WO2015026138A1 - Method for removing limonene and device for removing limonene in biomass saccharification liquid, and bioethanol production method using the removal method - Google Patents

Method for removing limonene and device for removing limonene in biomass saccharification liquid, and bioethanol production method using the removal method Download PDF

Info

Publication number
WO2015026138A1
WO2015026138A1 PCT/KR2014/007693 KR2014007693W WO2015026138A1 WO 2015026138 A1 WO2015026138 A1 WO 2015026138A1 KR 2014007693 W KR2014007693 W KR 2014007693W WO 2015026138 A1 WO2015026138 A1 WO 2015026138A1
Authority
WO
WIPO (PCT)
Prior art keywords
limonene
biomass
activated carbon
removal
cellulose fiber
Prior art date
Application number
PCT/KR2014/007693
Other languages
French (fr)
Korean (ko)
Inventor
배현종
신한기
최인성
Original Assignee
전남대학교산학협력단
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 전남대학교산학협력단 filed Critical 전남대학교산학협력단
Priority to CN201480046589.7A priority Critical patent/CN105473621A/en
Publication of WO2015026138A1 publication Critical patent/WO2015026138A1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M45/00Means for pre-treatment of biological substances
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/12Bioreactors or fermenters specially adapted for specific uses for producing fuels or solvents
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • C12P7/08Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
    • C12P7/12Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate substrate containing sulfite waste liquor or citrus waste
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Definitions

  • the present invention relates to a method for removing limonene of biomass, and more particularly, to efficiently remove limonene present in biomass such as citrus fruit, orange, grapefruit, lemon and lime, and to improve bioethanol production yield. It relates to a limonene removal method, limonene removal device and bioethanol production method using the removal method of the biomass saccharification solution.
  • Raw materials for the production of these first-generation bioethanol face many problems such as competition with food and livestock feed, saturation of cultivated area. In order to overcome this, research is being conducted to produce bioethanol using waste resources.
  • the saccharification process converts biomass into sugar components by acid and enzyme treatment
  • the fermentation process refers to a process of converting ethanol and carbon dioxide by using microorganisms such as yeast and E. coli using the saccharification liquid generated through saccharification process.
  • the presence of a fermentation inhibitor to inhibit the fermentation of microorganisms is very low efficiency of conversion of sugar components to ethanol.
  • Biomass such as citrus, orange, grapefruit, lemon and lime are attracting attention as a raw material for bioethanol production because they contain high sugar content, but they contain fermentation inhibitors called limonene. There is a difficulty. Therefore, effective removal of limonene for bioethanol production is recognized as an important task.
  • the present inventors have completed the present invention by solving the problems of the limonene removal method and apparatus using the conventional steam aeration as a result of research efforts to solve this problem.
  • an object of the present invention by using activated carbon and cellulose fibers, limonene known as fermentation inhibitors can be removed to a level that will not affect the fermentation process, the biomass saccharification liquid which can improve the fermentation efficiency converted to ethanol It is to provide a method for removing limonene.
  • Another object of the present invention is to provide a separate process apparatus, such as a steam decay apparatus, and a limonene removal method of biomass saccharified liquid which can be usefully used because high energy for generating steam is not required.
  • Another object of the present invention is to separate the limonene from the activated carbon and cellulose fiber after the limonene removal process, can reduce the waste of resources, the activated carbon and cellulose fiber can be easily reused, significantly reducing the processing cost
  • the present invention provides a method for removing limonene from a biomass saccharified solution.
  • the present invention comprises the steps of preparing a saccharified liquid obtained from the biomass containing limonene; And it provides a limonene removal method of biomass saccharified liquid comprising the step of contacting any one or more of the saccharified liquid and activated carbon and cellulose fiber.
  • the contacting step is used 0.3 to 0.5g of activated carbon based on the limonene content of 0.8411g / cm 3 of the saccharified solution when using activated carbon.
  • the step of contacting the cellulose fiber is used 0.125 to 0.2g based on the limonene content of 0.8411g / cm 3 of the saccharified solution when using the cellulose fiber.
  • the present invention also provides a saccharified liquid obtained from limonene-containing biomass, wherein the limonene content is less than 0.025% by weight.
  • the present invention is a hollow housing therein; And it provides a limonene removal device comprising any one or more of activated carbon and cellulose fiber inserted into the hollow at a predetermined thickness.
  • At least one of the activated carbon and cellulose fiber is contacted with saccharified liquid obtained from limonene containing biomass to remove limonene.
  • the present invention comprises the steps of preparing a saccharified solution in which the limonene removal method is performed; And it provides a method of producing a bioethanol comprising a fermentation step of fermenting using any one or more of yeast and E. coli in the saccharification liquid.
  • the present invention has the following excellent effects.
  • a separate process apparatus such as a steam attenuating device, and high energy for generating steam can be usefully used.
  • limonene can be separated from the activated carbon and the cellulose fiber, thereby reducing the waste of resources, and the activated carbon and the cellulose fiber can be easily reused, thereby significantly reducing the processing cost.
  • FIG. 1 (a) is a graph analyzing the limonene content before limonene removal using GC (Gas Chromatography), (b) is a graph analyzing the result after limonene removal using the limonene removal method using GC to be.
  • FIG. 2 (a) is a schematic diagram of a limonene removal apparatus according to an embodiment of the present invention, (b) is a schematic diagram of a limonene removal apparatus according to another embodiment of the present invention, (c) is another of the present invention It is a schematic diagram of a limonene removal apparatus which concerns on an Example.
  • Figure 3 is a graph showing the fermentation efficiency before and after limonene removal using the limonene removal method of the present invention.
  • the technical feature of the present invention is a new limonene removal method that can improve the fermentation efficiency of converting limonene, known as a fermentation inhibitor, to a level that will not affect the fermentation process by using activated carbon and cellulose fiber to convert to ethanol.
  • the limonene removal method of the biomass saccharification liquid of the present invention includes preparing a saccharification liquid obtained from the biomass containing limonene and contacting any one or more of the saccharification liquid with activated carbon and cellulose fiber.
  • the biomass is not limited to biomass containing limonene, but any one or more selected from the group consisting of peels of tangerines, oranges, grapefruits, lemons, limes, and mixtures thereof, which are discarded as waste after being used. This is preferably used. This is because waste resources that are discarded can be used as biomass, thereby reducing the cost of treating waste resources and producing value-added resources such as bioethanol and limonene from waste resources.
  • the step of secreting the saccharification liquid may be prepared in general through the saccharification process of acid hydrolysis and enzymatic hydrolysis from the biomass.
  • the method of hydrolysis is not limited.
  • Figure 1 (a) is a graph of the saccharified solution analyzed by GC, showing that the saccharin contains limonene.
  • Figure 1 (b) is a result of analyzing the saccharified solution after removing the limonene using the limonene removal method of the present invention using GC.
  • limonene contained in the saccharified solution is contacted with activated carbon, contacted with cellulose fiber, and contacted with a mixture prepared by mixing the activated carbon and cellulose fiber.
  • Limonene may be removed through one or more of the step of making.
  • the contacting step is preferably 0.3 to 0.5 g of activated carbon based on the limonene content of 0.8411 g / cm 3 of the saccharified solution when activated carbon is used. If less than 0.3 g of activated carbon is used, the content of limonene that is not removed is higher than the concentration causing the inhibition of fermentation, which causes fermentation inhibition in the fermentation process using microorganisms, thereby lowering the production efficiency of bioethanol. In addition, when using more than 0.5g of activated carbon exceeds the amount necessary to remove limonene is a waste of resources, because it does not affect the fermentation efficiency.
  • the cellulose fiber in the contacting step it is preferable that 0.125 to 0.2g of the cellulose fiber is used based on the limonene content 0.8411g / cm 3 of the saccharified solution.
  • the content of limonene, which is not removed is higher than the concentration causing the inhibition of fermentation, which induces the inhibition of fermentation in the fermentation process using microorganisms.
  • the production efficiency of is lowered, and when using the cellulose fiber in excess of 0.2g, it exceeds the amount necessary to remove limonene, wastes resources, and does not affect the fermentation efficiency.
  • a saccharified liquid obtained from a limonene-containing biomass wherein the limonene content is less than 0.025% by weight.
  • the sugar component contained in the saccharified liquid may be converted into bioethanol by the microorganism.
  • the limonene content of the saccharified solution may be used by removing it to 0.020% by weight or less. If the limonene content of the saccharified solution is removed to 0.020% by weight or less, limonene does not affect the fermentation process at all, and bioethanol can be produced efficiently.
  • a hollow is formed therein, so that the activated carbon is inserted into the hollow at a predetermined thickness to provide a device capable of removing limonene.
  • the cellulose fiber may be inserted into the hollow at a predetermined thickness to remove limonene, and as shown in (c) of FIG. 2, the activated carbon and the cellulose fiber of the hollow may be removed.
  • the mixture can be inserted to a certain thickness to remove limonene.
  • the limonene removal device is not limited as long as it is manufactured containing any one or more of activated carbon and cellulose fiber.
  • the activated carbon and cellulose fiber to which limonene is adsorbed after contact with the saccharification solution to remove limonene can be reused by separating limonene using an organic solvent, wherein the separated limonene is a food additive, a perfume of perfume, a known detergent It can be used as a car article, a cleaning agent, and the like.
  • saccharomyces cerevisiae saccharomyces cerevisiae
  • Any of the conventional strains known in the art may be used, such as convertible heat resistant strains, recombinant strains that can simultaneously perform glycosylation and fermentation.
  • Limonene was removed by contacting the saccharified solution containing 1% by weight of limonene using 0 mg, 50 mg, 100 mg, 150 mg, 200 mg, 250 mg, 300 mg, 500 mg of each activated carbon, and the results are shown in Table 1 below.
  • Limonene was removed by contacting the saccharified solution containing 1% by weight of limonene using 0 mg, 5 mg, 15 mg, 25 mg, 50 mg, 75 mg, 100 mg, 125 mg, and 150 mg of each of the cellulose fibers. Shown in
  • a limonene removal device was prepared in which 25 mg of cellulose fiber and 150 mg of activated carbon were mixed.
  • Limonene was removed from the saccharification solution containing 1% by weight of limonene by using the limonene removing apparatus prepared in Example 3, and as a result, all limonene was removed as shown in Table 3 below.
  • Bioethanol was prepared from the saccharification liquid from which the components of limonene were removed from each of Examples 1 to 4 by less than 0.025% by weight.
  • the strain using a known Saccharomyces cerevisiae the pH was maintained at 5.0, the fermentation process was carried out in a fermentation tank of 30 under the conditions of rpm 200, to obtain a bioethanol.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Genetics & Genomics (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Sustainable Development (AREA)
  • Biomedical Technology (AREA)
  • Molecular Biology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

The present invention relates to a method for removing limonene in biomass. More specifically, the present invention relates to: a method for removing limonene and a device for removing limonene in a biomass saccharification liquid, whereby it is possible to effectively remove the limonene present in biomass such as mandarin peel, orange peel, grapefruit peel, lemon peel and lime peel, and it is possible to improve the production yield of bioethanol; and a bioethanol production method using the removal method.

Description

바이오매스 당화액의 리모넨 제거방법, 리모넨 제거 장치 및 상기 제거방법을 이용한 바이오에탄올 제조 방법Limonene removal method, limonene removal device of biomass saccharification liquid and bioethanol production method using the removal method
본 발명은 바이오매스의 리모넨 제거방법에 관한 것으로, 보다 구체적으로는 감귤박, 오렌지박, 자몽박, 레몬박, 라임박 등의 바이오매스에 존재하는 리모넨을 효율적으로 제거하고 바이오에탄올 생산 수율을 향상시킬 수 있는 바이오매스 당화액의 리모넨 제거방법, 리모넨 제거 장치 및 상기 제거방법을 이용한 바이오에탄올 제조 방법에 관한 것이다.The present invention relates to a method for removing limonene of biomass, and more particularly, to efficiently remove limonene present in biomass such as citrus fruit, orange, grapefruit, lemon and lime, and to improve bioethanol production yield. It relates to a limonene removal method, limonene removal device and bioethanol production method using the removal method of the biomass saccharification solution.
최근 급격하게 진행되고 있는 지구 온난화에 의한 온실효과와 석유고갈 문제를 해결하기 위하여 당화액을 이용한 바이오에탄올 생산에 많은 관심과 연구가 집중되고 있으며, 바이오에탄올 생산을 위한 바이오매스로서 사탕수수 또는 전분이 이용되어 왔다. In order to solve the greenhouse effect and petroleum depletion problem caused by the recent global warming, much attention and research is focused on the production of bioethanol using saccharified liquid, and sugar cane or starch is used as biomass for bioethanol production. Has been used.
이러한 1세대 바이오에탄올 생산을 위한 원료들은 식품 및 가축사료와의 경쟁, 재배 면적의 포화 등 많은 문제에 봉착해 있다. 이를 극복하기 위하여 폐자원을 이용하여 바이오 에탄올을 생산하기 위한 연구가 진행되고 있다. Raw materials for the production of these first-generation bioethanol face many problems such as competition with food and livestock feed, saturation of cultivated area. In order to overcome this, research is being conducted to produce bioethanol using waste resources.
일반적으로 폐자원을 포함한 바이오매스로부터 바이오 에탄올을 생산하기 위하여 당화 공정 및 발효공정을 거치게 된다. 당화 공정은 바이오매스를 산 및 효소처리하여 당성분으로 전환 시키는 공정이며, 발효공정은 당화 공정을 통해 생성된 당화액을 이용하여 효모, 이콜라이등 미생물을 이용하여 에탄올과 이산화탄소로 전환되는 과정을 일컫는다. 이때 발효공정에서는 미생물의 발효를 억제시키는 발효 억제재가 존재하게 되면 당성분이 에탄올로 전환되는 효율이 매우 낮아지게 된다. 감귤박, 오렌지박, 자몽박, 레몬박, 라임박 등의 바이오매스들은 높은 당성분을 함유하고 있어 바이오에탄올 생산원료로써 주목을 받고 있으나, 리모넨이라는 발효저해물질을 함유하고 있어, 바이오에탄올로 전환하는데 어려움이 있다. 따라서 바이오에탄올 생산을 위하여 리모넨의 효과적인 제거가 중요한 과제로 인식되고 있다. In general, in order to produce bioethanol from biomass including waste resources, it is subjected to saccharification and fermentation. The saccharification process converts biomass into sugar components by acid and enzyme treatment, and the fermentation process refers to a process of converting ethanol and carbon dioxide by using microorganisms such as yeast and E. coli using the saccharification liquid generated through saccharification process. . At this time, in the fermentation process, the presence of a fermentation inhibitor to inhibit the fermentation of microorganisms is very low efficiency of conversion of sugar components to ethanol. Biomass such as citrus, orange, grapefruit, lemon and lime are attracting attention as a raw material for bioethanol production because they contain high sugar content, but they contain fermentation inhibitors called limonene. There is a difficulty. Therefore, effective removal of limonene for bioethanol production is recognized as an important task.
기존 리모넨 제거 방법으로는 스팀 폭쇄(steam explosion)가 개발되어 이용되고 있으나, 스팀 폭쇄를 이용하는 경우에는 별도의 공정장치와 스팀을 발생시키기 위한 높은 에너지가 필요하고, 리모넨을 일정수준 이하까지 제거할 수 없어, 발효 시 에탄올로 전환되는 효율이 낮아지게 되는 문제점이 있다.Steam explosion has been developed and used as a method of removing limonene. However, when steam explosion is used, a separate process device and high energy for generating steam are required, and limonene can be removed to a certain level or less. There is no problem that the efficiency of conversion to ethanol during fermentation is low.
본 발명자들은 이러한 문제점을 해결하기 위하여 연구 노력한 결과 종래의 스팀 폭쇄를 이용한 리모넨 제거방법 및 장치가 가지고 있는 문제점을 해결함으로써 본 발명을 완성하였다.The present inventors have completed the present invention by solving the problems of the limonene removal method and apparatus using the conventional steam aeration as a result of research efforts to solve this problem.
따라서 본 발명의 목적은 활성탄과 셀룰로오스 파이버를 이용하여, 발효 억제재로 알려진 리모넨이 발효공정에 영향을 미치지 않을 수준까지 제거할 수 있어, 에탄올로 전환되는 발효 효율을 향상시킬 수 있는 바이오매스 당화액의 리모넨 제거방법을 제공하는 것이다.Therefore, an object of the present invention, by using activated carbon and cellulose fibers, limonene known as fermentation inhibitors can be removed to a level that will not affect the fermentation process, the biomass saccharification liquid which can improve the fermentation efficiency converted to ethanol It is to provide a method for removing limonene.
본 발명의 다른 목적은 스팀 폭쇄 장치와 같은 별도의 공정장치와 스팀을 발생시키기 위한 높은 에너지가 필요하지 않아 유용하게 이용될 수 있는 바이오매스 당화액의 리모넨 제거방법을 제공하는 것이다.Another object of the present invention is to provide a separate process apparatus, such as a steam decay apparatus, and a limonene removal method of biomass saccharified liquid which can be usefully used because high energy for generating steam is not required.
본 발명의 또 다른 목적은 리모넨 제거 공정 이후에 활성탄 및 셀룰로오스 파이버로부터 리모넨을 분리할 수 있어, 자원의 낭비를 줄일 수 있으며, 활성탄 및 셀룰로오스 파이버는 재사용이 용이하여, 처리비용을 획기적으로 절감할 수 있는 바이오매스 당화액의 리모넨 제거방법을 제공하는 것이다.Another object of the present invention is to separate the limonene from the activated carbon and cellulose fiber after the limonene removal process, can reduce the waste of resources, the activated carbon and cellulose fiber can be easily reused, significantly reducing the processing cost The present invention provides a method for removing limonene from a biomass saccharified solution.
본 발명의 목적들은 이상에서 언급한 목적들로 제한되지 않으며, 언급되지 않은 또 다른 목적들은 아래의 기재로부터 당업자에게 명확하게 이해될 수 있을 것이다.The objects of the present invention are not limited to the above-mentioned objects, and other objects that are not mentioned will be clearly understood by those skilled in the art from the following description.
상술된 본 발명의 목적을 달성하기 위해, 먼저 본 발명은 리모넨이 함유된 바이오매스로부터 얻어진 당화액을 준비하는 단계; 및 상기 당화액과 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상을 접촉시키는 단계를 포함하는 바이오매스 당화액의 리모넨 제거방법을 제공한다.In order to achieve the above object of the present invention, firstly, the present invention comprises the steps of preparing a saccharified liquid obtained from the biomass containing limonene; And it provides a limonene removal method of biomass saccharified liquid comprising the step of contacting any one or more of the saccharified liquid and activated carbon and cellulose fiber.
바람직한 실시예에 있어서, 상기 접촉시키는 단계는 활성탄을 이용할 경우 상기 당화액의 리모넨 함량 0.8411g/cm3 기준으로 상기 활성탄이 0.3 내지 0.5g 사용된다.In a preferred embodiment, the contacting step is used 0.3 to 0.5g of activated carbon based on the limonene content of 0.8411g / cm 3 of the saccharified solution when using activated carbon.
바람직한 실시예에 있어서, 상기 접촉시키는 단계는 셀룰로오스 파이버를 이용할 경우 상기 당화액의 리모넨 함량 0.8411g/cm3 기준으로 상기 셀룰로오스 파이버가 0.125 내지 0.2g 사용된다.In a preferred embodiment, the step of contacting the cellulose fiber is used 0.125 to 0.2g based on the limonene content of 0.8411g / cm 3 of the saccharified solution when using the cellulose fiber.
또한 본 발명은 리모넨 함량이 0.025중량% 미만인 것을 특징으로 하는 리모넨 함유 바이오매스로부터 얻어진 당화액을 제공한다.The present invention also provides a saccharified liquid obtained from limonene-containing biomass, wherein the limonene content is less than 0.025% by weight.
또한 본 발명은 내부에 중공이 형성된 하우징; 및 상기 중공에 일정 두께로 삽입되는 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상을 포함하는 리모넨 제거 장치를 제공한다.In addition, the present invention is a hollow housing therein; And it provides a limonene removal device comprising any one or more of activated carbon and cellulose fiber inserted into the hollow at a predetermined thickness.
바람직한 실시예에 있어서 상기 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상은 리모넨 함유 바이오매스로부터 얻어진 당화액과 접촉되어 리모넨이 제거된다.In a preferred embodiment, at least one of the activated carbon and cellulose fiber is contacted with saccharified liquid obtained from limonene containing biomass to remove limonene.
또한 본 발명은 리모넨 제거방법이 수행된 당화액을 준비하는 단계; 및 상기 당화액에 효모 및 이콜라이 중 어느 하나 이상을 이용하여 발효시키는 발효단계를 포함하는 것을 특징으로 하는 바이오에탄올 제조방법을 제공한다.In another aspect, the present invention comprises the steps of preparing a saccharified solution in which the limonene removal method is performed; And it provides a method of producing a bioethanol comprising a fermentation step of fermenting using any one or more of yeast and E. coli in the saccharification liquid.
본 발명은 다음과 같은 우수한 효과를 갖는다.The present invention has the following excellent effects.
먼저, 본 발명에 의하면 활성탄과 셀룰로오스 파이버를 이용하여, 발효 억제재로 알려진 리모넨을 발효공정에 영향을 미치지 않을 수준까지 제거할 수 있어, 에탄올로 전환되는 발효 효율을 향상시킬 수 있다.First, according to the present invention, using activated carbon and cellulose fiber, limonene, known as a fermentation inhibitor, can be removed to a level that will not affect the fermentation process, thereby improving the fermentation efficiency converted to ethanol.
또한 본 발명에 의하면 스팀폭쇄장치와 같은 별도의 공정장치와 스팀을 발생시키기 위한 높은 에너지가 필요하지 않아 유용하게 이용될 수 있다.In addition, according to the present invention, a separate process apparatus, such as a steam attenuating device, and high energy for generating steam can be usefully used.
또한 본 발명에 의하면 리모넨 제거 공정 이후에 활성탄 및 셀룰로오스 파이버로부터 리모넨을 분리할 수 있어, 자원의 낭비를 줄일 수 있으며, 활성탄 및 셀룰로오스 파이버는 재사용이 용이하여, 처리비용을 획기적으로 절감할 수 있다.In addition, according to the present invention, after the limonene removal process, limonene can be separated from the activated carbon and the cellulose fiber, thereby reducing the waste of resources, and the activated carbon and the cellulose fiber can be easily reused, thereby significantly reducing the processing cost.
도 1 중 (a)는 리모넨 제거 이전의 리모넨 함유량을 GC(Gas Chromatography)를 이용하여 분석한 그래프이고, (b)는 리모넨 제거방법을 이용하여 리모넨 제거 이후의 결과를 GC를 이용하여 분석한 그래프이다.In Figure 1 (a) is a graph analyzing the limonene content before limonene removal using GC (Gas Chromatography), (b) is a graph analyzing the result after limonene removal using the limonene removal method using GC to be.
도 2 중 (a)는 본 발명의 일실시예에 따른 리모넨 제거 장치의 모식도이고, (b)는 본 발명의 다른 실시예에 따른 리모넨 제거 장치의 모식도이며, (c)는 본 발명의 또 다른 실시예에 따른 리모넨 제거 장치의 모식도이다.In Figure 2 (a) is a schematic diagram of a limonene removal apparatus according to an embodiment of the present invention, (b) is a schematic diagram of a limonene removal apparatus according to another embodiment of the present invention, (c) is another of the present invention It is a schematic diagram of a limonene removal apparatus which concerns on an Example.
도 3은 본 발명의 리모넨 제거방법을 이용하여 리모넨 제거 전과 후의 발효 효율을 보여주는 그래프이다. Figure 3 is a graph showing the fermentation efficiency before and after limonene removal using the limonene removal method of the present invention.
본 발명에서 사용되는 용어는 가능한 현재 널리 사용되는 일반적인 용어를 선택하였으나, 특정한 경우는 출원인이 임의로 선정한 용어도 있는데 이 경우에는 단순한 용어의 명칭이 아닌 발명의 상세한 설명 부분에 기재되거나 사용된 의미를 고려하여 그 의미가 파악되어야 할 것이다.The terms used in the present invention were selected as general terms as widely used as possible, but in some cases, the terms arbitrarily selected by the applicant are included. In this case, the meanings described or used in the detailed description of the present invention are considered, rather than simply the names of the terms. The meaning should be grasped.
이하, 첨부한 도면 및 바람직한 실시예들을 참조하여 본 발명의 기술적 구성을 상세하게 설명한다.Hereinafter, with reference to the accompanying drawings and preferred embodiments will be described in detail the technical configuration of the present invention.
그러나 본 발명은 여기서 설명되는 실시예에 한정되지 않고 다른 형태로 구체화 될 수도 있다. However, the present invention is not limited to the embodiments described herein and may be embodied in other forms.
본 발명의 기술적 특징은 활성탄과 셀룰로오스 파이버를 이용하여, 발효 억제재로 알려진 리모넨을 발효공정에 영향을 미치지 않을 수준까지 제거하여, 에탄올로 전환하는 발효 효율을 향상시킬 수 있는 새로운 리모넨 제거방법에 있다.The technical feature of the present invention is a new limonene removal method that can improve the fermentation efficiency of converting limonene, known as a fermentation inhibitor, to a level that will not affect the fermentation process by using activated carbon and cellulose fiber to convert to ethanol.
따라서 본 발명의 바이오매스 당화액의 리모넨 제거방법은 리모넨이 함유된 바이오매스로부터 얻어진 당화액을 준비하는 단계 및 상기 당화액과 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상을 접촉시키는 단계를 포함한다. 이때 상기 바이오매스는 리모넨을 함유하고 있는 바이오매스이면 제한되지 않으나, 사용되어 지고 난 이후에 폐기물로 버려지는 감귤, 오렌지, 자몽, 레몬, 라임의 껍질 및 이들의 혼합물로 그룹으로부터 선택되는 어느 하나 이상이 이용되는 것이 바람직하다. 버려지는 폐자원을 바이오매스로 이용하여, 폐자원의 처리비용을 절감할 수 있으며, 폐자원으로부터 바이오에탄올, 리모넨 등의 부가가치 자원을 생산 할 수 있기 때문이다. 또한 상기 당화액을 분비하는 단계는 일반적으로 바이오매스로부터 산 가수분해 및 효소 가수분해의 당화공정을 통해 당화액을 준비할 수 있다. 이때 상기 당화액은 발효가 가능한 당성분을 포함하고 있기만 하면, 상기 가수분해의 방법은 제한되지 않는다. Therefore, the limonene removal method of the biomass saccharification liquid of the present invention includes preparing a saccharification liquid obtained from the biomass containing limonene and contacting any one or more of the saccharification liquid with activated carbon and cellulose fiber. At this time, the biomass is not limited to biomass containing limonene, but any one or more selected from the group consisting of peels of tangerines, oranges, grapefruits, lemons, limes, and mixtures thereof, which are discarded as waste after being used. This is preferably used. This is because waste resources that are discarded can be used as biomass, thereby reducing the cost of treating waste resources and producing value-added resources such as bioethanol and limonene from waste resources. In addition, the step of secreting the saccharification liquid may be prepared in general through the saccharification process of acid hydrolysis and enzymatic hydrolysis from the biomass. At this time, as long as the saccharification liquid contains a sugar component capable of fermentation, the method of hydrolysis is not limited.
도 1 중 (a)는 당화액을 GC로 분석한 그래프이며, 당화액에 리모넨이 함유되어 있음을 보여준다. 도 1 중 (b)는 본 발명의 리모넨 제거방법을 이용하여 리모넨을 제거한 이후의 당화액을 GC를 이용하여 분석한 결과이다. 도 1 의 (a) 및 (b)에 도시된 바와 같이, 상기 당화액에 포함된 리모넨은 활성탄과 접촉하는 단계, 셀룰로오스 파이버와 접촉시키는 단계 및 상기 활성탄과 셀룰로오스 파이버를 혼합하여 제조된 혼합물과 접촉시키는 단계 중 어느 하나 이상의 단계를 통하여 리모넨이 제거 될 수 있다. In Figure 1 (a) is a graph of the saccharified solution analyzed by GC, showing that the saccharin contains limonene. In Figure 1 (b) is a result of analyzing the saccharified solution after removing the limonene using the limonene removal method of the present invention using GC. As shown in (a) and (b) of FIG. 1, limonene contained in the saccharified solution is contacted with activated carbon, contacted with cellulose fiber, and contacted with a mixture prepared by mixing the activated carbon and cellulose fiber. Limonene may be removed through one or more of the step of making.
이때 상기 접촉시키는 단계는 활성탄을 이용할 경우 상기 당화액의 리모넨 함량 0.8411g/cm3 기준으로 상기 활성탄이 0.3 내지 0.5g 사용되는 것이 바람직하다. 0.3g 미만의 활성탄을 이용할 경우에는 제거되지 않고 남아있는 리모넨의 함유량이 발효 저해를 유발하게 되는 농도보다 높아, 미생물을 이용한 발효 공정에서 발효 저해를 유발하게 되어 바이오에탄올의 생산효율이 낮아지게 된다. 또한 활성탄을 0.5g 초과하여 사용할 경우에는 리모넨을 제거하는데 필요한 양을 초과하게 되어 자원이 낭비되며, 발효효율에도 영향을 주지 않기 때문이다. In this case, the contacting step is preferably 0.3 to 0.5 g of activated carbon based on the limonene content of 0.8411 g / cm 3 of the saccharified solution when activated carbon is used. If less than 0.3 g of activated carbon is used, the content of limonene that is not removed is higher than the concentration causing the inhibition of fermentation, which causes fermentation inhibition in the fermentation process using microorganisms, thereby lowering the production efficiency of bioethanol. In addition, when using more than 0.5g of activated carbon exceeds the amount necessary to remove limonene is a waste of resources, because it does not affect the fermentation efficiency.
또한 상기 접촉시키는 단계에서 셀룰로오스 파이버를 이용할 경우 상기 당화액의 리모넨 함량 0.8411g/cm3 기준으로 상기 셀룰로오스 파이버가 0.125 내지 0.2g 사용되는 것이 바람직하다. 상기의 활성탄을 이용하는 경우와 마찬가지로 0125g 미만의 셀룰로오스 파이버를 이용할 경우에는 제거되지 않고 남아있는 리모넨의 함유량이 발효 저해를 유발하게 되는 농도보다 높아, 미생물을 이용한 발효 공정에서 발효 저해를 유발하게 되어 바이오에탄올의 생산효율이 낮아지게 되고, 0.2g 초과하여 셀롤로오스 파이버를 사용할 경우에는 리모넨을 제거하는데 필요한 양을 초과하게 되어 자원이 낭비되며, 발효효율에도 영향을 주지 않는다. In addition, when using the cellulose fiber in the contacting step, it is preferable that 0.125 to 0.2g of the cellulose fiber is used based on the limonene content 0.8411g / cm 3 of the saccharified solution. When using cellulose fiber of less than 0125g as in the case of using the activated carbon, the content of limonene, which is not removed, is higher than the concentration causing the inhibition of fermentation, which induces the inhibition of fermentation in the fermentation process using microorganisms. The production efficiency of is lowered, and when using the cellulose fiber in excess of 0.2g, it exceeds the amount necessary to remove limonene, wastes resources, and does not affect the fermentation efficiency.
또한 리모넨 함량이 0.025중량% 미만인 것을 특징으로 하는 리모넨 함유 바이오매스로부터 얻어진 당화액이 제공된다. 바이오매스로부터 얻어진 당화액의 리모넨 함량이 0.025중량% 미만으로 떨어지게 되면, 당화액에 포함된 당성분이 미생물에 의해 바이오에탄올로 전환 될 수 있다. 이때 보다 바람직하게는 당화액의 리모넨 함량이 0.020중량% 이하로 제거하여 이용될 수 있다. 당화액의 리모넨 함량이 0.020중량% 이하로 제거되면, 발효 공정에 리모넨이 전혀 영향을 미치지 않으며, 효율적으로 바이오에탄올을 생산할 수 있기 때문이다.Also provided is a saccharified liquid obtained from a limonene-containing biomass, wherein the limonene content is less than 0.025% by weight. When the limonene content of the saccharified liquid obtained from the biomass falls below 0.025% by weight, the sugar component contained in the saccharified liquid may be converted into bioethanol by the microorganism. At this time, more preferably, the limonene content of the saccharified solution may be used by removing it to 0.020% by weight or less. If the limonene content of the saccharified solution is removed to 0.020% by weight or less, limonene does not affect the fermentation process at all, and bioethanol can be produced efficiently.
또한 내부에 중공이 형성된 하우징; 및 상기 중공에 일정 두께로 삽입되는 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상을 포함하는 리모넨 제거 장치가 제공된다. 도 2 중 (a)에 도시된 바와 같이 내부에 중공이 형성되어, 상기 중공에 활성탄이 일정 두께로 삽입되어 리모넨을 제거할 수 있는 장치가 제공될 수 있다. 또한 도 2 중 (b)에 도시된 바와 같이 상기 중공에 셀룰로오스 파이버가 일정 두께로 삽입되어 리모넨을 제거할 수 있으며, 도 2 중 (c)에 도시된 바와 같이 상기 중공에 상기 활성탄과 셀룰로오스 파이버의 혼합물이 일정 두께로 삽입되어 리모넨을 제거할 수 있다. 즉 상기 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상은 리모넨 함유 바이오매스로부터 얻어진 당화액과 접촉되어 리모넨이 제거된다. 이때 상기 리모넨 제거 장치는 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상을 포함하여 제조되면 제한되지 않는다.In addition, a hollow housing therein; And there is provided a limonene removal device comprising any one or more of activated carbon and cellulose fiber inserted into the hollow at a predetermined thickness. As shown in (a) of FIG. 2, a hollow is formed therein, so that the activated carbon is inserted into the hollow at a predetermined thickness to provide a device capable of removing limonene. In addition, as shown in (b) of FIG. 2, the cellulose fiber may be inserted into the hollow at a predetermined thickness to remove limonene, and as shown in (c) of FIG. 2, the activated carbon and the cellulose fiber of the hollow may be removed. The mixture can be inserted to a certain thickness to remove limonene. That is, at least one of the activated carbon and the cellulose fiber is contacted with the saccharification liquid obtained from the limonene-containing biomass to remove limonene. At this time, the limonene removal device is not limited as long as it is manufactured containing any one or more of activated carbon and cellulose fiber.
또한 당화액과 접촉되어 리모넨을 제거한 이후에 리모넨이 흡착되어 있는 상기 활성탄 및 셀룰로오스 파이버는 유기용매를 이용하여 리모넨을 분리시켜 재사용 될 수 있으며, 이때 분리된 리모넨은 식품 첨가제, 향수의 향료, 공지 청정제, 자동차 용품, 세정제 등으로 사용될 수 있다. In addition, the activated carbon and cellulose fiber to which limonene is adsorbed after contact with the saccharification solution to remove limonene can be reused by separating limonene using an organic solvent, wherein the separated limonene is a food additive, a perfume of perfume, a known detergent It can be used as a car article, a cleaning agent, and the like.
또한 본 발명에 따른 리모넨 제거방법이 수행된 당화액을 준비하는 단계; 및 상기 당화액에 효모 및 이콜라이 중 어느 하나 이상을 이용하여 발효시키는 발효단계를 포함하는 것을 특징으로 하는 바이오에탄올 제조방법을 제공한다. 이때 당성분을 에탄올로 전환시킬 수 있는 사카로마이세스 세레비지(saccharomyces cerevisiae)를 사용할 수 있으며, 높은 당 농도에서 발효를 수행할 수 있는 내당성 균주, 효소 당화의 최적 온도인 40~45에서 에탄올 전환이 가능한 내열성 균주, 당화 및 발효를 동시에 수행할 수 있는 재조합 균주 등 당업계에서 알려진 통상적인 균주 중 어느 것이라도 이용될 수 있다.In addition, preparing a saccharified solution in which the limonene removal method according to the present invention was performed; And it provides a method of producing a bioethanol comprising a fermentation step of fermenting using any one or more of yeast and E. coli in the saccharification liquid. At this time, saccharomyces cerevisiae ( saccharomyces cerevisiae ), which can convert sugar components to ethanol, can be used. Any of the conventional strains known in the art may be used, such as convertible heat resistant strains, recombinant strains that can simultaneously perform glycosylation and fermentation.
실시예1Example 1
1 중량%의 리모넨을 함유하고 있는 당화액에 각각의 활성탄 0mg, 50mg, 100mg, 150mg, 200mg, 250mg, 300mg, 500mg을 사용하여 접촉시켜 리모넨을 제거하였으며 그 결과를 하기 표 1에 나타내었다.Limonene was removed by contacting the saccharified solution containing 1% by weight of limonene using 0 mg, 50 mg, 100 mg, 150 mg, 200 mg, 250 mg, 300 mg, 500 mg of each activated carbon, and the results are shown in Table 1 below.
표 1
활성탄 사용량(mg) 잔류 리모넨(중량%)
0 1
50 0.88
100 0.71
150 0.55
200 0.31
250 0.12
300 0.02
500 0.08
Table 1
Activated Carbon Usage (mg) Residual Limonene (wt%)
0 One
50 0.88
100 0.71
150 0.55
200 0.31
250 0.12
300 0.02
500 0.08
실시예2Example 2
1 중량%의 리모넨을 함유하고 있는 당화액에 각각의 셀룰로오스 파이버 0mg, 5mg, 15mg, 25mg, 50mg, 75mg, 100mg, 125mg, 150mg을 사용하여 접촉시켜 리모넨을 제거하었으며, 그 결과를 하기 표 2에 나타내었다.Limonene was removed by contacting the saccharified solution containing 1% by weight of limonene using 0 mg, 5 mg, 15 mg, 25 mg, 50 mg, 75 mg, 100 mg, 125 mg, and 150 mg of each of the cellulose fibers. Shown in
표 2
셀룰로오스 파이버 사용량(mg) 잔류 리모넨(중량%)
0 1
5 0.8
15 0.73
25 0.5
50 1.38
75 0.26
100 0.12
125 0.02
150 0.01
TABLE 2
Cellulose Fiber Usage (mg) Residual Limonene (wt%)
0 One
5 0.8
15 0.73
25 0.5
50 1.38
75 0.26
100 0.12
125 0.02
150 0.01
실시예 3Example 3
감귤박 당화액에 함유되어 있는 리모넨 성분을 제거하기 위하여 셀룰로오스 파이버 25mg과 활성탄 150mg을 혼합시킨 리모넨 제거 장치를 제조 하였다. In order to remove the limonene component contained in the citrus sac solution, a limonene removal device was prepared in which 25 mg of cellulose fiber and 150 mg of activated carbon were mixed.
실시예 4Example 4
실시예 3에서 제조된 상기 리모넨 제거 장치를 이용하여 1 중량%의 리모넨이 포함된 당화액으로부터 리모넨을 제거하였으며, 그 결과 하기 표3에 나타낸 바와 같이 리모넨이 모두 제거되었다.Limonene was removed from the saccharification solution containing 1% by weight of limonene by using the limonene removing apparatus prepared in Example 3, and as a result, all limonene was removed as shown in Table 3 below.
표 3
활성탄 사용량(mg) 셀룰로오스 파이버 사용량(mg) 잔류 리모넨(중량%)
0 0 1
0 25 0.5
150 0 0.55
25 150 0
TABLE 3
Activated Carbon Usage (mg) Cellulose Fiber Usage (mg) Residual Limonene (wt%)
0 0 One
0 25 0.5
150 0 0.55
25 150 0
실시예 5Example 5
각각의 실시예 1 내지 4로부터 리모넨의 성분이 0.025중량% 미만으로 제거된 당화액을 이용하여 바이오 에탄올을 제조하였다. 이때 균주는 공지되어 있는 Saccharomyces cerevisiae를 이용하여, PH는 5.0으로 유지하였으며, rpm200의 조건으로 30의 발효조에서 발효공정을 수행하여, 바이오에탄올을 수득하였다. Bioethanol was prepared from the saccharification liquid from which the components of limonene were removed from each of Examples 1 to 4 by less than 0.025% by weight. At this time, the strain using a known Saccharomyces cerevisiae , the pH was maintained at 5.0, the fermentation process was carried out in a fermentation tank of 30 under the conditions of rpm 200, to obtain a bioethanol.
실험예 1Experimental Example 1
리모넨의 발효 저해 현상을 확인하기 위하여 리모넨을 0.5중량% 함유하고 있는 당화액과 본 발명의 리모넨 제거방법으로 리모넨이 0.025중량% 미만으로 제거된 당화액을 이용하여, 각각 실시예 4에서 수행된 바와 같은 동일한 조건에서 에탄올로 전환되는 발효 공정을 수행하였고, 그 결과를 도 3에 도시하였다. 그 결과 0.5중량%의 리모넨을 함유하고 있는 당화액은 발효율이 최대 48%를 보이고 있으나, 리모넨이 0.025중량% 미만으로 제거된 당화액은 91%의 발효율을 보였다. 이 결과로부터 리모넨이 발효 저해 현상을 발생시키는 것을 확인할 수 있으며, 본 발명의 리모넨 제거방법으로 발효 효율을 향상시킬 수 있음을 확인할 수 있다. In order to confirm the inhibition of limonene fermentation using a saccharification solution containing 0.5% by weight of limonene and a saccharification solution in which limonene was removed to less than 0.025% by weight according to the limonene removal method of the present invention, Under the same conditions, a fermentation process for conversion to ethanol was performed, and the results are shown in FIG. 3. As a result, the saccharified solution containing limonene of 0.5% by weight showed the maximum efficiency of 48%, but the saccharified liquid removed to less than 0.025% by weight of limonene showed 91%. From this result, it can be confirmed that limonene causes a fermentation inhibition phenomenon, and it can be confirmed that the fermentation efficiency can be improved by the limonene removal method of the present invention.
본 발명은 이상에서 살펴본 바와 같이 바람직한 실시 예를 들어 도시하고 설명하였으나, 상기한 실시 예에 한정되지 아니하며 본 발명의 정신을 벗어나지 않는 범위 내에서 당해 발명이 속하는 기술분야에서 통상의 지식을 가진 자에 의해 다양한 변경과 수정이 가능할 것이다.Although the present invention has been shown and described with reference to preferred embodiments as described above, it is not limited to the above-described embodiments and those skilled in the art without departing from the spirit of the present invention. Various changes and modifications will be possible.

Claims (7)

  1. 리모넨이 함유된 바이오매스로부터 얻어진 당화액을 준비하는 단계; 및Preparing a saccharified solution obtained from limonene-containing biomass; And
    상기 당화액과 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상을 접촉시키는 단계를 포함하는 바이오매스 당화액의 리모넨 제거방법.Limonene removal method of the biomass saccharification liquid comprising the step of contacting any one or more of the saccharification liquid and activated carbon and cellulose fiber.
  2. 제 1항에 있어서,The method of claim 1,
    상기 접촉시키는 단계는 활성탄을 이용할 경우 상기 당화액의 리모넨 함량 0.8411g/cm3 기준으로 상기 활성탄이 0.3 내지 0.5g 사용되는 것을 특징으로 하는 바이오매스 당화액의 리모넨 제거방법.Wherein the step of contacting limonene removal of biomass saccharification liquid, characterized in that the activated carbon is used 0.3 to 0.5g based on the limonene content 0.8411g / cm3 of the saccharification liquid when using activated carbon.
  3. 제 1항에 있어서,The method of claim 1,
    상기 접촉시키는 단계는 셀룰로오스 파이버를 이용할 경우 상기 당화액의 리모넨 함량 0.8411g/cm3 기준으로 상기 셀룰로오스 파이버가 0.125 내지 0.2g 사용되는 것을 특징으로 하는 바이오매스 당화액의 리모넨 제거방법.Wherein the step of contacting limonene removal of biomass saccharification liquid, characterized in that when using a cellulose fiber, the cellulose fiber is used 0.125 to 0.2g based on the limonene content 0.8411g / cm3 of the saccharified solution.
  4. 리모넨 함량이 0.025중량% 미만인 것을 특징으로 하는 리모넨 함유 바이오매스로부터 얻어진 당화액.A saccharified liquid obtained from a limonene-containing biomass, wherein the limonene content is less than 0.025% by weight.
  5. 내부에 중공이 형성된 하우징; 및A hollow housing formed therein; And
    상기 중공에 일정 두께로 삽입되는 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상을 포함하는 리모넨 제거 장치.Limonene removal device comprising any one or more of activated carbon and cellulose fiber inserted into the hollow at a predetermined thickness.
  6. 제 5항에 있어서,The method of claim 5,
    상기 활성탄 및 셀룰로오스 파이버 중 어느 하나 이상은 리모넨 함유 바이오매스로부터 얻어진 당화액과 접촉되어 리모넨이 제거되는 것을 특징으로 하는 리모넨 제거 장치.At least one of the activated carbon and cellulose fiber is in contact with the saccharified liquid obtained from limonene-containing biomass, limonene removal apparatus characterized in that the removal of limonene.
  7. 제 1항 내지 제 3항 중 어느 한 항의 리모넨 제거방법이 수행된 당화액을 준비하는 단계; 및 Preparing a saccharified solution in which the limonene removing method of claim 1 is performed; And
    상기 당화액에 효모 및 이콜라이 중 어느 하나 이상을 이용하여 발효시키는 발효단계를 포함하는 것을 특징으로 하는 바이오에탄올 제조방법.Bioethanol production method comprising the step of fermentation using any one or more of yeast and E. coli in the saccharification liquid.
PCT/KR2014/007693 2013-08-22 2014-08-19 Method for removing limonene and device for removing limonene in biomass saccharification liquid, and bioethanol production method using the removal method WO2015026138A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201480046589.7A CN105473621A (en) 2013-08-22 2014-08-19 Method for removing limonene and device for removing limonene in biomass saccharification liquid, and bioethanol production method using the removal method

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020130099680A KR101498213B1 (en) 2013-08-22 2013-08-22 Method for removing limonene of saccharification liquid from biomass, Apparatus of removing limonene and Method for the production of bio-ethanol using the same
KR10-2013-0099680 2013-08-22

Publications (1)

Publication Number Publication Date
WO2015026138A1 true WO2015026138A1 (en) 2015-02-26

Family

ID=52483863

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2014/007693 WO2015026138A1 (en) 2013-08-22 2014-08-19 Method for removing limonene and device for removing limonene in biomass saccharification liquid, and bioethanol production method using the removal method

Country Status (3)

Country Link
KR (1) KR101498213B1 (en)
CN (1) CN105473621A (en)
WO (1) WO2015026138A1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19980071950A (en) * 1998-07-07 1998-10-26 노경호 Extraction and Separation of Peryl alcohol and D-limonene from Korean Tangerine Peel
KR100318755B1 (en) * 1999-12-24 2001-12-28 손재익 Process for producing ethanol with high concentration from wood hydrolysate using low-temperature sterilization
JP2002336000A (en) * 2001-05-21 2002-11-26 Kurita Water Ind Ltd Purification apparatus for sugar liquid
JP2010094093A (en) * 2008-10-17 2010-04-30 National Institute Of Advanced Industrial Science & Technology Method for producing ethanol from hull of citrus

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1199400B (en) * 1984-07-03 1988-12-30 Aid Agricolture Ind Dev PROCEDURE FOR THE EXTRACTION OF LIMONINA AND LIMONOIC ACID FROM CITRUS JUICES
JPH05328915A (en) * 1992-06-01 1993-12-14 Teijin Ltd Method for removing limonin
KR100555225B1 (en) * 2004-03-31 2006-03-03 김문갑 A method of alleviating stench of cleansing agent including dichloropropane
US8252566B2 (en) * 2008-05-20 2012-08-28 Jj Florida Properties Llc Ethanol production from citrus waste through limonene reduction
BRPI0908634A2 (en) * 2008-05-20 2016-08-30 Jj Florida Properties Llc method for producing ethanol from citrus residues
WO2013063251A1 (en) * 2011-10-26 2013-05-02 Frito-Lay North America, Inc. Sustainable conversion of citrus peel waste

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19980071950A (en) * 1998-07-07 1998-10-26 노경호 Extraction and Separation of Peryl alcohol and D-limonene from Korean Tangerine Peel
KR100318755B1 (en) * 1999-12-24 2001-12-28 손재익 Process for producing ethanol with high concentration from wood hydrolysate using low-temperature sterilization
JP2002336000A (en) * 2001-05-21 2002-11-26 Kurita Water Ind Ltd Purification apparatus for sugar liquid
JP2010094093A (en) * 2008-10-17 2010-04-30 National Institute Of Advanced Industrial Science & Technology Method for producing ethanol from hull of citrus

Also Published As

Publication number Publication date
CN105473621A (en) 2016-04-06
KR101498213B1 (en) 2015-03-06
KR20150023104A (en) 2015-03-05

Similar Documents

Publication Publication Date Title
Battista et al. Selection of the best pretreatment for hydrogen and bioethanol production from olive oil waste products
Nollet et al. Effect of 2-bromoethanesulfonic acid and Peptostreptococcus productus ATCC 35244 addition on stimulation of reductive acetogenesis in the ruminal ecosystem by selective inhibition of methanogenesis
Yang et al. Pretreatment of grass waste using combined ionizing radiation-acid treatment for enhancing fermentative hydrogen production
Juárez et al. Saccharification of microalgae biomass obtained from wastewater treatment by enzymatic hydrolysis. Effect of alkaline-peroxide pretreatment
Kumari et al. Biologically pretreated sugarcane top as a potential raw material for the enhancement of gaseous energy recovery by two stage biohythane process
DE602005024918D1 (en)
TW200641130A (en) Production of polyunsaturated fatty acids using novel cell treatment method
Liang et al. Effect of substrate load on anaerobic fermentation of rice straw with rumen liquid as inoculum: Hydrolysis and acidogenesis efficiency, enzymatic activities and rumen bacterial community structure
CN101560488A (en) Enzyme and microbial inoculum for decomposing lignocellulose
BRPI0819896B1 (en) PROCESS TO CONVERT VEGETABLE MATERIAL DERIVED FROM A ARACACEAE SP. Containing manana in an alcohol
WO2013018960A1 (en) Method for preparing volatile fatty acids using extracts of pre-treated seaweed residues
JP2008043328A (en) Method for saccharifying wood-based biomass
RU2010122502A (en) OBTAINING BIOLOGICAL FUEL USING PENICILLIUM FUNICULOSUM ENZYMES
WO2015026138A1 (en) Method for removing limonene and device for removing limonene in biomass saccharification liquid, and bioethanol production method using the removal method
CN106418322B (en) A kind of method of soluble dietary fibre content in raising apple pomace
JP2009291154A (en) Method for producing bio-ethanol
US20170107632A1 (en) Method, container and uses for converting biomass materials into soluble substances by one-step
JP2012179021A (en) Method for producing ethanol from waste
Liang et al. Metagenomic analysis reveals the efficient digestion mechanism of corn stover in Angus bull rumen: microbial community succession, CAZyme composition and functional gene expression
KR20110095662A (en) Preparation methods of sugar from sea algae by plasma treatment and preparation methods of bio-fuel using thereof
WO2010068054A2 (en) Method for preparing bioalcohol ingredient having low concentration of toxic materials from red algae and method for producing bioalcohol through the same
WO2010068053A2 (en) Method for preparing methane gas using red algae extract
WO2010008189A2 (en) Method for preparing bio-ethanol
CN108531516B (en) Comprehensive utilization method of water lettuce
CN109537065B (en) Biological degumming device and degumming method for ramie

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 201480046589.7

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 14837451

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 14837451

Country of ref document: EP

Kind code of ref document: A1