WO2010068053A2 - Method for preparing methane gas using red algae extract - Google Patents

Method for preparing methane gas using red algae extract Download PDF

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WO2010068053A2
WO2010068053A2 PCT/KR2009/007412 KR2009007412W WO2010068053A2 WO 2010068053 A2 WO2010068053 A2 WO 2010068053A2 KR 2009007412 W KR2009007412 W KR 2009007412W WO 2010068053 A2 WO2010068053 A2 WO 2010068053A2
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red algae
algae extract
methane gas
extract
methane
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PCT/KR2009/007412
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French (fr)
Korean (ko)
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WO2010068053A3 (en
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유학철
서영범
최우영
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(주)페가서스인터내셔날
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Publication of WO2010068053A3 publication Critical patent/WO2010068053A3/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/02Biological treatment
    • C02F11/04Anaerobic treatment; Production of methane by such processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/286Anaerobic digestion processes including two or more steps
    • 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
    • C12P5/00Preparation of hydrocarbons or halogenated hydrocarbons
    • C12P5/02Preparation of hydrocarbons or halogenated hydrocarbons acyclic
    • C12P5/023Methane
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/26Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof
    • C02F2103/28Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof from the paper or cellulose industry
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/32Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
    • 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
    • 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
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing

Definitions

  • the present invention uses the red algae extract generated in the pulp production process using red algae for the production of methane gas. Specifically, the present invention comprises the steps of (a) hydrolyzing the red algae extract; (b) removing impurities of the red algae extract which passed through step (a); (c) The method of directly producing methane gas from red algae extract comprising the step of fermenting methane using the methane fermentation of the extract after the step (b).
  • Methane is the simplest carbon compound and has a structure in which four hydrogens are bonded to one carbon, and exist in the form of a gas at room temperature. Methane gas itself is odorless, but for industrial use, some odors are mixed to make it easier to detect leaks. Such methane gas is produced through the methane fermentation process. Methane fermentation occurs as anaerobic bacteria break down organic matter, producing methane and carbon dioxide. Methane fermentation has been used for the treatment of manure and industrial waste. Recently, attempts have been made to use the methane gas collected through the fermentation of methane produced during the treatment of manure or industrial waste.
  • Korean Unexamined Patent Publication No. 1997-0069903 discloses a device for obtaining methane gas from organic wastewater
  • Korean Unexamined Patent Publication No. 1999-0083953 discloses a method and device for methane gasification of household waste and animal carcasses.
  • Republic of Korea Patent Publication No. 2000-0001131 Livestock waste food waste purification and methane gas extraction device
  • methane fermentation requires organic materials that can be used as substrates by anaerobic bacteria that methane fermentation, and the range of these organic materials can be considered in various ways, as described above.
  • Use as a substrate for fermentation would be desirable when considering aspects of efficient use of resources.
  • Red algae inhabit relatively deeper water than other algae, and are relatively small in size. There are more than 4,000 species, and the algae grow wider than green algae and brown algae, and grow from shallow depths to deep water rays. Republic of Korea Patent No. 0811193 discloses "pulp made of red algae and its manufacturing method".
  • the patent goes through the steps of washing red algae, oxygen pretreatment, extracting the gel components of red algae to produce pulp from red algae, which is a gel component and low-molecular-weight carbohydrates, such as ummu and carrageenan present in the algae
  • red algae is composed of pulp fibers
  • it is a step for treating this because it causes problems such as increasing drug consumption and preventing dehydration.
  • the gel component (woom; also called agar or Agar), which is a constituent of red algae, may be extracted from red algae according to the characteristics of the paper to be manufactured, and then paper may be produced. You may. The higher the content of the gel component can produce a paper with high transparency and density, the lower the content of the gel component can produce a paper with high opacity and excellent bonding. In other words, this is a part that can be adjusted by the manufacturer according to the needs of the consumer, in any case, the gel component extracted from the red algae is bound to be discarded.
  • the gel component of radish has been used for food or medicine for a long time, but the gel component of radish, which is a waste generated in the process of preparing pulp from red algae, goes through a washing step and a bleaching step. There was a limit to use, and it has been required to derive its use.
  • the present inventors first developed a method for producing red algae into pulp, and as a inventor of a source patent registered and patented, the red algae after researching to produce methane gas using the gel extract extracted in the process of manufacturing the red algae into pulp The methane gas production method using the extract was completed.
  • an object of the present invention is to regenerate resources that are discarded as the methane gas is produced using the gel extract generated during the manufacture of pulp from red algae.
  • the present invention provides a method of directly producing methane gas from red algae extract and a method of producing methane gas using ethanol from the red algae extract and the remaining distillation waste.
  • the method of directly producing methane gas from the red algae extract includes the steps of: (a) hydrolyzing the red algae extract; (b) removing impurities of the red algae extract which passed through step (a); (c) methane fermentation using the methane fermentation of the extract after the step (b).
  • Red algae extract used in the present invention can be obtained using the method described in the existing Korean Patent No. 0811193 and the like by the present inventors. First, the red algae may be immersed in an acidic aqueous solution to remove impurities and calcium carbonate, and then the red algae may be immersed in an extraction solvent capable of dissolving the red algae gel component. In the present invention, such red algae extract gel components will be referred to as red algae extract. Red algae extract refers to a daikon (agar, also called agar) present in red algae.
  • the red algae extract having undergone this process, is subjected to (a) hydrolysis step.
  • the hydrolysis step is to bring the red algae extract into a reducing sugar state that is suitable for methane fermentation as a substrate.
  • hydrolysis may be considered hydrolysis using an acid or an enzyme, but in the present invention, an acid hydrolysis method is used.
  • the acid may preferably be oxalic acid, sulfuric acid, phosphoric acid, and particularly, in the case of oxalic acid, it is preferable to proceed in an environment having a temperature of 130 to 140 ° C and a pH of 3.0 or less.
  • the hydrolysis is preferably carried out for 1 to 2 atm, for 30 to 60 minutes.
  • the red algae extract that passed through step (a) is subjected to an impurity treatment step (b).
  • the impurity treatment step is characterized by consisting of an air blowing step and an alkali treatment step.
  • the air blowing step is a step for removing furfural which is a fermentation blockage generated in the acid hydrolysis step (a).
  • the air blowing step is preferably carried out by blowing the steam of 95 ⁇ 105 °C.
  • Alkali treatment step is to remove the hydroxy methyl furfural (Hydroxy Methyl Furfural) as the air blowing step.
  • the alkali treatment step it is preferable to use chemicals such as calcium oxide, sodium hydroxide, potassium hydroxide, etc. to maintain the environment of pH 10 ⁇ 10.5.
  • the red algae extract of step (b) is a state in which methane fermentation bacteria have been changed into a form of reducing sugar which is good for use as a substrate, and furfural and hydroxy methyl furfural, which are obstacles to fermentation, have been removed.
  • methane fermentation may use a general methane fermentation tank.
  • a fermentation tank that is sufficiently mixed with the temperature range of 10 ⁇ 40 °C and circulation.
  • Methane fermentation bacteria is not particularly limited and is a mesophilic archaea Methanobacterium bryantii , Methanococcus vannielii , Methanosarcina mazei And thermophilic archaea Methanobacterium thermoformicicum , Methanothermus fervidus , Methanosarcina thermophila All methane fermentation bacteria, including
  • a method of producing methane gas using the remaining distillation waste after producing ethanol from the red algae extract comprises the steps of: (a) hydrolyzing the red algae extract; (b) removing impurities of the red algae extract which passed through step (a); (c) pH neutralization step of the red algae extract that passed through step (b); (d) judo inoculation to the red algae extract that passed through the step (c); (e) alcohol fermenting the red algae extract having undergone the step (d); (f) distilling the alcohol fermentation broth from step (e) to recover ethanol; (g) The step of (m) recovering the ethanol and the remaining distillation waste consists of methane fermentation using methane fermentation bacteria.
  • the red algae extract may be obtained using a method described in Korean Patent No. 0811193, which is an existing registered patent by the present inventors, and the like. Such extracts may preferably undergo a "concentration step" before the hydrolysis step corresponding to step (a). Concentration step is preferably evaporation concentration using a temperature of 100 ⁇ 160 °C the temperature when the red algae extract comes out of the extractor. When the concentration step is performed using the temperature of the red algae extract from the extractor, it is possible to obtain an effect of reducing energy consumption in the distillation process in the ethanol production process.
  • hydrolysis step (b) impurity treatment step, which is the same as the method for producing methane gas directly from the red algae extract described above.
  • impurity treatment step ammonium hydroxide and magnesium hydroxide may be added to supply the essential nutrients necessary for the strain.
  • the step of neutralizing the pH of the red algae extract through the above steps is to create an environment in the pH range 5.5 to 6.5 in which alcohol fermentation can be made properly.
  • the acid used herein is not limited to a specific acid as long as the acid can adjust the pH range of the red algae extract that has undergone the impurity treatment to the range of 5.5 to 6.5.
  • the strain used for this is preferably Saccharomyces cerevisiae Can be used in pre-culture, but Saccharomyces cerevisiae on Without limitation, any microorganism which ferments alcohol can be used.
  • the alcohol fermentation step may be proceeded as anaerobic effect tablets, preferably at 30 ° C. for 5 to 7 days.
  • a distillation waste solution is obtained. This can be used as a substrate of methane fermentation.
  • Methane gas can be produced using methane fermentation bacteria in the same way as the method discussed above.
  • waste products can be efficiently recycled as fuel by reproducing by-products generated by producing pulp from red algae as methane gas. Will be. It is environmentally friendly and methane gas produced by this method can be used for transportation, heating, and natural gas for power generation.
  • FIG. 1 is a schematic diagram of a process for producing methane gas from red algae extract according to the present invention.
  • the red starfish a type of red algae, was immersed in an acidic solution at pH 2-3 for 55 minutes to remove impurities and calcium carbonate mixed in the algae.
  • the pH of the acid solution was adjusted using hydrochloric acid and the temperature was 20 °C.
  • 10 kg of whole loaf of wormwood that is, the weight of 10 kg when completely dried, was immersed in an aqueous sodium hydroxide solution containing 4% by weight of sodium hydroxide compared to the whole lodge, and then treated for 90 minutes in a 120 °C water bath. . After the treatment of the water bath at 40 ° C.
  • the red algae extract extracted by treating in this way is low molecular weight in the extraction process to maintain the liquid state at room temperature.
  • the red algae extract extracted in the above step was hydrolyzed with oxalic acid at 1.5 atmosphere for 50 minutes. 6.2 kg of red algae extracts were obtained, and the hydrolysis resulted in 3.5 kg of reducing sugars.
  • the red algae extract which has undergone the step of removing impurities, is added to CSTR (Continous Stirrer Tank Reactor), a R-201 series reactor system manufactured by Reaction Engineering Co., Ltd. Methanococcus vannielii 3.85m of methane-coated tablets under standard temperature and pressure conditions after inoculating strains 3 Methane gas was obtained.
  • CSTR Continuous Stirrer Tank Reactor
  • Methanol gas is produced by using ethanol from red algae extract and distillation waste.
  • the red starfish a type of red algae, was immersed in an acidic solution at pH 2-3 for 55 minutes to remove impurities and calcium carbonate mixed in the algae.
  • the pH of the acid solution was adjusted using hydrochloric acid and the temperature was 20 °C.
  • 10 kg of whole loaf of wormwood that is, the weight of 10 kg when completely dried, was immersed in an aqueous sodium hydroxide solution containing 4% by weight of sodium hydroxide compared to the whole lodge, and then treated for 90 minutes in a 120 °C water bath. . After the treatment of the water bath at 40 ° C.
  • the red algae extract extracted by treating in this way is low molecular weight in the extraction process to maintain the liquid state at room temperature.
  • the red algae extract extracted in the above step was hydrolyzed with oxalic acid at 1.5 atmosphere for 50 minutes. 6.2 kg of red algae extracts were obtained, and the hydrolysis resulted in 3.5 kg of reducing sugars.
  • Phosphoric acid was added to the red algae extract after the impurity removal step to adjust the pH to 5.7.
  • Saccharomyces cerevisiae Precultured 2 ⁇ 10 -7 cfu ml - One At the level of it was inoculated into the red algae extract.

Abstract

The present invention relates to use of a red algae extract for preparing methane gas, generated during a pulp manufacturing process using red algae. More specifically, the present invention provides a method for directly preparing methane gas from red algae extract and a method for preparing methane gas using distillery wastewater remaining after ethanol preparation from red algae. The direct method for preparing the methane gas comprises: (a) a step of hydrolyzing red algae extract; (b) a step of removing impurities from red algae extract from step (a); and (c) a step of performing methane fermentation of the extract obtained through step (b) using methane-fermenting fungi. The other method for preparing methane gas using distillery wastewater comprises: (a) a step of hydrolyzing red algae extract; (b) a step of removing impurities from red algae extract from step (a); (c) a step of neutralizing the pH of red algae extract obtained through step (b); (d) a step of inoculating distiller's yeast to red algae extract from step (c); (e) a step of performing alcohol fermentation of red algae extract from step (d); (f) a step of distilling alcohol fermentation liquid obtained through step (e) and collecting ethanol; and (g) a step of performing methane fermentation of distillery wastewater remaining after collecting the ethanol from step (f) using methane-fermenting fungi.

Description

홍조류 추출물을 이용한 메탄가스 생산방법Methane gas production method using red algae extract
본 발명은 홍조류를 이용한 펄프 생산공정에서 발생된 홍조류 추출물을 메탄가스의 생산에 이용하는 것이다. 구체적으로 본 발명은 (a)홍조류 추출물을 가수분해하는 단계; (b)상기 (a)단계를 거친 홍조류 추출물의 불순물을 제거하는 단계; (c)상기 (b)단계를 거친 추출물을 메탄발효균을 이용하여 메탄발효하는 단계를 포함하는 홍조류 추출물로부터 메탄가스를 직접적으로 생산하는 방법에 대한 것이다.The present invention uses the red algae extract generated in the pulp production process using red algae for the production of methane gas. Specifically, the present invention comprises the steps of (a) hydrolyzing the red algae extract; (b) removing impurities of the red algae extract which passed through step (a); (c) The method of directly producing methane gas from red algae extract comprising the step of fermenting methane using the methane fermentation of the extract after the step (b).
메탄은 가장 간단한 탄소 화합물로, 탄소 하나에 수소 4개가 결합되어 있는 구조를 취하고 있으며, 상온에서 기체의 형태로 존재한다. 메탄가스는 그 자체로는 냄새가 없지만, 산업용으로 사용할 때에는 누출을 발견하기 쉽게 하기 위해 약간의 냄새를 섞기도 하며, 이와 같은 메탄가스는 메탄발효공정을 통해 생성된다. 메탄발효는 혐기성 세균이 유기물을 분해하는 과정으로 일어나는데, 이 과정에서 메탄과 이산화탄소가 생성된다. 메탄발효는 분뇨나 산업폐기물의 처리에 이용되어 왔는데, 최근에는 분뇨나 산업폐기물의 처리과정에서 일어나는 메탄발효를 통해 포집된 메탄가스를 연료로 사용하려는 시도가 이루어지고 있다.Methane is the simplest carbon compound and has a structure in which four hydrogens are bonded to one carbon, and exist in the form of a gas at room temperature. Methane gas itself is odorless, but for industrial use, some odors are mixed to make it easier to detect leaks. Such methane gas is produced through the methane fermentation process. Methane fermentation occurs as anaerobic bacteria break down organic matter, producing methane and carbon dioxide. Methane fermentation has been used for the treatment of manure and industrial waste. Recently, attempts have been made to use the methane gas collected through the fermentation of methane produced during the treatment of manure or industrial waste.
대한민국 공개특허 제1997-0069903호에는 "유기폐수로부터 메탄가스를 수득하는 장치"가 개시되어 있으며, 대한민국 공개특허 제1999-0083953호에는 "생활쓰레기 및 동물사체의 메탄가스화 방법 및 장치"가 개시되어 있고, 대한민국 공개특허 제2000-0001131호에는 "축산물 폐기물 음식물쓰레기 정화 및 메탄가스추출 장치"가 개시되어 있으며, 이와 관련된 기술은 현재까지 지속적으로 개발되고 있는 상태이다.Korean Unexamined Patent Publication No. 1997-0069903 discloses a device for obtaining methane gas from organic wastewater, and Korean Unexamined Patent Publication No. 1999-0083953 discloses a method and device for methane gasification of household waste and animal carcasses. In addition, the Republic of Korea Patent Publication No. 2000-0001131 "Livestock waste food waste purification and methane gas extraction device" is disclosed, and the related technology has been continuously developed to date.
이와 같이 메탄발효는 메탄발효를 하는 혐기성 세균이 기질로 사용할 수 있는 유기물을 필요로 하는데, 이러한 유기물의 범위는 다양하게 고려될 수 있으며, 상기에서 살핀 바와 같이 더 이상 자원으로 사용하기 곤란한 폐기물을 메탄발효의 기질로서 사용하는 것이 자원의 효율적 이용 측면을 고려할 때 바람직할 것이다.As such, methane fermentation requires organic materials that can be used as substrates by anaerobic bacteria that methane fermentation, and the range of these organic materials can be considered in various ways, as described above. Use as a substrate for fermentation would be desirable when considering aspects of efficient use of resources.
최근 홍조류를 이용하여 생산된 펄프로서 종이를 생산하는 방법이 개발되었고, 이의 산업화가 활발하게 시도되고 있다. 홍조류는 다른 조류보다 비교적 깊은 물에 서식하고, 크기가 비교적 작으며, 종류는 4000여 종으로 매우 다양하며 녹조류, 갈조류보다 서식 범위가 넓어 얕은 수심에서부터 광선이 닿는 깊은 수심에까지 자생한다. 대한민국 등록특허 제0811193호는 "홍조류로 제조된 펄프 및 그 제조방법"을 개시하고 있다. 상기 특허는 홍조류로부터 펄프를 제조하기 위하여 홍조류를 세척하는 단계, 산소 전처리하는 단계, 홍조류의 젤 성분을 추출하는 단계를 거치는데, 이는 홍조류 내부에 존재하는 우무나 카라기난 등의 젤성분 및 저분자량 탄수화물이 홍조류가 펄프섬유로 구성될 때 약품소비를 증가시키고 탈수를 방해하는 등의 문제점을 발생시키므로 이를 처리하기 위한 단계이다. Recently, a method of producing paper as pulp produced using red algae has been developed, and industrialization thereof has been actively attempted. Red algae inhabit relatively deeper water than other algae, and are relatively small in size. There are more than 4,000 species, and the algae grow wider than green algae and brown algae, and grow from shallow depths to deep water rays. Republic of Korea Patent No. 0811193 discloses "pulp made of red algae and its manufacturing method". The patent goes through the steps of washing red algae, oxygen pretreatment, extracting the gel components of red algae to produce pulp from red algae, which is a gel component and low-molecular-weight carbohydrates, such as ummu and carrageenan present in the algae When the red algae is composed of pulp fibers, it is a step for treating this because it causes problems such as increasing drug consumption and preventing dehydration.
이와 같이 홍조류 내부의 구성물질인 젤성분(우무;한천 또는 Agar로 칭하기도 함)는 제조하고자 하는 종이의 특성에 따라 홍조류로부터 모두 추출한 후 종이를 제조할 수도 있으며, 일부 존재하는 상태에서 종이를 제조할 수도 있다. 젤성분의 함량이 높을수록 투명도와 밀도가 높은 종이를 제조할 수 있고, 젤성분 함량이 낮을수록 불투명도가 높고 지합이 우수한 종이를 제조할 수 있다. 즉, 이는 수요자의 요구에 따라 제조자가 조절할 수 있는 부분이지만, 어느 경우에 있어서나 홍조류로부터 추출된 젤성분은 폐기될 수밖에 없다. As such, the gel component (woom; also called agar or Agar), which is a constituent of red algae, may be extracted from red algae according to the characteristics of the paper to be manufactured, and then paper may be produced. You may. The higher the content of the gel component can produce a paper with high transparency and density, the lower the content of the gel component can produce a paper with high opacity and excellent bonding. In other words, this is a part that can be adjusted by the manufacturer according to the needs of the consumer, in any case, the gel component extracted from the red algae is bound to be discarded.
이와 같이 홍조류로부터 펄프를 제조할 경우, 목재펄프를 사용하는 경우 원료 목재의 구입에 드는 비용에 비하여 생산비용이 저렴하고 리그닌 제거 및 표백을 위한 화학약품 등의 사용이 현저히 감소 되는바 환경오염을 방지할 수 있고, 최종 제품 또한 유해 화학 약품을 함유하지 아니하여 인체와 환경에 무해한 제품을 생산할 수 있는 장점이 있으나, 상기에서 살핀 바와 같이 그 과정에서 발생된 젤성분이 폐기될 수밖에 없는 문제점이 있었다.As such, when pulp is produced from red algae, the production cost is lower than the cost of purchasing raw timber, and the use of chemicals for lignin removal and bleaching is significantly reduced compared to the cost of purchasing raw wood. It can be, and the final product also does not contain harmful chemicals, there is an advantage to produce a product that is harmless to the human body and the environment, but as described above, there was a problem that the gel component generated in the process must be discarded.
물론 상기 젤성분인 우무는 예로부터 음식이나 약 등 식용으로 사용하여 왔으나, 상기와 같이 홍조류로부터 펄프를 제조하는 과정에서 발생 되는 폐기물인 젤성분 우무는 세척단계, 표백단계를 거치게 되는바 이를 식용으로 사용하기에는 한계가 있었고, 이의 활용방안 도출이 요구되어 왔다.Of course, the gel component of radish has been used for food or medicine for a long time, but the gel component of radish, which is a waste generated in the process of preparing pulp from red algae, goes through a washing step and a bleaching step. There was a limit to use, and it has been required to derive its use.
본 발명자들은 홍조류를 펄프로 제조하는 방법을 최초로 개발하고 이를 특허출원하여 등록받은 원천 특허의 발명자들로서 상기 홍조류를 펄프로 제조하는 과정에서 추출된 젤 추출물을 이용하여 메탄가스를 생산하고자 연구한 끝에 홍조류 추출물을 이용한 메탄가스 생산방법을 완성하였다. The present inventors first developed a method for producing red algae into pulp, and as a inventor of a source patent registered and patented, the red algae after researching to produce methane gas using the gel extract extracted in the process of manufacturing the red algae into pulp The methane gas production method using the extract was completed.
즉, 본 발명은 홍조류로부터 펄프를 제조하는 과정에서 발생 되는 젤 추출물을 이용하여 메탄가스를 생산하게 됨에 따라 폐기되는 자원을 재생하는 것을 목적으로 한다.That is, an object of the present invention is to regenerate resources that are discarded as the methane gas is produced using the gel extract generated during the manufacture of pulp from red algae.
상기 목적을 달성하기 위하여 본 발명은 홍조류 추출물로부터 메탄가스를 직접적으로 생산하는 방법 및 홍조류 추출물로부터 에탄올을 생산하고 남은 증류폐액을 이용하여 메탄가스를 생산하는 방법을 제공한다.In order to achieve the above object, the present invention provides a method of directly producing methane gas from red algae extract and a method of producing methane gas using ethanol from the red algae extract and the remaining distillation waste.
1. 홍조류로부터 메탄가스를 직접적으로 생산하는 방법1. Method of producing methane gas directly from red algae
먼저, 홍조류 추출물로부터 메탄가스를 직접적으로 생산하는 방법은 (a)홍조류 추출물을 가수분해하는 단계; (b)상기 (a)단계를 거친 홍조류 추출물의 불순물을 제거하는 단계; (c)상기 (b)단계를 거친 추출물을 메탄발효균을 이용하여 메탄발효하는 단계로 이루어진다.First, the method of directly producing methane gas from the red algae extract includes the steps of: (a) hydrolyzing the red algae extract; (b) removing impurities of the red algae extract which passed through step (a); (c) methane fermentation using the methane fermentation of the extract after the step (b).
본 발명에 사용되는 홍조류 추출물은 본 발명자들에 의한 기존 대한민국 등록특허 제0811193호 등에 기재된 방법 등을 이용하여 얻을 수 있다. 먼저 홍조류를 산성수용액에 침지시켜 불순물과 탄산칼슘을 제거하고, 이를 홍조류의 젤성분을 용해시킬 수 있는 추출용매에 침지하여 젤성분을 추출할 수 있다. 본 발명에서는 이와 같은 홍조류 추출 젤성분을 홍조류 추출물이라 칭하기로 한다. 홍조류 추출물이란 홍조류 내부에 존재하는 우무(아가, 한천이라고도 칭함)성분을 의미한다. Red algae extract used in the present invention can be obtained using the method described in the existing Korean Patent No. 0811193 and the like by the present inventors. First, the red algae may be immersed in an acidic aqueous solution to remove impurities and calcium carbonate, and then the red algae may be immersed in an extraction solvent capable of dissolving the red algae gel component. In the present invention, such red algae extract gel components will be referred to as red algae extract. Red algae extract refers to a daikon (agar, also called agar) present in red algae.
이와 같은 과정을 거친 홍조류 추출물은 (a)가수분해 단계를 거치게 된다. 가수분해 단계는 홍조류 추출물인 우무를 메탄발효균이 기질로서 이용하기에 적절한 형태인 환원당 상태로 만들어 주기 위해서이다. 일반적으로 가수분해는 산 또는 효소를 이용한 가수분해를 고려할 수 있으나, 본 발명에서는 산가수분해 방법을 이용한다. 산은 바람직하게는 옥살산, 황산, 인산을 사용할 수 있으며, 특히 옥살산의 경우 130~140℃의 온도, pH 3.0 이하의 환경에서 진행하는 것이 바람직하다. 또한 상기 가수분해는 바람직하게는 1~2기압에서, 30~60분 동안 실시함이 바람직하다.The red algae extract, having undergone this process, is subjected to (a) hydrolysis step. The hydrolysis step is to bring the red algae extract into a reducing sugar state that is suitable for methane fermentation as a substrate. In general, hydrolysis may be considered hydrolysis using an acid or an enzyme, but in the present invention, an acid hydrolysis method is used. The acid may preferably be oxalic acid, sulfuric acid, phosphoric acid, and particularly, in the case of oxalic acid, it is preferable to proceed in an environment having a temperature of 130 to 140 ° C and a pH of 3.0 or less. In addition, the hydrolysis is preferably carried out for 1 to 2 atm, for 30 to 60 minutes.
상기 (a)단계를 거친 홍조류 추출물은 (b)단계인 불순물 처리단계를 거치게된다. 불순물 처리단계는 공기취입단계 및 알칼리 처리단계로 이루어지는 것을 특징으로 한다. 공기취입단계는 상기(a)단계인 산가수분해 단계에서 발생한 발효 방해물인 푸르푸랄(Furfural)을 제거하기 위한 단계이다. 상기 공기취입단계는 95~105℃의 수증기를 취입하여 진행하는 것이 바람직하다. The red algae extract that passed through step (a) is subjected to an impurity treatment step (b). The impurity treatment step is characterized by consisting of an air blowing step and an alkali treatment step. The air blowing step is a step for removing furfural which is a fermentation blockage generated in the acid hydrolysis step (a). The air blowing step is preferably carried out by blowing the steam of 95 ~ 105 ℃.
알칼리 처리 단계는 상기 공기취입단계와 마찬가지로 발효의 방해물인 하이드록시 메틸 푸르푸랄(Hydroxy Methyl Furfural)을 제거하기 위한 단계이다. 상기 알칼리 처리 단계는 pH 10~10.5의 환경을 유지시켜주기 위하여 산화칼슘, 수산화 나트륨, 수산화 칼륨 등의 약품을 사용하는 것이 바람직하다. Alkali treatment step is to remove the hydroxy methyl furfural (Hydroxy Methyl Furfural) as the air blowing step. In the alkali treatment step, it is preferable to use chemicals such as calcium oxide, sodium hydroxide, potassium hydroxide, etc. to maintain the environment of pH 10 ~ 10.5.
상기 (b)단계를 거친 홍조류 추출물은 메탄발효균이 기질로 이용하기 좋은 환원당의 형태로 변화된 상태이며, 발효의 방해물인 푸르푸랄(Furfural), 하이드록시 메틸 푸르푸랄(Hydroxy Methyl Furfural)이 제거된 상태로서 메탄발효단계인 (c)단계를 거치게 된다. 상기 메탄발효단계인 (c)단계는 일반적인 메탄 발효조를 이용할 수 있다. 바람직하게는 10~40℃의 온도범위와 내부혼합 및 순환이 충분히 이루어지는 발효조를 사용할 수 있다. 메탄발효균은 특별히 한정되지 아니하며, 중온성 고세균인 Methanobacterium bryantii , Methanococcus vannielii , Methanosarcina mazei 및 고온성 고세균인 Methanobacterium thermoformicicum , Methanothermus fervidus , Methanosarcina thermophila을 포함한 모든 메탄발효균을 이용할 수 있다The red algae extract of step (b) is a state in which methane fermentation bacteria have been changed into a form of reducing sugar which is good for use as a substrate, and furfural and hydroxy methyl furfural, which are obstacles to fermentation, have been removed. As it goes through the step (c) methane fermentation. The methane fermentation step (c) may use a general methane fermentation tank. Preferably it is possible to use a fermentation tank that is sufficiently mixed with the temperature range of 10 ~ 40 ℃ and circulation. Methane fermentation bacteria is not particularly limited and is a mesophilic archaeaMethanobacterium                                  bryantii                 ,                 Methanococcus                                  vannielii                 , Methanosarcina                 mazei                  And thermophilic archaea                 Methanobacterium                                  thermoformicicum                 , Methanothermus                 fervidus                 ,                 Methanosarcina                                  thermophilaAll methane fermentation bacteria, including
..
상기와 같은 (a),(b) 및 (c)단계를 통하여 홍조류 추출물로부터 메탄가스를 생산할 수 있다. It is possible to produce methane gas from the red algae extract through the steps (a), (b) and (c) as described above.
2. 홍조류 추출물로부터 에탄올을 생산하고 남은 증류폐액을 이용하여 메탄 가스를 생산하는 방법 2. Method of producing methane gas using the remaining distillation waste after producing ethanol from red algae extract
그 다음으로 홍조류 추출물로부터 에탄올을 생산하고 남은 증류폐액을 이용하여 메탄가스를 생산하는 방법은 (a)홍조류 추출물을 가수분해하는 단계; (b)상기 (a)단계를 거친 홍조류 추출물의 불순물을 제거하는 단계; (c)상기 (b)단계를 거친 홍조류 추출물의 pH중화 단계; (d)상기 (c)단계를 거친 홍조류 추출물에 주모접종을 하는 단계; (e)상기 (d)단계를 거친 홍조류 추출물을 알코올 발효하는 단계; (f)상기 (e)단계를 거친 알코올 발효액을 증류하여 에탄올을 회수하는 단계; (g)상기 (f)단계에서 에탄올을 회수하고 남은 증류폐액을 메탄발효균을 이용하여 메탄발효 하는 단계로 이루어진다. Next, a method of producing methane gas using the remaining distillation waste after producing ethanol from the red algae extract comprises the steps of: (a) hydrolyzing the red algae extract; (b) removing impurities of the red algae extract which passed through step (a); (c) pH neutralization step of the red algae extract that passed through step (b); (d) judo inoculation to the red algae extract that passed through the step (c); (e) alcohol fermenting the red algae extract having undergone the step (d); (f) distilling the alcohol fermentation broth from step (e) to recover ethanol; (g) The step of (m) recovering the ethanol and the remaining distillation waste consists of methane fermentation using methane fermentation bacteria.
홍조류 추출물은 상기에서 설명한 바와 같이 본 발명자들에 의한 기존 등록특허인 대한민국 등록특허 제0811193호 등에 기재된 방법 등을 이용하여 얻을 수 있다. 이와 같은 추출물은 바람직하게는 상기 (a)단계에 해당하는 가수분해 단계이전에 "농축단계"를 거칠 수 있다. 농축단계는 홍조류 추출물이 추출기에서 나올 때의 온도인 100~160℃의 온도를 이용하여 증발농축함이 바람직하다. 이와 같은 농축단계를 추출기에서 나온 홍조류 추출물의 온도를 이용하여 진행하게 되면, 이후 에탄올 생산과정에 있을 증류과정에 있어서의 에너지 소모를 감소시키는 효과를 얻을 수 있다.As described above, the red algae extract may be obtained using a method described in Korean Patent No. 0811193, which is an existing registered patent by the present inventors, and the like. Such extracts may preferably undergo a "concentration step" before the hydrolysis step corresponding to step (a). Concentration step is preferably evaporation concentration using a temperature of 100 ~ 160 ℃ the temperature when the red algae extract comes out of the extractor. When the concentration step is performed using the temperature of the red algae extract from the extractor, it is possible to obtain an effect of reducing energy consumption in the distillation process in the ethanol production process.
그 다음으로 (a)가수분해단계, (b)불순물처리단계를 거치게 되는데, 이는 상기에서 설명한 홍조류 추출물로부터 메탄가스를 직접적으로 생산하는 방법과 동일하다. 다만 바람직하게는 상기 (a)가수분해단계와 (b)불순물처리단계 사이 공정에서 수산화암모늄과 수산화마그네슘 등을 첨가하여 균주에 필요한 필수영양성분을 공급하는 공정을 추가할 수도 있다.It is then subjected to (a) hydrolysis step, (b) impurity treatment step, which is the same as the method for producing methane gas directly from the red algae extract described above. However, preferably, in the process between (a) hydrolysis step and (b) impurity treatment step, ammonium hydroxide and magnesium hydroxide may be added to supply the essential nutrients necessary for the strain.
그 다음으로 상기 단계를 거친 홍조류 추출물의 pH를 중화시키는 단계를 거치게 된다. 이는 알코올 발효가 적절하게 이루어질 수 있는 pH 5.5~6.5 범위의 환경을 만들어주기 위한 것이다. 이에 사용되는 산은 상기 불순물 처리단계를 거친 홍조류 추출물의 pH범위를 상기 5.5~6.5의 범위로 조정할 수 있는 산이라면 특정 산으로 그 종류가 제한되지 않는다.Then, the step of neutralizing the pH of the red algae extract through the above steps. This is to create an environment in the pH range 5.5 to 6.5 in which alcohol fermentation can be made properly. The acid used herein is not limited to a specific acid as long as the acid can adjust the pH range of the red algae extract that has undergone the impurity treatment to the range of 5.5 to 6.5.
그 다음으로 (d)주모접종단계를 거치게 된다. 이에 사용되는 균주는 바람직하게는 Saccharomyces cerevisiae를 전배양하여 사용할 수 있으나 반드시, Saccharomyces cerevisiae 한정되지 아니하고 알코올 발효를 하는 미생물이라면 어떠한 것이든 사용가능하다. Then, (d) the main vaccination step. The strain used for this is preferablySaccharomyces                                  cerevisiaeCan be used in pre-culture, butSaccharomyces                 cerevisiaeon Without limitation, any microorganism which ferments alcohol can be used.
그 다음으로 (e)알코올 발효단계는 혐기발효과정으로서 바람직하게는 30℃에서 5~7일간 진행할 수 있다. 상기 알코올 발효단계 이후에는 (f)알코올 발효액을 증류하여 에탄올을 회수하는 단계를 거친 후, 증류폐액을 얻게 된다. 이것이 메탄발효의 기질로서 사용될 수 있다. 상기에서 검토한 방법과 동일하게 메탄발효균을 이용하여 메탄가스를 생산할 수 있다.Next, (e) the alcohol fermentation step may be proceeded as anaerobic effect tablets, preferably at 30 ° C. for 5 to 7 days. After the alcohol fermentation step (f) after distilling the alcohol fermentation broth to recover ethanol, a distillation waste solution is obtained. This can be used as a substrate of methane fermentation. Methane gas can be produced using methane fermentation bacteria in the same way as the method discussed above.
살펴본 바와 같이 본 발명에 따른 홍조류 추출물로부터 메탄가스를 생산하는 방법발명을 실시할 경우, 홍조류로부터 펄프를 생산함에 따라 발생 된 부산물을 메탄가스로 재생산함에 따라 폐자원을 효율적으로 재생하여 연료로 사용할 수 있게 된다. 이는 친환경적이며 이러한 방법에 의해 생산된 메탄가스는 수송, 난방, 발전용 천연가스 등으로 사용할 수 있게 된다.As described above, when the method of producing methane gas from red algae extract according to the present invention is carried out, waste products can be efficiently recycled as fuel by reproducing by-products generated by producing pulp from red algae as methane gas. Will be. It is environmentally friendly and methane gas produced by this method can be used for transportation, heating, and natural gas for power generation.
도1은 본 발명에 따른 홍조류 추출물로부터 메탄가스를 생산하는 공정에 대한 모식도이다.1 is a schematic diagram of a process for producing methane gas from red algae extract according to the present invention.
실시예Example
1. 홍조류로부터 메탄가스를 직접적으로 생산1. Direct production of methane gas from red algae
(1)홍조류 추출물 획득 단계(1) red algae extract acquisition step
홍조류의 일종인 우뭇가사리를 pH 2~3사이의 산성용액에 55분간 침지시킴으로써 우뭇가사리에 섞여있는 불순물과 탄산칼슘을 제거시켰다. 이때 산성용액의 pH는 염산을 이용하여 조절하였으며 온도는 20℃였다. 세척이 완료되면 우뭇가사리 전건 10kg 즉, 완전히 건조되었을 때의 중량이 10kg이 되는 양의 우뭇가사리를 전건 우뭇가사리 대비 4 중량%의 수산화나트륨이 함유된 수산화나트륨 수용액에 침지시켜 120℃ 물중탕에서 90분간 처리하였다. 40℃ 물중탕 처리가 완료되면 우뭇가사리를 꺼내 수돗물로 세척한 후 전건 우뭇가사리 대비 5 중량%의 수산화나트륨이 함유된 수산화나트륨 수용액에 침지시켜 80℃ 물중탕에서 3시간 처리하였다. 이때 물과 우뭇가사리 중량 비율은 10:1로 하였다. 이와 같이 처리하여 추출된 홍조류 추출물은 추출과정에서 저 분자화되어 상온에서도 액체 상태를 유지하게 된다. The red starfish, a type of red algae, was immersed in an acidic solution at pH 2-3 for 55 minutes to remove impurities and calcium carbonate mixed in the algae. At this time, the pH of the acid solution was adjusted using hydrochloric acid and the temperature was 20 ℃. When the washing was completed, 10 kg of whole loaf of wormwood, that is, the weight of 10 kg when completely dried, was immersed in an aqueous sodium hydroxide solution containing 4% by weight of sodium hydroxide compared to the whole lodge, and then treated for 90 minutes in a 120 ℃ water bath. . After the treatment of the water bath at 40 ° C. was completed, the wood starch was removed, washed with tap water, and then immersed in an aqueous sodium hydroxide solution containing 5% by weight of sodium hydroxide compared to the whole starch starch and treated in an 80 ° C. water bath for 3 hours. At this time, the weight ratio of water and mantle was 10: 1. The red algae extract extracted by treating in this way is low molecular weight in the extraction process to maintain the liquid state at room temperature.
(2)가수분해단계 (2) Hydrolysis step
상기 단계에서 추출한 홍조류 추출물을 1.5기압에서 50분간 옥살산으로 가수분해하였다. 홍조류 10kg에서 6.2kg의 추출물을 얻게 되고, 이의 가수분해 결과 3.5kg 가량의 환원당을 얻을 수 있었다. The red algae extract extracted in the above step was hydrolyzed with oxalic acid at 1.5 atmosphere for 50 minutes. 6.2 kg of red algae extracts were obtained, and the hydrolysis resulted in 3.5 kg of reducing sugars.
(3)불순물 제거 단계(3) impurities removal step
상기 가수분해 단계를 거친 홍조류 추출물에 103℃의 수증기를 취입하여 주었으며, 생석회(CaO)로서 pH 10.3의 환경을 만들어 발효 방해물인 푸프푸랄과 하이드록시 메틸 푸르푸랄을 제거하였다.Water vapor at 103 ° C. was blown to the red algae extract which had undergone the hydrolysis step, and the environment of pH 10.3 as quicklime (CaO) was removed to remove the fermentation obstacles, pulpfural and hydroxy methyl furfural.
(4)메탄발효 단계(4) methane fermentation step
상기 불순물 제거 단계를 거친 홍조류 추출물을 (주)리액션 엔지니어링사가 제조한 R-201 series Reactor system 제품인 CSTR(Continous Stirrer Tank Reactor)에 Methanococcus vannielii 균주를 접종하여 표준온도압력 조건하에서 메탄발효과정을 실시한 결과 약 3.85m3의 메탄가스를 얻을 수 있었다.The red algae extract, which has undergone the step of removing impurities, is added to CSTR (Continous Stirrer Tank Reactor), a R-201 series reactor system manufactured by Reaction Engineering Co., Ltd.Methanococcus                                  vannielii                  3.85m of methane-coated tablets under standard temperature and pressure conditions after inoculating strains3Methane gas was obtained.
2. 홍조류 추출물로부터 에탄올을 생산하고 남은 증류폐액을 이용하여 메탄 가스를 생산 2. Methanol gas is produced by using ethanol from red algae extract and distillation waste.
(1)홍조류 추출물 획득단계 (1) red algae extract acquisition step
홍조류의 일종인 우뭇가사리를 pH 2~3사이의 산성용액에 55분간 침지시킴으로써 우뭇가사리에 섞여있는 불순물과 탄산칼슘을 제거시켰다. 이때 산성용액의 pH는 염산을 이용하여 조절하였으며 온도는 20℃였다. 세척이 완료되면 우뭇가사리 전건 10kg 즉, 완전히 건조되었을 때의 중량이 10kg이 되는 양의 우뭇가사리를 전건 우뭇가사리 대비 4 중량%의 수산화나트륨이 함유된 수산화나트륨 수용액에 침지시켜 120℃ 물중탕에서 90분간 처리하였다. 40℃ 물중탕 처리가 완료되면 우뭇가사리를 꺼내 수돗물로 세척한 후 전건 우뭇가사리 대비 5 중량%의 수산화나트륨이 함유된 수산화나트륨 수용액에 침지시켜 80℃ 물중탕에서 3시간 처리하였다. 이때 물과 우뭇가사리 중량 비율은 10:1로 하였다. 이와 같이 처리하여 추출된 홍조류 추출물은 추출과정에서 저 분자화되어 상온에서도 액체 상태를 유지하게 된다. The red starfish, a type of red algae, was immersed in an acidic solution at pH 2-3 for 55 minutes to remove impurities and calcium carbonate mixed in the algae. At this time, the pH of the acid solution was adjusted using hydrochloric acid and the temperature was 20 ℃. When the washing was completed, 10 kg of whole loaf of wormwood, that is, the weight of 10 kg when completely dried, was immersed in an aqueous sodium hydroxide solution containing 4% by weight of sodium hydroxide compared to the whole lodge, and then treated for 90 minutes in a 120 ℃ water bath. . After the treatment of the water bath at 40 ° C. was completed, the wood starch was removed, washed with tap water, and then immersed in an aqueous sodium hydroxide solution containing 5% by weight of sodium hydroxide compared to the whole starch starch and treated in an 80 ° C. water bath for 3 hours. At this time, the weight ratio of water and mantle was 10: 1. The red algae extract extracted by treating in this way is low molecular weight in the extraction process to maintain the liquid state at room temperature.
(2)가수분해단계 (2) Hydrolysis step
상기 단계에서 추출한 홍조류 추출물을 1.5기압에서 50분간 옥살산으로 가수분해하였다. 홍조류 10kg에서 6.2kg의 추출물을 얻게 되고, 이의 가수분해 결과 3.5kg 가량의 환원당을 얻을 수 있었다. The red algae extract extracted in the above step was hydrolyzed with oxalic acid at 1.5 atmosphere for 50 minutes. 6.2 kg of red algae extracts were obtained, and the hydrolysis resulted in 3.5 kg of reducing sugars.
(3)불순물 제거 단계(3) impurities removal step
상기 가수분해 단계를 거친 홍조류 추출물에 103℃의 수증기를 취입하여 주었으며, 생석회(CaO)로서 pH 10.3의 환경을 만들어 발효 방해물인 푸프푸랄과 하이드록시 메틸 푸르푸랄을 제거하였다.Water vapor at 103 ° C. was blown to the red algae extract which had undergone the hydrolysis step, and the environment of pH 10.3 as quicklime (CaO) was removed to remove the fermentation obstacles, pulpfural and hydroxy methyl furfural.
(4)(4) pHpH 중화단계Neutralization stage
상기 불순물 제거 단계를 거친 홍조류 추출물에 인산을 첨가하여 pH를 5.7로 조정하였다.Phosphoric acid was added to the red algae extract after the impurity removal step to adjust the pH to 5.7.
(5)주모접종 단계(5) Main hair vaccination step
Saccharomyces cerevisiae를 전배양하여 최초 생균수 2×10-7 cfu ㎖- 1 의 수준에서 이를 상기 홍조류 추출물에 접종하였다. Saccharomyces cerevisiaePrecultured 2 × 10-7 cfu ml- One At the level of it was inoculated into the red algae extract.
(6)알코올 발효단계(6) Alcohol fermentation stage
상기 Saccharomyces cerevisiae를 접종한 홍조류 추출물은 6일간 30℃ 온도 조건에서 혐기발효 하였다.remindSaccharomyces                                  cerevisiaeRed algae inoculated were anaerobic fermented at 30 ° C. for 6 days.
(7)알코올 발효액을 증류하여 에탄올을 회수하는 단계(7) distilling alcohol fermentation broth to recover ethanol
상기 알코올 발효단계를 거친 후 이를 증류하여 에탄올만 회수하였다.After the alcohol fermentation step, it was distilled to recover only ethanol.
(8)에탄올을 회수하고 남은 증류폐액을 메탄발효균을 이용하여 메탄발효 하는 단계 (8) step of recovering ethanol and methane fermentation of remaining distillation waste using methane fermentation bacteria
상기 알코올 발효액을 증류하여 에탄올을 회수하는 단계 이후 남은 증류폐액을 (주)리액션 엔지니어링사가 제조한 R-201 series Reactor system 제품인 CSTR(Continous Stirrer Tank Reactor)에 Methanococcus vannielii 균주를 이용하여 표준온도압력 조건하에서 메탄발효과정을 실시한 결과 약 약 2.8m3의 메탄가스를 얻을 수 있었다. After distilling the alcohol fermentation broth to recover ethanol, the remaining distillate waste liquid was added to CSTR (Continous Stirrer Tank Reactor), a product of R-201 series reactor system manufactured by Reaction Engineering Co., Ltd.Methanococcus                                  vannielii                  The methane-balancing effect tablet was carried out using the strain under standard temperature and pressure conditions.3Methane gas was obtained.
본 발명에 따른 홍조류 추출물로부터 메탄가스를 생산하는 방법발명을 실시할 경우, 홍조류로부터 펄프를 생산함에 따라 발생 된 부산물을 메탄가스로 재생산함에 따라 폐자원을 효율적으로 재생하여 연료로 사용할 수 있게 된다. 이는 친환경적이며 이러한 방법에 의해 생산된 메탄가스는 수송, 난방, 발전용 천연가스 등으로 사용할 수 있게 된다.When the method of producing methane gas from red algae extract according to the present invention is carried out, by-products generated by producing pulp from red algae can be recycled to methane gas to efficiently recycle waste resources and used as fuel. It is environmentally friendly, and methane gas produced by this method can be used for transportation, heating, and natural gas for power generation.

Claims (9)

  1. 다음 단계를 포함하는 홍조류 추출물로부터 메탄가스를 생산하는 방법:Method for producing methane gas from red algae extract comprising the following steps:
    (a)홍조류 추출물을 가수분해하는 단계;(a) hydrolyzing the algae extract;
    (b)상기 (a)단계를 거친 홍조류 추출물의 불순물을 제거하는 단계;(b) removing impurities of the red algae extract which passed through step (a);
    (c)상기 (b)단계를 거친 추출물을 메탄발효균을 이용하여 메탄발효 하는 단계.(c) methane fermentation using the methane fermentation of the extract after the step (b).
  2. 청구항 1에 있어서, 상기 (b)단계는 (a)단계를 거친 홍조류 추출물에 공기를 취입하는 단계 및 홍조류 추출물을 알칼리 처리하는 단계를 포함하는 것을 특징으로 하는 홍조류 추출물로부터 메탄가스를 생산하는 방법. The method according to claim 1, wherein the step (b) comprises the step of blowing air into the red algae extract that passed through the step (a) and alkali treatment of the red algae extract.
  3. 청구항 1에 있어서, 상기 (a)단계는 산가수분해 방식인 것을 특징으로 하는 홍조류 추출물로부터 메탄가스를 생산하는 방법.The method of claim 1, wherein step (a) is a method of producing methane gas from red algae extract, characterized in that the acid hydrolysis method.
  4. 청구항 1에 있어서, 상기 (C)단계는 산화칼슘,수산화나트륨,수산화칼륨을 이용하여 알칼리 처리하는 것을 특징으로 하는 홍조류 추출물로부터 메탄가스를 생산하는 방법.The method of claim 1, wherein step (C) is methane gas production from red algae extract, characterized in that the alkali treatment using calcium oxide, sodium hydroxide, potassium hydroxide.
  5. 다음 단계를 포함하는 홍조류 추출물로부터 메탄가스를 생산하는 방법:Method for producing methane gas from red algae extract comprising the following steps:
    (a)홍조류 추출물을 가수분해하는 단계;(a) hydrolyzing the algae extract;
    (b)상기 (a)단계를 거친 홍조류 추출물의 불순물을 제거하는 단계;(b) removing impurities of the red algae extract which passed through step (a);
    (c)상기 (b)단계를 거친 홍조류 추출물의 pH중화 단계;(c) pH neutralization step of the red algae extract that passed through step (b);
    (d)상기 (c)단계를 거친 홍조류 추출물에 주모접종을 하는 단계;(d) judo inoculation to the red algae extract passed through step (c);
    (e)상기 (d)단계를 거친 홍조류 추출물을 알코올 발효하는 단계;(e) alcohol fermenting the red algae extract having undergone the step (d);
    (f)상기 (e)단계를 거친 알코올 발효액을 증류하여 에탄올을 회수하는 단계;(f) distilling the alcohol fermentation broth from step (e) to recover ethanol;
    (g)상기 (f)단계에서 에탄올을 회수하고 남은 증류폐액을 메탄발효균을 이용하여 메탄발효 하는 단계.(g) methane fermentation using the methane fermentation of the remaining distillation waste after recovering the ethanol in the step (f).
  6. 청구항 5에 있어서, 상기 (b)단계는 (a)단계를 거친 홍조류 추출물에 공기를 취입하는 단계 및 홍조류 추출물을 알칼리 처리하는 단계를 포함하는 것을 특징으로 하는 홍조류 추출물로부터 메탄가스를 생산하는 방법.The method according to claim 5, wherein the step (b) comprises the step of blowing air to the red algae extract that passed through the step (a) and alkali treatment of the red algae extract method of producing methane gas from the red algae extract.
  7. 청구항 5에 있어서, 상기 (a)단계는 산가수분해 방식인 것을 특징으로 하는 홍조류 추출물로부터 메탄가스를 생산하는 방법.The method of claim 5, wherein step (a) is a method of producing methane gas from red algae extract, characterized in that the acid hydrolysis method.
  8. 청구항 5에 있어서, 상기 (C)단계는 산화칼슘,수산화나트륨,수산화칼륨을 이용하여 알칼리 처리하는 것을 특징으로 하는 홍조류 추출물로부터 메탄가스를 생산하는 방법. The method of claim 5, wherein step (C) is methane gas production from red algae extract, characterized in that the alkali treatment using calcium oxide, sodium hydroxide, potassium hydroxide.
  9. 청구항 5에 있어서, 상기(a)단계 이전에 홍조류 추출물을 농축하는 단계를 추가로 포함하는 것을 특징으로 하는 홍조류 추출물로부터 메탄가스를 생산하는 방법. The method of claim 5, further comprising the step of concentrating the red algae extract before step (a).
PCT/KR2009/007412 2008-12-12 2009-12-11 Method for preparing methane gas using red algae extract WO2010068053A2 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8395486B2 (en) 2010-08-27 2013-03-12 Q Street, LLC System and method for interactive user-directed interfacing between handheld devices and RFID media
EP3102219A4 (en) * 2014-01-21 2017-08-09 Commonwealth Scientific and Industrial Research Organisation Method for reducing total gas production and/or methane production in a ruminant animal

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56139200A (en) * 1980-03-31 1981-10-30 Matsushita Electric Works Ltd Methane fermentation process
US4376163A (en) * 1979-10-01 1983-03-08 Alfa-Laval Ab Process for producing ethanol by continuous fermentation of polysaccharide-containing raw materials
US7067303B1 (en) * 2003-01-24 2006-06-27 The United States Of America As Represented By The Secretary Of Agriculture Culture containing biomass acid hydrolysate and Coniochaeta ligniaria fungus
WO2008105618A1 (en) * 2007-02-26 2008-09-04 Korea Institute Of Industrial Technology Method of producing biofuel using sea algae

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4376163A (en) * 1979-10-01 1983-03-08 Alfa-Laval Ab Process for producing ethanol by continuous fermentation of polysaccharide-containing raw materials
JPS56139200A (en) * 1980-03-31 1981-10-30 Matsushita Electric Works Ltd Methane fermentation process
US7067303B1 (en) * 2003-01-24 2006-06-27 The United States Of America As Represented By The Secretary Of Agriculture Culture containing biomass acid hydrolysate and Coniochaeta ligniaria fungus
WO2008105618A1 (en) * 2007-02-26 2008-09-04 Korea Institute Of Industrial Technology Method of producing biofuel using sea algae

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8395486B2 (en) 2010-08-27 2013-03-12 Q Street, LLC System and method for interactive user-directed interfacing between handheld devices and RFID media
EP3102219A4 (en) * 2014-01-21 2017-08-09 Commonwealth Scientific and Industrial Research Organisation Method for reducing total gas production and/or methane production in a ruminant animal

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