범위가 한정되는 것은 아니며, 해당 기술분야의 당업자는 하기의 특허 청구의 범위에 기재된 본 발명의 사상 및 영역으로 부터 벗어나지 않는 범위내에서 본 발명을 다양하게 수정 및 변경시킬수 있음을 이해할 수 있을 것이다.Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples, which are emission reductions. However, the scope of the present invention is not limited by these embodiments, and those skilled in the art can variously modify the present invention without departing from the spirit and scope of the present invention as set forth in the claims below. And can be changed.

실시예들과 비교예들로부터 제조된 A중유 또는 B중유 또는 C중유, 원유를 메스실린더에 200㎖를 넣고, 80℃ 온도의 항온수조에 12시간동안 넣어 시간의 경과에 따른 상분리 되는 정도를 관찰하여 표1에 나타내었다. 상분리 정도는 간편하면서도 예민한 "Volumetric method"를 이용하여 다음 식과 같이 유화 안정지수(Emulsion Stability Index: ESI)를 계산하였다.200 ml of A heavy oil or B heavy oil or C heavy oil and crude oil prepared from Examples and Comparative Examples were put in a measuring cylinder, and placed in a constant temperature water bath at 80 ° C. for 12 hours to observe the degree of phase separation. It is shown in Table 1. Emulsion Stability Index (ESI) was calculated using the simple and sensitive "Volumetric method" as follows.

ESI = 100 - (So + Sw), So = (Vo/Va) × 100, Sw = (Vw/Va) × 100ESI = 100-(So + Sw), So = (Vo / V a ) × 100, Sw = (Vw / V a ) × 100

여기서 So는 기름층의 분리도, Sw는 수층의 분리도이고, Va는 유화계의 총 부피이며, Vo는 시간이 경과함에 따라 유화계로부터 분리되어지는 기름층의 부피를, Vw는 시간이 경과함에 따라 유화계로부터 분리되어지는 수분층의 부피를 의미한다. ESI가 100%이면 상분리가 전혀 되지 않은 안정한 상태를 의미한다.Where So is the separation of the oil layer, Sw is the separation of the aqueous layer, Va is the total volume of the emulsification system, Vo is the volume of the oil layer separated from the emulsification system over time, and Vw is the time This means the volume of the water layer separated from the emulsification system. If the ESI is 100%, it means a stable state without any phase separation.

그리고 하기 실시예들과 비교예들에서 제조된 물이 첨가되어 유화된 A중유 또는 B중유 또는 C중유를 사용하여 배출가스 저감 성능을 시험하여 표2에 나타내었다. 그리고 원유와 유화된 원유와의 점도를 동점도로 측정하여 표3에 나타내었다. 성능 시험에 사용된 압축착화 기관은 직렬 직립 4행정 기관으로 연소방식은 직접분사식이며, 실린더내경×행정이 123mm×155mm인 6기통, 11,051cc 배기량에 압축비 17.1:1, 최대토크/엔진속도 = 81.5kg·m/1,400rpm, 최대출력/엔진속도 = 780Nm/2,200rpm인 엔진을 사용하였고, 배출가스 조사는 AVL사의 엔진동력계를 사용하여 ND-13 mode로 운행하여 Firm Ware Technology사의 EXL-1628 배기분석계를 사용하였다. In addition, the exhaust gas reduction performance was tested using A heavy oil, B heavy oil, or C heavy oil emulsified by adding water prepared in Examples and Comparative Examples, and is shown in Table 2. And the viscosity of the crude oil and the emulsified crude oil is shown in Table 3 by measuring the kinematic viscosity. The compression ignition engine used in the performance test was a series upright four-stroke engine, and the combustion method was direct injection type. The engine was used with kg · m / 1,400rpm, maximum output / engine speed = 780Nm / 2,200rpm, and exhaust gas irradiation was operated in ND-13 mode using AVL's engine dynamometer and the EXL-1628 exhaust analyzer from Firm Ware Technology Was used.

실시예 1Example 1

A화합물로 폴리옥시에틸렌 알코올의 반복단위(중합도)가 10인 폴리옥시에틸렌 라우릴알코올에톡시레이트5g과 B화합물로 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위(중합도)가 10인 노닐페놀폴리옥시에틸렌프로필렌 블록공중합물질 5g을 혼합한 유화제를 물 30중량%가 혼합된 A중유 10kg에 넣고 20㎛ 진폭의 초음파를 15분간 조사하였더니 물의 평균 입경이 2㎛가 되었으며 물 외부를 A중유가 감싸며 유화되었다. 5 g of polyoxyethylene lauryl alcohol ethoxylate having a repeating unit (polymerization degree) of polyoxyethylene alcohol as compound A and nonylphenol polyoxy having a repeating unit (polymerization degree) of alkylpolyethylene polypropylene block copolymer as 10 compound An emulsifier mixed with 5 g of ethylene propylene block copolymer was placed in 10 kg of A heavy oil mixed with 30 wt% of water, and irradiated with ultrasonic waves having a 20 μm amplitude for 15 minutes. The average particle diameter of water became 2 μm. It became.

실시예 2Example 2

A화합물로 폴리옥시에틸렌 알코올의 반복단위가 20인 폴리옥시에틸렌 세틸알코올에톡시레이트5g과 B화합물로 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위가 20인 글리세롤스테아레이트폴리옥시에틸렌프로필렌 블록공중합물질 5g을 혼합한 유화제를 물 30중량%가 혼합된 B중유 10kg에 넣고 20㎛ 진폭의 초음파를 15분간 조사하였더니 물의 평균 입경이 2㎛가 되었으며 물 외부를 B중유가 감싸며 유화되었다.5 g of polyoxyethylene cetyl alcohol ethoxylate with a repeating unit of polyoxyethylene alcohol as compound A and 5 g of glycerol stearate polyoxyethylene propylene block copolymer with a repeating unit of alkylpolyethylene polypropylene block copolymer as a compound B of 20 The emulsifier was mixed with 10 kg of B heavy oil mixed with 30% by weight of water, and irradiated with ultrasonic waves having an amplitude of 20 μm for 15 minutes. The average particle diameter of the water was 2 μm, and the B oil was wrapped around the outside of the water.

실시예 3Example 3

A화합물로 폴리옥시에틸렌 알코올의 반복단위가 20인 폴리옥시에틸렌 스테아릴알코올에톡시레이트2.5g과 반복단위가 20인 폴리옥시에틸렌 트리데실알코올에톡시레이트2.5g과 B화합물로 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위가 20인 글리세롤스테아레이트폴리옥시에틸렌프로필렌 블록공중합물질 2.5g과 반복단위가 20인 라우릴알코올폴리옥시에틸렌프로필렌 블록공중합물질 2.5g을 혼합한 유화제를 물 30중량%가 혼합된 C중유 10kg에 넣고 20㎛ 진폭의 초음파를 15분간 조사하였더니 물의 평균 입경이 2㎛가 되었으며 물 외부를 C중유가 감싸며 유화되었다.As compound A, 2.5g of polyoxyethylene stearyl alcohol ethoxylate having a repeating unit of 20 polyoxyethylene alcohol, 2.5g of polyoxyethylene tridecyl alcohol ethoxylate having a repeating unit of 20 and a compound B of alkylpolyethylene polypropylene 30 weight% of an emulsifier mixed with 2.5 g of glycerol stearate polyoxyethylene propylene block copolymer having a repeating unit of 20 and 2.5 g of lauryl alcohol polyoxyethylene propylene block copolymer having a repeating unit of 20 After the ultrasonic wave of 20㎛ amplitude was put into 10kg of C heavy oil for 15 minutes, the average particle diameter of water became 2㎛ and the C oil was wrapped around the water.

실시예 4Example 4

A화합물로 폴리옥시에틸렌 알코올의 반복단위가 10인 폴리옥시에틸렌 올레일알코올에톡시레이트2.5g과 반복단위가 10인 폴리옥시에틸렌 옥틸알코올에톡시레이트2.5g과 B화합물로 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위가 10인 글리세롤스테아레이트폴리옥시에틸렌프로필렌 블록공중합물질 2.5g과 반복단위가 10인 옥틸페놀폴리옥시에틸렌프로필렌 블록공중합물질 2.5g을 혼합한 유화제를 물 30중량%가 혼합된 A중유 10kg에 넣고 20㎛ 진폭의 초음파를 15분간 조사하였더니 물의 평균 입경이 2㎛가 되었으며 물 외부를 A중유가 감싸며 유화되었다..Block A copolymer of polyoxyethylene oleyl alcohol ethoxylate 2.5g with 10 repeating units of polyoxyethylene alcohol as compound A and 2.5g of polyoxyethylene octyl alcohol ethoxylate with 10 repeating units and B copolymer A heavy oil containing 30% by weight of water in an emulsifier mixed with 2.5 g of glycerol stearate polyoxyethylene propylene block copolymer having a repeating unit of 10 and 2.5 g of octylphenol polyoxyethylene propylene block copolymer having a repeating unit of 10 After the ultrasonic wave of 20㎛ amplitude was put into 10kg for 15 minutes, the average particle diameter of water became 2㎛, and the oil of A was wrapped around the outside of the water.

실시예 5Example 5

A화합물로 폴리옥시에틸렌 알코올의 반복단위가 20인 폴리옥시에틸렌 세틸알코올에톡시레이트5g과 B화합물로 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위가 20인 글리세롤스테아레이트폴리옥시에틸렌프로필렌 블록공중합물질 5g을 혼합한 유화제를 물 20중량%가 혼합된 사우디산 원유 10kg에 넣고 40℃에서 200rpm으로 15분간 교반하였더니 원유의 외부를 물이 감싸며 유화되었다.5 g of polyoxyethylene cetyl alcohol ethoxylate with a repeating unit of polyoxyethylene alcohol as compound A and 5 g of glycerol stearate polyoxyethylene propylene block copolymer with a repeating unit of alkylpolyethylene polypropylene block copolymer as a compound B of 20 The emulsifier was mixed into 20kg of Saudi Arabian crude oil mixed with 20% by weight of water and stirred at 200rpm at 40 ° C. for 15 minutes to emulsify the outside of the crude oil.

비교예 1Comparative Example 1

A화합물로 폴리옥시에틸렌 알코올의 반복단위(중합도)가 10인 폴리옥시에틸렌 라우릴알코올에톡시레이트 10g만을 물 30중량%가 혼합된 A중유 10kg에 넣고 20㎛ 진폭의 초음파를 15분간 조사하였다.Only 10 g of polyoxyethylene lauryl alcohol ethoxylate having 10 repeating units (polymerization degree) of polyoxyethylene alcohol as compound A was placed in 10 kg of A heavy oil mixed with 30 wt% of water and irradiated with ultrasonic waves having a 20 μm amplitude for 15 minutes.

비교예 2Comparative Example 2

B화합물로 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위(중합도)가 10인 노닐페놀폴리옥시에틸렌프로필렌 블록공중합물질 10g만을 물 30중량%가 혼합된 A중유 10kg에 넣고 20㎛ 진폭의 초음파를 15분간 조사하였다.As a compound B, only 10 g of nonylphenolpolyoxyethylene propylene block copolymer having 10 repeating units (polymerization degree) of an alkyl polyethylene polypropylene block copolymer was placed in 10 kg of A heavy oil mixed with 30% by weight of water and subjected to ultrasonic waves having a 20 μm amplitude for 15 minutes. Investigate.

비교예 3Comparative Example 3

물 30중량%가 혼합된 A중유 10kg에 20㎛ 진폭의 초음파를 15분간 조사하였다. Ultrasound having a 20 μm amplitude was irradiated for 10 minutes to 10 kg of A heavy oil mixed with 30 wt% water.

비교예 4Comparative Example 4

물 30중량%가 혼합된 B중유에 10kg에 20㎛ 진폭의 초음파를 15분간 조사하였다.Ultrasound of 20 μm amplitude was irradiated to 10 kg of B heavy oil mixed with 30 wt% of water for 15 minutes.

비교예 5Comparative Example 5

물 30중량%가 혼합된 C중유에 10kg에 20㎛ 진폭의 초음파를 15분간 조사하였다Ultrasound of 20 μm amplitude was irradiated to 10 kg of C heavy oil mixed with 30 wt% water for 15 minutes.

비교예 6Comparative Example 6

물 20중량%가 혼합된 사우디산 원유 10kg에 40℃에서 200rpm으로 15분간 교반하였다.20 kg of Saudi Arabian crude oil mixed with 20% by weight of water was stirred at 40 ° C. at 200 rpm for 15 minutes.

유화 중질유의 상분리 정도 Phase separation degree of emulsified heavy oil 80℃의 항온조 내에서 시간경과에 따른 상분리 정도(ESI%)Degree of phase separation (ESI%) over time in a thermostatic chamber at 80 ℃ 실시예Example 1시간1 hours 2시간2 hours 6시간6 hours 12시간12 hours 실시예 1Example 1 100100 100100 100100 100100 실시예 2Example 2 100100 100100 100100 100100 실시예 3Example 3 100100 100100 100100 100100 실시예 4Example 4 100100 100100 100100 100100 실시예 5Example 5 100100 100100 100100 100100 비교예 1Comparative Example 1 7676 3232 00 00 비교예 2Comparative Example 2 7979 3636 00 00 비교예 3Comparative Example 3 1515 00 00 00 비교예 4Comparative Example 4 2424 88 00 00 비교예 5Comparative Example 5 3333 1212 00 00 비교예 6Comparative Example 6 00 00 00 00

표1에서 보는 것과 같이 A화합물과 B화합물을 혼합하여 유화제로 사용한 실시예1부터 실시예5까지의 경우 유화가 잘되고 물과 중질유와의 상분리가 일어나지 않아 안전하게 사용할 수 있다.   As shown in Table 1, in the case of Examples 1 to 5, in which A compound and B compound were mixed and used as an emulsifier, emulsification was good and phase separation between water and heavy oil did not occur, and thus it could be used safely.

배출가스 분석Emissions analysis 실시예Example 매연 저감(%)Smoke reduction (%) 질소산화물 저감(%)Nitrogen oxide reduction (%) 실시예 1Example 1 5757 6565 실시예 2Example 2 6464 6767 실시예 3Example 3 7272 6868 실시예 4Example 4 5858 6666 비교예 1Comparative Example 1 1717 4343 비교예 2Comparative Example 2 1919 4545 비교예 3Comparative Example 3 1313 2626 비교예 4Comparative Example 4 1414 2828 비교예 5Comparative Example 5 1616 2929

표 2에서 보는것과 같이 중질유를 본 발명의 실시예처럼 유화시켜 사용하게 되면 중질유 내부에 미세입자화 되어 있던 물이 엔진 내부에서 미세폭발을 일으켜 중질유 입자를 잘게 쪼개어 주어 산소와 접촉을 원활하게 하는 역할을 하여 완전 산화에 가깝게 유도하여 매연을 50% 이상 줄여주며, 중질유 내부에 미세입자화 되어 있던 물이 엔진 내부에서 미세폭발을 일으킬 때 잠열을 빼앗아 엔진 내부의 온도를 낮춰주어 질소산화물의 발생을 억제하게 되어 질소산화물 배출을 60% 이상 줄여주는 효과를 보여주고 있다. 따라서 본 발명의 효과로 대기오염물질을 덜 배출시켜 대기환경개선에 크게 기여할수 있을 것으로 판단되며, 물을 사용함으로 인하여 그만큼 에너지를 감소하게 되고 온실가스인 이산화탄소 배출을 감축하는 효과를 동시에 얻을수 있다.  As shown in Table 2, when the oil is used to emulsify the heavy oil as in the embodiment of the present invention, water that has been finely granulated inside the heavy oil causes microexplosion in the engine to finely split the heavy oil particles to smoothly contact with oxygen. It reduces the smoke by more than 50% by inducing close to complete oxidation, and takes the latent heat when the microparticles of water inside the heavy oil causes microexplosion inside the engine to lower the temperature inside the engine to suppress the generation of nitrogen oxides. It has been shown to reduce nitrogen oxide emissions by more than 60%. Therefore, it is judged that the air pollutants can be greatly contributed to the improvement of the atmospheric environment by reducing the air pollutants by the effect of the present invention, and the energy can be reduced by the use of water, and the effect of reducing the carbon dioxide emission of greenhouse gases can be simultaneously obtained.

원유의 온도별 동점도 저하 효과Effects of Crude Viscosity on Oil Temperature 실시예Example 온도별 동점도(cSt)Dynamic Kinematic Viscosity (cSt) 20℃20 ℃ 30℃30 ℃ 40℃40 ℃ 실시예 5Example 5 6767 4444 2323 비교예 6Comparative Example 6 214214 155155 8484

Claims (8)

폴리옥시에틸렌 알코올 중에서 선택된 하나 이상의 화합물 (A)와 알킬폴리에틸렌폴리프로필렌 블록공중합 물질 중에서 선택된 하나 이상의 화합물 (B)를 1 : 100 ∼ 100 : 1 의 중량비율로 혼합되고,
상기 화합물 A 또는 상기 화합물 B가 2종 이상일 때에는 중량을 기준으로 하는 화합물 A의 합과 화합물 B의 합의 비가 1 : 100 ∼ 100 : 1 이며,
상기 폴리옥시에틸렌 알코올에서 폴리옥시에틸렌의 반복단위(중합도)는 1∼30 이고, 상기 알킬폴리에틸렌폴리프로필렌 블록공중합 물질의 반복단위(중합도)는 1∼30 이고,
상기 폴리옥시에틸렌 알코올에서 알코올 성분으로는 노닐페놀에톡시레이트, 옥틸페놀에톡시레이트, 라우릴알코올에톡시레이트, 세틸알코올에톡시레이트, 올레일알코올에톡시레이트, 스테아릴알코올에톡시레이트, 트리데실알코올에톡시레이트 및 소르비탄에스테르로 구성된 군으로부터 단독으로 또는 조합적으로 선택되며, 상기 알킬폴리에틸렌 폴리프로필렌 블록공중합 물질에서 알킬 성분으로는 노닐페놀, 라우릴알코올, 글리세롤스테아레이트 및 브랜치드데실알코올로 구성된 군으로부터 단독으로 또는 조합적으로 선택되는 것을 특징으로 하는 중질유 유화제.
At least one compound (A) selected from polyoxyethylene alcohol and at least one compound (B) selected from alkylpolyethylene polypropylene block copolymer materials are mixed at a weight ratio of 1: 100 to 100: 1,
When the compound A or the compound B is two or more kinds, the sum of the sum of the compound A and the compound B on the basis of weight is from 1: 100 to 100: 1,
In the polyoxyethylene alcohol, the repeating unit (polymerization degree) of polyoxyethylene is 1 to 30, and the repeating unit (polymerization degree) of the alkylpolyethylene polypropylene block copolymer is 1 to 30,
The alcohol component in the polyoxyethylene alcohol is nonylphenol ethoxylate, octylphenol ethoxylate, lauryl alcohol ethoxylate, cetyl alcohol ethoxylate, oleyl alcohol ethoxylate, stearyl alcohol ethoxylate, tri It is selected alone or in combination from the group consisting of decyl alcohol ethoxylate and sorbitan ester, and the alkyl component in the alkyl polyethylene polypropylene block copolymer is nonylphenol, lauryl alcohol, glycerol stearate and branched decyl alcohol. Heavy oil emulsifier, characterized in that selected from the group consisting of alone or in combination.
삭제delete 삭제delete 삭제delete 제 1항에 따른 중질유 유화제를 A 중유 또는 B 중유 또는 C 중유 또는 원유와 물이 중량비로 1 ∼ 60%로 혼합된 연료에 중량비로 0.01% ∼ 15%를 첨가하여 제조된 것을 특징으로 하는 유화중질유.The heavy oil emulsifier according to claim 1 is prepared by adding 0.01% to 15% by weight to a fuel in which A heavy oil or B heavy oil or C heavy oil or crude oil and water are mixed at a weight ratio of 1 to 60%. . 제 1항에 따른 유화제를 기계적인 유화 또는 초음파를 사용하여 유화시켜 물의 입경이 0.1 ∼ 20㎛로 되도록 세절화시켜 물 주위에 A 중유, B 중유 또는 C중유가 감싸게 유화시키는 것을 특징으로 하는 유화중질유.Emulsified heavy oil, characterized in that the emulsifier according to claim 1 is emulsified using mechanical emulsification or ultrasonic wave so that the particle size of the water is 0.1 ~ 20㎛ emulsified so that A heavy oil, B heavy oil or C heavy oil wrapped around the water . 제 6항에 있어서, 초음파를 사용할 때에는 진폭이 5 ∼ 200㎛인 것을 특징으로 하는 유화중질유.The emulsified heavy oil according to claim 6, wherein the amplitude is 5 to 200 mu m when using ultrasonic waves. 제 1항에서 제조된 유화제를 기계적인 유화 또는 초음파를 사용하여 유화시켜 원유 주위에 물이 감싸게 유화시키는 것을 특징으로 하는 유화중질유.Emulsified heavy oil, characterized in that the emulsifier prepared in claim 1 is emulsified using a mechanical emulsification or ultrasonic wave so that water is wrapped around the crude oil.
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