[go: up one dir, main page]

KR20020088328A - The method of preparing alkylpolygluco side - Google Patents

The method of preparing alkylpolygluco side Download PDF

Info

Publication number
KR20020088328A
KR20020088328A KR1020010027869A KR20010027869A KR20020088328A KR 20020088328 A KR20020088328 A KR 20020088328A KR 1020010027869 A KR1020010027869 A KR 1020010027869A KR 20010027869 A KR20010027869 A KR 20010027869A KR 20020088328 A KR20020088328 A KR 20020088328A
Authority
KR
South Korea
Prior art keywords
reaction
solvent
alcohol
glucose
glass beads
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
KR1020010027869A
Other languages
Korean (ko)
Inventor
구재필
이형오
권태혁
Original Assignee
한국산노프코 주식회사
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 한국산노프코 주식회사 filed Critical 한국산노프코 주식회사
Priority to KR1020010027869A priority Critical patent/KR20020088328A/en
Publication of KR20020088328A publication Critical patent/KR20020088328A/en
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H1/00Processes for the preparation of sugar derivatives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H15/00Compounds containing hydrocarbon or substituted hydrocarbon radicals directly attached to hetero atoms of saccharide radicals
    • C07H15/02Acyclic radicals, not substituted by cyclic structures
    • C07H15/04Acyclic radicals, not substituted by cyclic structures attached to an oxygen atom of the saccharide radical

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Molecular Biology (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Saccharide Compounds (AREA)

Abstract

본 발명은 유기용매, 촉매제로서의 산을 이용하여 글루코즈와 알콜을 반응시켜 알킬폴리글루코자이드를 제조하는 방법에 관한 것으로,The present invention relates to a method for preparing alkyl polyglucozide by reacting glucose with alcohol using an organic solvent and an acid as a catalyst.

특히 본 발명에서는 저비점 용매와 그라스비드를 반응에 도입하므로서 종래 폴리글루코즈의 생성 억제 및 점도를 줄이기 위해 글루코즈에 대하여 2-7배에 해당하는 당량비에 해당하는 과량이 알콜을 사용하던 것을 알콜 사용량을 약 2당량 이하로 줄이므로서 미반응 알콜의 회수비용을 줄일 수 있고 그라스비드를 사용하므로서 반응면적을 극대화시키므로 알킬폴리글루코자이드의 반응수율을 크게 높일 수 있으며 저비점 용매를 사용하므로 용매의 회수가 용이하고 비교적 저온에서 반응시킬 수 있으므로 고온 반응으로 발생하는 폴리글루코자이드의 변색을 방지할 수 있는 저비점 용매와 그라스비드를 사용한 알킬폴리글루코자이드의 제조방법에 관한것임.In particular, in the present invention, by introducing a low-boiling solvent and glass beads into the reaction, the excessive amount of alcohol corresponding to the equivalent ratio of 2-7 times the glucose was used to reduce the production and suppress the viscosity of the conventional polyglucose. It can reduce the recovery cost of unreacted alcohol by reducing it to less than 2 equivalents, and maximize the reaction area by using glass beads, which can greatly increase the reaction yield of alkyl polyglucozide. The present invention relates to a method for producing alkylpolyglucoside using low boiling point solvent and glass beads that can be prevented from discoloration caused by high temperature reaction because it can be reacted at a relatively low temperature.

Description

알킬폴리글루코자이드의 제법{THE METHOD OF PREPARING ALKYLPOLYGLUCO SIDE}The manufacturing method of alkyl polyglucozide {THE METHOD OF PREPARING ALKYLPOLYGLUCO SIDE}

본 발명은 생분해성이 좋고 독성이 거의없이 세정제 및 화장품 등의 첨가제로 각광받고 있는 알킬폴리글루코자이드의 제조방법에 관한 것으로 글루코즈와 반응하는 알콜, 저비점용매 및 그라스비드를 사용한 알킬폴리글루코자이드의 제조방법에 관한 것으로 특징으로는 글루코즈와 반응하는 알콜을 종래와 같이 과량으로 사용하지 않아도 DP 값이 낮은 알킬폴리글루코자이드를 얻을 수 있고 이에 따라 미반응 알콜을 제거처리에 따른 경비 또한 절약할 수 있고 저비점 용매를 사용하므로서 용제의 회수가 용이하며 비교적 저온에서 반응시키므로 알킬폴리글루코자이드 반응물의 색상이 변색되지 않으며 그라스비드를 반응물에 첨가시키므로서 반응 면적을 극대화 시키므로서 우수한 반응을 얻을 수 있는 알킬폴리글루코자이드의 제조방법이라 할 수 있다.The present invention relates to a method for producing alkyl polyglucozide, which has been spotlighted as an additive for detergents and cosmetics with good biodegradability and little toxicity. The production of alkyl polyglucozide using alcohols, low boiling solvents and glass beads reacting with glucose The method is characterized in that an alkyl polyglucozide having a low DP value can be obtained without using an alcohol that reacts with glucose in an excessive amount as in the prior art, and thus it is possible to save the cost of removing the unreacted alcohol and lower boiling point. It is easy to recover the solvent by using a solvent and reacts at a relatively low temperature so that the color of the alkylpolyglucozide reactant does not discolor and alkyl polyglucozide can be obtained by maximizing the reaction area by adding glass beads to the reactants. Can be called have.

종래기술분야로서,As the prior art,

알킬폴리글루코자이드의 제조에 관한 방법은 Emill Fisher에 의해 처음으로 소개된후 Henkel 및 Horizon 같은 기업에서 생산해오고 있으며, 알킬폴리글루코자이드의 일반적인 구조는 (I)번과 같다.The method for the preparation of alkylpolyglucosides has been produced by companies such as Henkel and Horizon since it was first introduced by Emill Fisher, and the general structure of alkylpolyglucosides is shown in (I).

H-(G)DP-O-R (I)H- (G) DP -OR (I)

여기서 G는 글루코자이드이며, R은 글루코자이드와 아세탈반응을 하는 알코올에 있는 탄소그룹이며, DP는 중합도를 나타낸다.Where G is glucozide, R is carbon group in alcohol which undergoes acetal reaction with glucozide, and DP is the degree of polymerization.

가장 널리 알려진 공업적 제조방법은 fisher glycosidation 방법으로 미국특허 3,839,318에 의하면 글루코즈에 다량의 알코올을 산촉매하에서 반응시켜 얻은 뒤 중화시켜 미반응 알코올을 진공감압하여 제거하는 직접법과, 글로코즈대신 옥수수, 밀, 야자유 등에서 추출한 전분을 이용하여 먼저 탄소길이가 짧은 부탄올과 먼저 반응시킨 뒤 중간체로서 부틸글루코자이드를 만든다음 여기에 탄소길이가 긴(C1- C30)알코올을 산촉매하에서 반응시켜 알킬폴리글루코자이드를 얻는 간접법이 미국특허 3,547,828에 소개되어졌으며, 이들 방법들의 장단점은 직접법은 설비비가 적은 대신 원료비가 비싸며 간접법은 원료비는 저렴하는 설비비가 많이 들어간다.The most widely known industrial manufacturing method is fisher glycosidation method, which is obtained by reacting glucose with a large amount of alcohol under acid catalysis and neutralizing it by vacuum-reducing the unreacted alcohol according to US Pat. No. 3,839,318, corn, wheat, Starch extracted from palm oil is first reacted with butanol having a short carbon length, and then butylglucoid is formed as an intermediate. Alkylpolyglucozide is reacted by reacting a long carbon (C 1 -C 30 ) alcohol under an acid catalyst. The indirect method obtained is introduced in US Pat. No. 3,547,828, and the advantages and disadvantages of these methods are that the direct method has a low equipment cost but a high raw material cost, and the indirect method has a large equipment cost.

알킬폴리글루코자이드를 제조할 때 형성되는 부산물로는 폴리글루코즈, 에테로, 색깔을 띤 불순물 등이 있으며 이들을 제어하는 인자로는 온도, 압력, 반응시간, 촉매등이 있으며, 너무나 오래 반응시키면 폴리글루코즈가 증가하여 점도가 증가하게 되어 침전물이 생길 수 있으며, 반응온도를 너무 올리면 변색이 되어 색깔이 문제시 될 수 있는 소비재 용품의 계면활성제로서 문제가 야기될 수 있으므로 적당한 반응 조건을 찾아야 한다.By-products formed during the production of alkyl polyglucosides include polyglucose, ether, and colored impurities. Factors controlling them include temperature, pressure, reaction time, and catalyst. To increase the viscosity may cause a precipitate, and if the reaction temperature is too high, discoloration may cause a problem as a surfactant of consumer goods, which may be a color problem, so you must find suitable reaction conditions.

알킬폴리글루코자이드를 제조하는데 사용되는 촉매로는 미국특허 4,223,129,4,393,203, 4,393,203, 독일특허 3,723,826, 3,842,541, 3,900,590 등에서 소개되어지는 바와 같이 황산, 염산, 인산, BF3, PTSA(파라톨루엔 술폰산), 알킬벤젠술폰산, 알킬술폰산, 디노닐나프탈렌술폰산 등 이외에도 여러종류가 있으며 가장 범용적으로 사용하고 있는 것은 PTSA(파라톨루엔 술폰산)이다.Catalysts used to prepare alkylpolyglucosidides include sulfuric acid, hydrochloric acid, phosphoric acid, BF 3 , PTSA (paratoluene sulfonic acid), alkyl as described in US Pat. Nos. 4,223,129,4,393,203, 4,393,203, German Patents 3,723,826, 3,842,541, 3,900,590 In addition to benzenesulfonic acid, alkylsulfonic acid, dinonylnaphthalenesulfonic acid, and the like, there are various kinds, and the most widely used is PTSA (paratoluene sulfonic acid).

반응이 끝난후 중화제로는 보통 NaOH, MgO를 많이 사용하고 이외에도 미국특허 4,713,447에 소개되어진 알카리 및 토알카리금속류의 알코올레이트등이 사용되어지고 있다.After the reaction, the neutralizing agent is usually used a lot of NaOH, MgO, and in addition to the alcoholate of alkali and earth alkali metals introduced in US Patent 4,713,447.

알킬폴리글루코자이드 반응이 끝난후 미반응 알코올을 제거하는 방법으로는 미국특허 4,889,925에서 소개되어지는 바에 의하면 얇은막증류(thin film distilation)를 150-180℃에서 사용하여 중합도 DP가 1.2-1.7 범위에서 얻어지는 알킬폴리글루코자이드를 얻을 수 있는 방법이 소개되어졌다.As a method of removing the unreacted alcohol after the completion of the alkylpolyglucoside reaction, as described in US Pat. No. 4,889,925, a thin film distilation is used at 150-180 ° C., and the degree of polymerization DP is 1.2-1.7. The method for obtaining the obtained alkyl polyglucozide was introduced.

또한 용매 추출법에 의한 방법이 미국특허 3,547,828와 유럽특허 92,355에서 소개되어져 있으며, 이외에도 미반응 지방알코올을 제거하는 방법에 관한 특허가 프랑스특허 A2017240, 독일특허 A13001064, 유럽특허 EP-B10092876, A10531647, B10493 등에서 소개되어지고 있다.In addition, a method of solvent extraction is introduced in US Patent 3,547,828 and European Patent 92,355. In addition, a method for removing unreacted fatty alcohol is disclosed in French Patent A2017240, German Patent A13001064, European Patent EP-B10092876, A10531647, B10493, and the like. It is introduced.

또한 유럽특허 132,043에 따르면 폴리글루코즈의 생성을 억제하기 위해 촉매를 황산 대신 파란톨루엔 술폰산(PTSA)나 벤젠술폰산을 촉매로 사용하면 알코올과 글루코즈의 반응비율이 2 : 1 인 경우 폴리글루코즈가 생성되는 양이 절반이하로 줄어든다고 밝히고 있으며, 유럽특허 449,866에서는 황산에 소수성기가 강한 그룹을 첨가한 새로운 촉매를 사용하면 알코올과 글루코즈의 반응비율이 5 : 1에서 폴리글루코즈의 생성량을 2%대로 줄일 수 있는 방법을 소개하고 있다.In addition, according to European Patent 132,043, when a catalyst is used to inhibit the production of polyglucose, bluetoluene sulfonic acid (PTSA) or benzene sulfonic acid instead of sulfuric acid is used as a catalyst, the amount of polyglucose is generated when the reaction ratio of alcohol and glucose is 2: 1. In the European Patent 449,866, the reaction rate of alcohol and glucose can be reduced from 5: 1 to 2% polyglucose by using a new catalyst with a hydrophobic group added to sulfuric acid. It introduces.

이외에도 유럽특허 B10437460에서는 다양한 합성과정을 조합하여 소개하였고, 스팀을 이용하여 알킬폴리글루코자이드이 냄새를 제거하는 방법이 독일특허 C2 4312559에 소개되어졌고, 낮은 중합도를 얻을 수 있는 방법을 독일특허 A1 4414696에서 소개하고 있다.In addition, European Patent B10437460 introduced various combinations of synthetic processes, and a method of removing odors of alkyl polyglucozide using steam was introduced in German Patent C2 4312559, and a method of obtaining a low polymerization degree was disclosed in German Patent A1 4414696. Introducing.

종래 알킬폴리글루코자이드의 제법에 있어서 폴리알킬폴리글루코자이드의 수율을 높히고 알킬폴리글루코자이드의 생성을 억제하기 위하여 글루코즈의 당량비로 적어도 2-7배에 해당하는 과량의 알콜 사용량을 최소화시키므로 반응후 알콜제거처리 비용을 대폭 감소시킬 수 있고 또한 비점이 낮은 용매를 사용하므로서 비교적 낮은 반응온도(80-100℃)에서 반응시키므로서 알킬폴리글루코자이드의 변색을 방지하므로서 상품성을 높일 수 있으며 반응물에 그라스비드(glass bead)를 첨가하므로서 반응면적을 극대화시키므로서 제품수율을 높힐 수 있는 알킬폴리글루코자이드의 제조방법을 제공함에 목적이 있다 하겠다.In order to increase the yield of polyalkylpolyglucosides and to suppress the production of alkylpolyglucosids in the conventional method of producing alkylpolyglucosides, the amount of alcohol used at least 2-7 times is minimized by the equivalent ratio of glucose so that the alcohol after the reaction The removal cost can be greatly reduced, and the solvent having a low boiling point can be reacted at a relatively low reaction temperature (80-100 ° C.), thereby preventing discoloration of the alkylpolyglucozide, thereby increasing the merchandise and allowing the glass beads to be reacted with the glass. It is an object of the present invention to provide a method for producing an alkylpolyglucoside that can increase the product yield while maximizing the reaction area by adding glass bead).

본 발명은 종래 알킬폴리글루코자이드의 제조방법에서 발생하는 문제점의 해결 및 종래 방법의 개선에 의한 알킬폴리글루코자이드의 제조방법으로서,The present invention is a method for producing an alkylpolyglucoside by solving the problems occurring in the conventional method for producing an alkylpolyglucoside and improving the conventional method,

먼저 글루코즈 1당량비에 대하여 지방산알콜 1-1.8 당량비 저비점 용매는 글루코즈 중량에 대하여 0.5-3배, 촉매로는 슬폰산계열의 산으로서 글루코즈에 대한몰비로 5mmol%, 유리비드는 글로코즈 중량에 대하여 0.5-5배를 첨가하여 반응온도 80-100℃로 유지하면서 교반하고 저비점용매를 순환시키면서 생성되는 물을 계속 제거하면서 7-8시간 반응시켜 반응을 완료시킨후 중화제로 중화시킨후 저비점 용매를 제거하여서된 다음<Ⅱ>식으로 표시되는 알킬폴리글루코자이드의 제조방법이라 할 수 있다.First, the fatty acid alcohol 1-1.8 equivalent ratio relative to glucose 1 equivalent ratio low boiling point solvent is 0.5-3 times the weight of glucose, the catalyst is a sulfonic acid-based acid in the molar ratio of glucose 5 mol%, glass beads 0.5 to the weight of the glucose After adding -5 times, stirring while maintaining the reaction temperature of 80-100 ℃ and circulating the low-boiling solvent while continuing to remove the water generated by the reaction for 7-8 hours to complete the reaction and neutralized with a neutralizing agent and then remove the low-boiling solvent It can be said to be a method for producing an alkyl polyglucozide represented by the following <II> formula.

상기식(Ⅱ)의 R은 탄소길이가 1에서 30까지 정도이며, Ra, Rb, Rc, Rd 는 수소 또는 C1- C30으로 선형, 가지형, 포화 또는 불포화 형태로 구성되어있고, DP(중합도)는 알코올 한 분자에 결합하는 글루코즈 단위수를 나타내며, DP의 값은 1-5의 중합도를 나타낸다.R in the formula (II) has a carbon length of about 1 to 30, Ra, Rb, Rc, Rd is hydrogen or C 1 -C 30 is composed of linear, branched, saturated or unsaturated form, DP ( Degree of polymerization) represents the number of glucose units bound to one molecule of alcohol, and the value of DP represents a degree of polymerization of 1-5.

여기에서 저비점 용매의 사용량에 있어서 알콜의 사용량 범위에서 사용량이 많아질 경우 저비점 용매의 최소 사용량의 범위에서도 순환과정이 가능하지만 그 이하로 사용할 경우 순환과정에 문제점이 발생하고 저비점 용매의 사용량의 사용범위 이상으로 사용해도 반응에는 영향이 없지만 반응후 회수공정에서 불리하다 할것이며,Here, when the amount of use of the low boiling point solvent is increased in the range of use of alcohol, the circulating process is possible even in the range of the minimum amount of use of the low boiling point solvent, but when it is used below, problems occur in the circulation process and the range of use of the low boiling point solvent is used. The above use does not affect the reaction, but will be disadvantageous in the recovery process after the reaction,

또한 그라스비드 사용량은 적어도 글루코즈에 대하여 중량비로 최저치인 0.5만 사용해도 현저한 반응효과가 나타나 점점 반응율이 상승하나 최고치인 5배 이상을 사용해도 더 이상의 반응상승 효과는 거의 나타나지 않는다.In addition, the amount of glass beads used is at least 0.5 g / w weight ratio, and the reaction rate is remarkable, and the reaction rate is gradually increased.

위의 방법에서 사용되는 지방산알콜로는 핵산, 햅탄, 옥탄 등을 사용할 수 있고 저비점 용매로는 핵산, 햅탄, 옥탄 등을 사용할 수 있으며 비점은 헥산 68.742℃, 햅탄 98.428℃, 옥탄 125.6℃등 비교적 저비점을 갖고 있다.As the fatty acid alcohol used in the above method, nucleic acid, heptan, octane, etc. may be used, and as the low boiling point solvent, nucleic acid, heptan, octane, etc. may be used, and the boiling point is relatively low boiling point such as hexane 68.742 ° C, heptan 98.428 ° C, octane 125.6 ° C, etc. Have

촉매로서 술폰산계열의 산으로는 오르토, 파라. 메타-토루엔 술폰산, 황산 등을 사용할 수 있다.As the catalyst, sulfonic acid-based acids include ortho and para. Meta-toluene sulfonic acid, sulfuric acid and the like can be used.

유리비드(glass bead)는 JHM 60(BINEX제품)을 사용하여 입도는 0.5㎜에서 10㎜까지 사용이 가능하며 중화제로는 가성소다, 산화마그네슘, 가성가리 등을 사용한다.Glass bead can be used with JHM 60 (BINEX), and its particle size can be used from 0.5mm to 10mm, and caustic soda, magnesium oxide, caustic, etc. are used as neutralizing agent.

특히 유리비드의 사용은 본 발명의 핵심기술로서 이를 사용하지 않으며 알킬폴리글루코자이드의 수율이 극히 낮고 폴리글루코즈생성량이 높아지며 중합도가 DP가 높아져 세정제나 화장품 첨가제로서 사용할 수 없다.In particular, the use of glass beads is not the core technology of the present invention, and the yield of alkylpolyglucoside is extremely low, the amount of polyglucose produced is high, and the degree of polymerization is high, so it cannot be used as a detergent or cosmetic additive.

발명의 목적에 적합한 중합도로서 가장 이상적인 것은 중한도 1.2-1.7 범위라 할 수 있다.The most suitable degree of polymerization suitable for the purpose of the invention can be said to be in the range of 1.2-1.7 median.

상기 본 발명의 기술구성을 분명하게 하고 효과를 알아보기 위하여 비교실시예와 실시예를 들었다.In order to clarify the technical configuration of the present invention and to examine the effects, comparative examples and examples were given.

비교 실시예Comparative Example

환류장치, 온도계가 장치된 둥근 플라스크에 글루코즈 90부를 넣고 옥탄올을 65부 넣고 촉매로는 파라 톨루엔 술포닉 산을 0.5부 넣고, 유리비드 JHM 60는 첨가하지않고 용매는 핵산을 사용하여 교반하면서 온도를 100℃로 올린후 12시간정도교반하면서 핵산을 순환시켰으나 중합도가(DP)가 55를 갖는 폴리글루코자이드를 36g 얻었다.In a round flask equipped with a reflux device and a thermometer, 90 parts of glucose was added, 65 parts of octanol was added, 0.5 parts of para-toluene sulfonic acid was added as a catalyst, and glass bead JHM 60 was not added, and the solvent was stirred using a nucleic acid. The nucleic acid was circulated while stirring at about 100 ° C. for 12 hours, but 36 g of polyglucozide having a degree of polymerization (DP) of 55 was obtained.

제조예 1Preparation Example 1

환류장치, 온도계가 장치된 둥근 플라스크에 글루코즈 90부를 넣고 옥탄올을 65부 넣고 촉매로는 파라 톨루엔 술포닉산을 0.5부 넣고, 유리비드 JHM 90부를 첨가하고 용매는 핵산을 사용하여 교반하면서 온도를 90℃로 올린후 7시간정도 교반하면서 핵산을 순환시키면서 물을 제거한후 산화마그네슘 5부를 넣어 중화시킨 뒤 용매로 사용된 핵산을 증류시켜 상기식(Ⅱ)의 형태의 알킬폴리글루코자이드를(DP=1.7)88g 얻었다.90 parts of glucose is added into a round flask equipped with a reflux device and a thermometer, 65 parts of octanol is added, 0.5 parts of para-toluene sulfonic acid is added as a catalyst, 90 parts of glass bead JHM is added, and the solvent is stirred at 90 ° by using a nucleic acid. After raising the temperature to 7 ℃ and circulating the nucleic acid while stirring for about 7 hours to remove the water and neutralized by adding 5 parts of magnesium oxide, and distilled the nucleic acid used as a solvent to form an alkyl polyglucozide of the formula (II) (DP = 1.7 88 g was obtained.

제조예 2Preparation Example 2

환류장치, 온도계가 장치된 둥근 플라스크에 글루코즈 90부르 넣고 데카놀을 80부 넣고 촉매로는 파라 톨루엔 술포닉산을 0.5부 넣고, 유리비드 JHM 90부를 첨가하고 용매는 핵산을 사용하여 교반하면서 온도를 90℃로 올린후 8시간정도 교반하면서 핵산을 순환시키면서 물을 제거한 후 수산화칼륨 2부를 넣어 중화시킨 뒤 용매로 사용된 핵산을 증류시켜 상기식(Ⅱ)의 형태의 알킬폴리글루코자이드를(DP=2.5)93g 얻었다.In a round flask equipped with a reflux device and a thermometer, 90 parts of glucose, 80 parts of decanol, 0.5 parts of para-toluene sulfonic acid are added as a catalyst, 90 parts of glass beads JHM are added, and the solvent is stirred using a nucleic acid and heated to 90 °. After raising to ℃ and circulating the nucleic acid while stirring for about 8 hours to remove water, neutralize by adding 2 parts of potassium hydroxide and distilling the nucleic acid used as a solvent to give the alkyl polyglucozide of the form of formula (II) (DP = 2.5 ) 93 g was obtained.

제조예 3Preparation Example 3

환류장치, 온도계가 장치된 둥근 플라스크에 글루코즈 90부를 넣고 도데카놀을 90부 넣고 촉매로는 파라 톨루엔 술포닉산을 0.5부 넣고, 유리비드 JHM 90부를 첨가하고 용매는 핵산을 사용하여 교반하면서 온도를 90℃로 올린후 8시간정도 교반하면서 핵산을 순환시키면서 물을 제거한 후 산화마그네슘 5부를 넣고 중화시킨 뒤 용매로 사용된 핵산을 증류시켜 상기식(Ⅱ)의 형태의 알킬폴리글루코자이드를(DP=3.7)86g 얻었다.In a round flask equipped with a reflux device and a thermometer, 90 parts of glucose is added, 90 parts of dodecanol is added, 0.5 parts of para-toluene sulfonic acid is added as a catalyst, 90 parts of glass bead JHM is added, and the solvent is stirred using a nucleic acid. After raising the temperature to 8 ℃ and removing the water while circulating the nucleic acid while stirring for about 8 hours, neutralized by adding 5 parts of magnesium oxide and distilling the nucleic acid used as a solvent to give the alkyl polyglucozide of the form of formula (II) (DP = 3.7 ) 86 g was obtained.

제조예 4Preparation Example 4

환류장치, 온도계가 장치된 둥근 플라스크에 글루코즈 90부를 넣고 데카놀을 80부 넣고 촉매로는 파라 톨루엔 술포닉산을 0.5부 넣고, 용매는 햅탄을 사용하며 유리비드는 JHM 90부를 넣고 교반하면서 온도를 100℃로 올린후 8시간정도 교반하면서 핵산을 순환시키면서 물을 제거한후 수산화나트륨 4부 넣고 중화시킨 뒤 용매로 사용된 햅탑을 증류시켜 상기식(Ⅱ)의 형태의 알킬폴리글루코자이드를(DP=4.2)80g 얻었다.Put 90 parts of glucose in a round flask equipped with a reflux device and a thermometer, add 80 parts of decanol, add 0.5 parts of para-toluene sulfonic acid as a catalyst, use haptan as a solvent, and add 90 parts of JHM to glass beads. After raising the temperature to 8 ℃, circulating the nucleic acid while circulating for 8 hours to remove water, neutralize 4 parts of sodium hydroxide and distill the Heptop used as a solvent to give the alkyl polyglucozide of the formula (II) (DP = 4.2 80 g was obtained.

제조예 5Preparation Example 5

환류장치, 온도계가 장치된 둥근 플라스크에 글루코즈 90부를 넣고 옥탄올을 70부 넣고 촉매로는 황산을 0.5부 넣고, 유리비드 JHM 90부를 첨가하고 용매는 핵산을 사용하여 교반하면서 온도를 90℃로 올린후 7시간정도 교반하면서 핵산을 순환시키면서 물을 제거한후 산화마그네슘 5부를 넣어 중화시킨 뒤 용매로 사용된 핵산을 증류시켜 상기식(Ⅱ)의 형태의 알킬폴리글루코자이드를(DP=3.8)70g 얻었다.In a round flask equipped with a reflux device and a thermometer, 90 parts of glucose was added, 70 parts of octanol was added, 0.5 parts of sulfuric acid was added as a catalyst, 90 parts of glass beads JHM were added, and the solvent was heated to 90 ° C. while stirring using a nucleic acid. After removing the water while circulating the nucleic acid while stirring for about 7 hours, neutralized by adding 5 parts of magnesium oxide, and distilled the nucleic acid used as a solvent to obtain 70 g of alkyl polyglucozide (DP = 3.8). .

이상의 비교실시예와 본 발명의 실시예를 비교할 때 비교실시예에서는 원료 투입량은 실시예와 같으나 수율면에서 알킬폴리글루코자이드의 수율이 엄청나게 떨어지고 중합도 또한 DP 55으로 나타나 사실상 세정제나 화장품 첨가제로는 사용할 수 없다.Compared with the above comparative example and the embodiment of the present invention, in the comparative example, the input amount of the raw material is the same as the example, but the yield of alkylpolyglucozide is greatly reduced in terms of yield, and the polymerization degree is also represented by DP 55, which is actually used as a detergent or cosmetic additive. Can't.

본 발명은 저비점 용매와 비드를 사용하여 글루코즈와 알코올을 당량비로 반응시키므로 다량의 알코올을 사용하는 기존방법보다 경제적이며 사용된 용매는 쉽게 회수하여 재사용할 수 있으며, 미반응 알코올을 제거할 필요가 없고 반응온도가 낮으므로 기존의 방법에서의 변색 문제를 해결하게되어 용이적으로 알킬폴리글루코자이드를 제조할 수 있게된다.According to the present invention, since glucose and alcohol are reacted in an equivalent ratio using a low boiling point solvent and beads, it is more economical than the conventional method using a large amount of alcohol, and the used solvent can be easily recovered and reused, and there is no need to remove unreacted alcohol. Since the reaction temperature is low to solve the problem of discoloration in the existing method it is possible to easily prepare the alkyl polyglucozide.

Claims (1)

글루코즈에 대하여 지방산 알콜이 당량비로 1-1.8, 저비점용매가 중량으로 0.5-3배, 술폰산계의 산이 몰비로 0.5mmol%, 그라스비드가 중량비로 0.5-5배를 첨가하여 반응온도 80-100℃로 유지하면서 교반하고 저비점용매를 순환시키면서 7-8시간 반응시켜 반응을 완료시켜 중화제로 중화시킨후 저비점 용매를 제거하여서된 다음(Ⅱ)식으로 표시되는 알킬폴리글루코자이드의 제법.The fatty acid alcohol is 1-1.8 equivalent weight, 0.5-3 times the weight ratio of the low boiling solvent, 0.5 mmol% the molar ratio of the acid of sulfonic acid, and 0.5-5 times the weight ratio of the glass beads. Stirring while maintaining and circulating a low boiling point solvent for 7-8 hours to complete the reaction to neutralize with a neutralizing agent and then to remove the low boiling point solvent of the following formula (II). 일반식(Ⅱ)의 R은 탄소길이가 1에서 30까지 정도이며, Ra, Rb, Rc, Rd는 수소 또는 C1- C30으로 구성되어 있는 포화 또는 불포화형태의 가지 또는 선형구조이고, DP의 값은 1-5의 값을 갖는다.R in general formula (II) has a carbon length of 1 to 30, and Ra, Rb, Rc and Rd are branched or linear structures of saturated or unsaturated form composed of hydrogen or C 1 -C 30 , and of DP The value has a value of 1-5.
KR1020010027869A 2001-05-21 2001-05-21 The method of preparing alkylpolygluco side Ceased KR20020088328A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020010027869A KR20020088328A (en) 2001-05-21 2001-05-21 The method of preparing alkylpolygluco side

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020010027869A KR20020088328A (en) 2001-05-21 2001-05-21 The method of preparing alkylpolygluco side

Publications (1)

Publication Number Publication Date
KR20020088328A true KR20020088328A (en) 2002-11-27

Family

ID=27705807

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020010027869A Ceased KR20020088328A (en) 2001-05-21 2001-05-21 The method of preparing alkylpolygluco side

Country Status (1)

Country Link
KR (1) KR20020088328A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0570056A1 (en) * 1992-05-15 1993-11-18 ENICHEM S.p.A. Process for preparing alkyl polyglucosides
KR950026885A (en) * 1994-03-14 1995-10-16 성재갑 Process for preparing higher alkyl polyglucoside
US5478930A (en) * 1993-09-20 1995-12-26 Henkel Kommanditgesellschaft Auf Aktien Process for producing light colored alkyl polyglucosides with partially sulfated fatty alcohol catalysts
KR960022552A (en) * 1994-12-03 1996-07-18 페터스, 슈베르트페거 Post-treatment method of fatty alcohol alkylpolyglycoside solution by distillation
KR970070014A (en) * 1996-04-03 1997-11-07 성재갑 Method for producing high alkylpolyglucoside
US6156885A (en) * 1997-10-30 2000-12-05 Condea Augusta S.P.A. Process for the synthesis of alkylpolyglucosides
WO2001009153A1 (en) * 1999-07-29 2001-02-08 Cognis Corporation Process for reducing cycle times in reactions during the production of alkyl polyglycosides

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0570056A1 (en) * 1992-05-15 1993-11-18 ENICHEM S.p.A. Process for preparing alkyl polyglucosides
US5478930A (en) * 1993-09-20 1995-12-26 Henkel Kommanditgesellschaft Auf Aktien Process for producing light colored alkyl polyglucosides with partially sulfated fatty alcohol catalysts
KR950026885A (en) * 1994-03-14 1995-10-16 성재갑 Process for preparing higher alkyl polyglucoside
KR960022552A (en) * 1994-12-03 1996-07-18 페터스, 슈베르트페거 Post-treatment method of fatty alcohol alkylpolyglycoside solution by distillation
KR970070014A (en) * 1996-04-03 1997-11-07 성재갑 Method for producing high alkylpolyglucoside
US6156885A (en) * 1997-10-30 2000-12-05 Condea Augusta S.P.A. Process for the synthesis of alkylpolyglucosides
WO2001009153A1 (en) * 1999-07-29 2001-02-08 Cognis Corporation Process for reducing cycle times in reactions during the production of alkyl polyglycosides

Similar Documents

Publication Publication Date Title
CA1219860A (en) Process for preparing alkyl glycosides
US4713447A (en) Process for preparing alkyl glycosides
SK32094A3 (en) Method of preparing of alkylpolyglucosides
EP0132046A1 (en) Improved process for preparing alkyl glycosides
US4783563A (en) Preparation of hexabromocyclododecane
EP0065770A1 (en) Process for the synthesis of p-nitrophenetol
CN105126905A (en) A kind of ionic liquid for synthesizing long-chain alkyl glycosides and its preparation method and application
KR20010103043A (en) Method of preparing surface-active alcohols and surface-active alcoholic ethers, products obtained by said method and their use
JPH07501061A (en) Method for producing alkyl and/or alkenyl oligoglycosides
CN111747871A (en) Production process of surfactant dioctyl sodium sulfosuccinate
JP3110722B2 (en) Synthetic method for improved alkyl polyglucosides
KR20020088328A (en) The method of preparing alkylpolygluco side
JPH0632795A (en) Production of alkylpolyglucoside
JP2001515469A (en) Method for producing alkyl polyglycoside
JPH0699463B2 (en) Method for producing alkyl glycoside
DE69830486T2 (en) ALUMINUM COMPOUNDS AND THEIR USE
KR20030016819A (en) The method of preparing alkylpolyglycoside capable of increasing a reaction property
JPH0383944A (en) Method for producing styrenated phenol
JP3989043B2 (en) Method for producing alkyl cyanoacetate
KR970005314B1 (en) Process for preparation of alkyl polyglucoside
KR0138203B1 (en) Process for preparing higher alkyl polyglucoside
DE102004006579A1 (en) 2,7-Dimethyl-octa-2,4,6-trienedial is prepared by double enolether condensation of a butenedial-bisacetal, hydrolysis, dialdehyde conversion and crystallization with all steps effected in an organic solvent
JP2001151789A (en) Method for producing alkyl glycoside
KR960016211B1 (en) Process for preparing alkoxy alkyl polyglucoside
US2995599A (en) Process for the production of alkyl esters of 7-hydroxyalkanoic acids

Legal Events

Date Code Title Description
A201 Request for examination
PA0109 Patent application

Patent event code: PA01091R01D

Comment text: Patent Application

Patent event date: 20010521

PA0201 Request for examination
PG1501 Laying open of application
E902 Notification of reason for refusal
PE0902 Notice of grounds for rejection

Comment text: Notification of reason for refusal

Patent event date: 20030731

Patent event code: PE09021S01D

E601 Decision to refuse application
PE0601 Decision on rejection of patent

Patent event date: 20040511

Comment text: Decision to Refuse Application

Patent event code: PE06012S01D

Patent event date: 20030731

Comment text: Notification of reason for refusal

Patent event code: PE06011S01I