KR0136552B1 - Preparation of chitin and chitosan from solenocera prominentis shells - Google Patents
Preparation of chitin and chitosan from solenocera prominentis shellsInfo
- Publication number
- KR0136552B1 KR0136552B1 KR1019930028901A KR930028901A KR0136552B1 KR 0136552 B1 KR0136552 B1 KR 0136552B1 KR 1019930028901 A KR1019930028901 A KR 1019930028901A KR 930028901 A KR930028901 A KR 930028901A KR 0136552 B1 KR0136552 B1 KR 0136552B1
- Authority
- KR
- South Korea
- Prior art keywords
- chitin
- chitosan
- hours
- hydrochloric acid
- molecular weight
- 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.)
- Expired - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
- C08B37/0024—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Glucans; (beta-1,3)-D-Glucans, e.g. paramylon, coriolan, sclerotan, pachyman, callose, scleroglucan, schizophyllan, laminaran, lentinan or curdlan; (beta-1,6)-D-Glucans, e.g. pustulan; (beta-1,4)-D-Glucans; (beta-1,3)(beta-1,4)-D-Glucans, e.g. lichenan; Derivatives thereof
- C08B37/0027—2-Acetamido-2-deoxy-beta-glucans; Derivatives thereof
- C08B37/003—Chitin, i.e. 2-acetamido-2-deoxy-(beta-1,4)-D-glucan or N-acetyl-beta-1,4-D-glucosamine; Chitosan, i.e. deacetylated product of chitin or (beta-1,4)-D-glucosamine; Derivatives thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Molecular Biology (AREA)
- Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
본 발명은 키틴 및 키토산의 제조 방법, 특히 대롱 수염 새우(solenocera prominentis)의 갑각으로부터 고순도 및 고백색도의 고분자량 및 저분자량 키틴을 동시에 얻고 이로부터 고순도, 고탈아세틸화도 및 고 백색도를 갖는 고분자량 또는 저분자량의 생체 임상의학용 키토산을 제조하는 방법에 관한 것이다.The present invention simultaneously obtains high purity and whiteness high molecular weight and low molecular weight chitin from the shell of chitin and chitosan, in particular from the shellfish of solenocera prominentis, from which the high molecular weight having high purity, high deacetylation and high whiteness or A method for producing low molecular weight chitosan for biomedical medicine.
Description
본 발명은 키틴 및 키토산의 제조 방법, 특히 대롱 수염 새우(Solenocera prominentis)의 갑각으로부터 고순도 및 고백색도의 고분자량 및 저분자량 키틴을 동시에 얻고 이로부터 고 순도, 고 탈아세틸화도 및 고 백색도를 갖는 고분자량 또는 저분자량의 생체 임상의학용 키토산을 제조하는 방법에 관한 것이다.The present invention simultaneously obtains high purity and whiteness of high molecular weight and low molecular weight chitin from the shell of chitin and chitosan, in particular the shellfish of Solenocera prominentis, from which high purity, high deacetylation and high whiteness are obtained. The present invention relates to a method for preparing chitosan for biomedical medicine of molecular weight or low molecular weight.
키틴은 지구상에 섬유소 다음으로 풀부한 천연 고분자 물질로서, 감각류 동물의 갑각으로부터 상업적으로 추출되는 고부가 가치의 생 고분자이다. 이러한 키틴은 수불용성이므로 활용에 큰 장애가 되고 있다. 따라서, 키틴을 탈아세틸화시켜 약산성 액성에서 수용성이 발현되는 키토산으로 전환시킬 수 있으며, 이러한 수용성 키토산이 산업적으로 키틴보다 더 유용하게 이용되고 있다. 최근들어 게 및 새우의 대량 어획으로 수산 폐기물인 갑각의 처분에 관심을 가지게 되면서 이로부터 추출 가능한 키틴의 이용도를 다양하게 개발하려 하게 되었다.Chitin is a natural polymer that is the second highest in the world, followed by fiber, and is a high value biopolymer that is commercially extracted from the crustaceans of sensory animals. Such chitin is insoluble in water and thus becomes a major obstacle to its utilization. Therefore, deacetylation of chitin can be used to convert chitosan, which is water soluble in weakly acidic liquids, and this water soluble chitosan is industrially more useful than chitin. Recently, the interest in the disposal of shellfish, aquatic wastes, has led to the development of various uses of chitin that can be extracted from large-scale fishing of crabs and shrimp.
이들 키틴 및 키토산은 초기이는 식품 공장 폐수내의 유효물질(단백질 등)을 회수하는 응집제로 쓰였으나, 최근 들러서는 식품 분야, 의료의학 분야, 기능성막, 효소 및 미생물의 고정화 담체 등과 같은 생물공학 분야, 화장품 분야, 농업분야, 화공 분야, 환경분야 등 전 분야에 걸쳐 폭넓게 이용되고 있다.These chitin and chitosan were initially used as coagulants for recovering effective substances (proteins, etc.) in food plant wastewater, but recently stopped by biotechnology such as food, medical, functional membranes, enzymes and immobilization carriers of enzymes and microorganisms, It is widely used in all fields such as cosmetics, agriculture, chemicals and environment.
구체적으로 키틴 및 키토산은 분자량에 따라 1000 센티포이즈(CPS) 이상의 고결정성, 고분자량인 경우는 섬유 형성능 또는 필름 형성능이 우수하고 강도가 뛰어나므로 키틴/키토산 섬유의 제조, 분리용 분리막의 제조 등에 효과적으로 사용할 수 있고, 평균 분자량 5000 내지 10000 범위의 비교적 저분자량인 경우는 식품보존제, 항암제, 체내콜레스테롤 강하제, 화장품 첨가제, 체내 중금속 제거제, 항균방취제 등으로 사용할 수 있다.Specifically, chitin and chitosan have high crystallinity and high molecular weight of 1000 centipoise (CPS) or more depending on the molecular weight, so that the fiber forming ability or film forming ability is excellent and the strength is excellent. In the case of using a relatively low molecular weight in the range of an average molecular weight of 5000 to 10,000, it can be used as a food preservative, an anticancer agent, a body cholesterol lowering agent, a cosmetic additive, a heavy metal remover in the body, an antibacterial deodorant, and the like.
1990년대에 들어서면서 세계적으로 키틴/키토산의 수요가 중대되고 있는데 저품위보다는 고품위의 수요가 급증하고 있다. 1990년 이전에는 주로 수처리, 농업용으로 이용되는 저급품의 키틴/키토산이 응용분야에서 주류를 이루어왔다고 볼 수 있으나 최근에는 식품분야에 응용될 수 있는 중품위와 의약 및 화장품 분야에서 효과적으로 응용될 수 있는 고품위가 요구되고 있다.In the 1990s, the demand for chitin / chitosan is increasing worldwide, and the demand for high quality rather than low quality is increasing rapidly. Prior to 1990, chitin / chitosan, a low-grade product mainly used for water treatment and agriculture, has been mainstream in the application field, but recently, a high-grade product that can be effectively applied in the food field and in medicine and cosmetics It is required.
고품위의 경우 세계적으로 제조기술을 보유하고 있는 국가가 극히 한정되어 있으며 공업화에 성공하여 상업적 시판을 이룩한 국가는 더욱 드물다. 생체 임상의학용의 제조과정에서 요구되는 고품위 키틴/키토산이 갖추어야 할 조건은 다음과 같다.In the case of high quality, only a few countries have manufacturing technology in the world, and few countries succeed in industrialization and commercialize them. The conditions for high quality chitin / chitosan that are required in the manufacture of bioclinical use are as follows.
첫째, 가장 필수적인 요건으로서 불순물의 함량이 낮아야 한다. 제조된 키틴/키토산에 잔류하는 대표적인 불순물로서 석회질(CaCO3가 주류를 이루고 있음), 단백질, 지질, 색소, 중금속 등을 열거할 수 있는데, 석회질의 경우 대략 0.2%이하, 단백질의 경우 0.1%이하, 중금 속의 경우 대략 5ppm이하가 만족되어야만 의약품, 화장품 분야에서의 응용이 가능하다. 석회질이나 단백질의 잔류함량을 최소로 저하시키려면 이론적으로는 Hcl 수용액에 의한 석회질 제거시와 NaOH 수용액에 의한 단백질 제거시에 격렬한 처리조건을 사용함으로써 간단히 해결될 수 있지만, 이와 동시에 급격한 분자쇄의 절단이 초래되어 분자량이 현저히 낮아질 뿐만 아니라 수득되어 키틴/키토산의 분자량 분포가 넓지며 진한 갈색의 착색이 수반되는 경우가 대부분이다. 키틴/키토산 제조시 나타나는 착색 현상은 분자쇄가 파괴될 때 나타나는 현상으로 추축되고 있는데, 에탄올/H2O 등의 혼합용매 처리에 의하여 제거되므로 착색현상은 제조되는 키틴/키토산 내부에 일종의 불순물이 함유되는 현상으로 해석될 수 있다.First, the most essential requirement should be a low content of impurities. Representative impurities in the produced chitin / chitosan can be listed as lime (CaCO 3 is the mainstream), proteins, lipids, pigments, heavy metals, etc., about 0.2% or less for lime, 0.1% or less for protein In the case of heavy metals, approximately 5ppm or less must be satisfied before they can be used in medicine and cosmetics. In order to minimize the residual amount of calcareous or protein, theoretically, it can be solved simply by using intensive treatment conditions when removing the calcareous solution with HCl aqueous solution and protein removal with NaOH aqueous solution, but at the same time, abruptly breaking the molecular chain This results in not only a significantly lower molecular weight, but also a wider molecular weight distribution of chitin / chitosan, which is often accompanied by dark brown coloration. The coloration phenomenon in chitin / chitosan production is thought to be a phenomenon that occurs when the molecular chain is broken. Since the coloration phenomenon is removed by a mixed solvent treatment such as ethanol / H 2 O, the coloration phenomenon contains a kind of impurities inside the manufactured chitin / chitosan. It can be interpreted as a phenomenon.
결과적으로 분자량의 저하방지와 분자량 저하에서 유발되는 착색현상을 방지하기 위해서는 기존의 키틴/키토산 제조법이 면밀하고 광범위하게 재검토되어야 할 것으로 판단된다. 발생된 착색을 제거하기 위하여 기공고된 특허나 논문들에서는 산화제를 사용하는 경우가 다소 발견되고 있다(P. Broussignac, Chim. Ind. Genie Chim. 99, 1241(1968); 구현철, 장병권, 최규석, J. of Korean Ind. Eng. Chemistry Vol. 4, No. 2, June 1933, P325).As a result, in order to prevent the reduction of the molecular weight and the coloring phenomenon caused by the molecular weight decrease, it is determined that the existing chitin / chitosan preparation method should be closely and extensively reviewed. The use of oxidants has been found in patents and papers published in order to remove coloration (P. Broussignac, Chim. Ind. Genie Chim. 99, 1241 (1968); , J. of Korean Ind. Eng. Chemistry Vol. 4, No. 2, June 1933, P325).
착색된 키틴이나 키토산으로부터 산화제를 사용하여 백도를 상승시킬 수는 있으나 이러한 산화제 처리에 의한 백도의 상승은 일시적이기 때문에 시간이 경과되면 (대략 10일 이후) 서서히 백도가 저하되기 시작하고 일정시간 경과후에는 산화제 처리전보다 착색이 더욱 강해지는 경우가 대부분이다. 그러므로, 산화제 처리에 의하여 백도를 상승시키는 방법은 고품위의 키틴/키토산 제조에서는 배제되어야 한다. 키틴의 경우는 특정종류의 용매처리에 의해서도 산화제 처리와 유사한 점진적인 착색이 유발되는 경우도 있다.Although it is possible to increase the whiteness by using an oxidant from colored chitin or chitosan, the increase in whiteness due to this oxidant treatment is temporary, and as time passes (after about 10 days), the whiteness gradually decreases and after a certain time In many cases, coloring becomes stronger than before oxidizing agent treatment. Therefore, the method of raising the whiteness by the oxidizing agent should be excluded in the production of high quality chitin / chitosan. In the case of chitin, a certain kind of solvent treatment may cause a gradual coloring similar to that of the oxidizer treatment.
또한, 고품위의 키틴/키토산의 제조에서는 분자량의 크기가 다양하고 고유특성을 갖는 차별화된 제품을 제조하기 위해서 키틴/키토산을 얻게 되는 근원(게, 새우, 오징어, 번데기, 곤충류, 균류) 자체도 차별화되어야만 한다. 최근에 이르러 키틴/키토산의 응용범위가 날로 확장되기 시작하면서 분자량 제어의 기술이 절실이 요구되고 있다.In addition, in the production of high-quality chitin / chitosan, the source (crab, shrimp, squid, chrysalis, insects, fungus) that obtain chitin / chitosan in order to manufacture differentiated products having various molecular weights and unique characteristics also differentiates itself. Should be. Recently, as the application range of chitin / chitosan is beginning to expand day by day, the technology of molecular weight control is urgently needed.
상기에서, 키틴 제조시 격렬한 반응 조건의 사용은 잔류불순물의 함량을 현저히 낮출 수 있지만 분자량의 저하가 유발되므로 고분자량의 제품 제조에는 부적합함이 지적된 바 있으나, 저분자량 제품의 제조에서는 격렬한 반응조건의 부여가 무리가 없을 것으로 판단된다.In the above, the use of violent reaction conditions in the production of chitin can significantly lower the content of residual impurities, but has been pointed out that it is unsuitable for the production of high molecular weight products due to the decrease in molecular weight, but in the production of low molecular weight products, violent reaction conditions. It is judged that the grant of is not unreasonable.
그러나 분자량의 저하와 함께 착색의 유발이 필연적이라 할 수 있다. 저분자량 제품에서 유발되는 착색현상이 식품분야의 응용에서는 크게 문제시 되지 않으나 화장품 첨가제, 의약품 등의 분야에서는 적용될 수 없기 때문에 저분자량의 키틴/키토산 제품이면서도 착색의 정도가 낮은 제품의 개발이 절실히 요구되고 있다. 키틴/키토산을 얻을 수 있는 원료근원(게, 새우, 갑오징어)에 따라서 함유된 석회질과 단백질의 양이 상이하고 키틴과의 결합상태에서 차이가 있기 때문에 석회질제거 반응조건과 단백질제거 반응조건이 근원에 따라서 차별화되어야 한다.However, it can be said that induction of coloring with the decrease of molecular weight is inevitable. Although the coloring phenomenon caused by low molecular weight products is not a big problem in the application of food, but it cannot be applied in the field of cosmetic additives and pharmaceuticals, the development of low molecular weight chitin / chitosan product and low degree of coloring is urgently needed. It is becoming. Depending on the source of raw material (crab, shrimp, cuttlefish) from which chitin / chitosan can be obtained, the amount of calcare and protein contained differs in the binding state with chitin. Differentiate accordingly.
일반적으로 게류의 갑각은 조직이 치밀하고 키틴의 결정화도가 지극히 높기 때문에 고분자량의 키틴/키토산을 얻기에는 용이하다. 그러나 저분자량을 얻기 위해서는 격렬한 반응조건이 부여되어야만 하는 결과 게 갑각에서 얻어지는 저분자량의 제품은 착색의 정도가 지극히 심하여 백도가 우수한 저분자량의 제조에서는 부적합하다.In general, crustaceans of crabs are easy to obtain high molecular weight chitin / chitosan because of their tight tissue and extremely high degree of crystallization of chitin. However, in order to obtain low molecular weight, violent reaction conditions must be imparted. The low molecular weight product obtained from the shellfish is extremely unsatisfactory in the manufacture of low molecular weight having excellent whiteness.
한편, 새우류의 갑각은 게 갑각에 적용되었던 조건보다 훨씬 온화한 조건으로도 석회질의 제거가 가능하기 때문에 고분자량의 키틴/키토산의 제조가 용이할 것으로 판단되었다. 그렇지만 일반적으로 새우류에서 유래된 키틴/키토산은 그 자체가 결정화도가 낮고 분자량이 낮기 때문에 게갑각에서 얻어진 바와같은 고분자량의 키틴/키토산을 얻기는 불가능한 것으로 밝혀졌다.On the other hand, shrimp shellfish can be easily prepared in high molecular weight chitin / chitosan because it can be removed even under milder conditions than the crab shell was applied. However, in general, chitin / chitosan derived from shrimp has been found to be impossible to obtain high molecular weight chitin / chitosan as obtained from crab shell because of its low crystallinity and low molecular weight.
오히려 새우류에서는 게갑각류에서 적용되었던 만큼의 격렬한 Hcl 처리 조건이 부여되지 않고도 저분자량의 키틴/키토산을 얻을 수 있으므로 게갑각에서 얻은 것보다 착색도가 훨씬 낮은 저분자량의 키틴/키토산을 쉽게 얻을 수 있다.Rather, in shrimps, low-molecular-weight chitin / chitosan can be obtained without the same intense Hcl treatment conditions as used in crab shellfish, so it is easy to obtain low-molecular weight chitin / chitosan with much lower coloration than that obtained from crab shellfish.
기존에 사용되어 온 키틴의 제조방법으로서는 핵크만(Hackman)법 (Austr. J. Biol, Sci. 7, 168-178(1954) ), 휘스러 (Whistler) 및 베밀러 (BeMiller)법 (J. O. C. 27, 1161-1163 (1962) ), 호로위쯔 (Horowitz), 로즈맨 (Roseman) 및 블루멘탈 (Blumenthal) 법 (JACS, 179, 5046-5049(1957) ) 및 브루시냑 (Broussignac)법 (Chim, Ind. Genie Chim. 99, 1241-1247(1968) )등이 있으나 상기 방법들은 일반적으로 제조공정이 번거롭고 처리시간이 너무 길거나 처리조건이 과격하여, 새우로부터 고분자량의 키틴/키토산을 고수율로 얻기에는 부적합한 방법들이다.Conventional methods for preparing chitin have been the Hackman method (Austr. J. Biol, Sci. 7, 168-178 (1954)), Whistler and BeMiller method (JOC 27, 1161-1163 (1962)), Horowitz, Roseeman and Blumenthal (JACS, 179, 5046-5049 (1957)) and Brusignacac (Chim, Ind. Genie Chim. 99, 1241-1247 (1968)), but these methods are generally inconvenient to obtain high molecular weight chitin / chitosan from shrimps due to the cumbersome manufacturing process, too long processing time, or extreme processing conditions. Methods.
또한 브루시냑 법에서는 탈색을 위해 산화제 H2O2를 사용하는데 이는 일정시간 경과 후 백도의 저하를 유발하며 생체 임상의학용의 키틴/키토산 제조공정으로서는 문제가 있다. 키토산은 상기 여러 방법들에 의해 수득된 불용성 키틴을 탈아세틸화함으로써 수득할 수 있는데, 일반적으로 30 내지 50%의 수산화나트륨 용액을 키틴량의 약20배 정도로 사용하여 5 내지 20시간 동안 처리함으로써 얻을 수 있다.In addition, the Brucignac method uses the oxidizing agent H2O2 for decolorization, which causes a decrease in whiteness after a certain time and has a problem as a manufacturing process for chitin / chitosan for biomedical medicine. Chitosan can be obtained by deacetylating insoluble chitin obtained by the various methods described above, which is generally obtained by treating 30 to 50% sodium hydroxide solution using about 20 times the amount of chitin for 5 to 20 hours. Can be.
이제까지 설명한 바와같이 게갑각으로부터는 저분자량의 키틴/키토산을 얻기 어려우며 새우 갑각으로부터는 고분자량의 키틴/키토산을 얻기 어려운 것으로 알려져 왔으나 본 발명자는 새우류에 대한 광범위한 연구를 통해 대롱수염새우 (Solenocera prominentis)로부터 고분자량과 저분자량의 키틴/키토산을 동시에 용이하게 수득할 수 있다는 사실을 발견하고, 보다 간단한 공정으로, 짧은 시간에 고순도 및 고백도의 키틴/키토산을 수득하는 방법을 개발하여 본 발명을 완성하게 되었다.As described above, it has been known that low molecular weight chitin / chitosan is difficult to obtain from crab shells and high molecular weight chitin / chitosan from shrimp shells. However, the present inventors have conducted extensive research on shrimps solenocera prominentis. The present invention finds that high molecular weight and low molecular weight chitin / chitosan can be easily obtained simultaneously, and in a simpler process, a method for obtaining high purity and high whiteness chitin / chitosan in a short time is completed. Was done.
즉, 우리나라 남해안과 제주도 근해에서 포획되는 대롱수염새우(Solenocera prominentis)는 석회질의 함량이 다른 종류의 새우보다 월등히 높고 수득되는 키틴자체의 분자량도 현저히 높기 때문에 게갑각에 적용되었던 방법보다 훨씬 간단한 방법을 적용하여 고분자량의 키틴/키토산을 손쉽게 얻을 수 있을 뿐만아니라 저분자량의 제조시 게갑각에 적용되었던 처리조건보다 훨씬 온화한 조건으로도 손쉽게 저분자량을 수득할 수 있다. 또한, 대롱수염새우는 일반 새우들이 지니고 있는 붉은 색소를 거의 지니고 있지 않기 때문에 탈색 공정이 생략되어도 백도가 지극히 우수한 키틴/키토산을 수득할 수 있다.That is, the solenocera prominentis, which are caught on the south coast of Korea and near the Jeju island, is much simpler than the method applied to crab shellfish because the lime content is much higher than that of other kinds of shrimp and the molecular weight of chitin itself is significantly higher. Not only can high molecular weight chitin / chitosan be easily applied, but also low molecular weight can be easily obtained even under milder conditions than the treatment conditions applied to crab shell during low molecular weight production. In addition, since the lobster has almost no red pigment that ordinary shrimps have, the chitin / chitosan having excellent whiteness can be obtained even if the decolorization process is omitted.
본 발명의 목적은 대롱수염새우로부터 고순도, 고백도 및 고분자량의 키틴과, 고순도,고백도 및 저분자량의 키틴을 동시에 손쉽게 수득할 수 있는 키틴의 제조방법을 제공하는 것이다.It is an object of the present invention to provide a method for preparing chitin, which can easily obtain high purity, high whiteness and high molecular weight chitin and high purity, high whiteness and low molecular weight chitin simultaneously from the sapling shrimp.
본 발명의 다른 목적은 상기에서 수득한 키틴으로 부터 고순도 및 고백도의 고분자량 키토산 및 저분자량 키토산을 동시에 수득하는 키토산의 제조방법을 제공하는 것이다.Another object of the present invention is to provide a method for preparing chitosan which simultaneously obtains high purity and high whiteness high molecular weight chitosan and low molecular weight chitosan from the chitin obtained above.
즉, 본 발명은 새우 갑각을 썩지 않도록 보관하는 단계, 건조된 새우 갑각을 분쇄하는 단계, 분쇄된 새우 갑각을 염산 수용액중에서 처리하여 석회질을 제거하는 단계, 석회질이 제거된 새우갑각을 NaOH수용액중에서 처리하여 단백질을 제거하는 단계 및 제조된 조키틴을 여과, 세척, 중화 및 건조시키는 단계를 포함하는 생체 임사의학용 키틴의 제조방법에 관한 것이다.That is, the present invention comprises the steps of keeping the shrimp crust intact, crushing the dried shrimp crust, processing the pulverized shrimp crust in an aqueous hydrochloric acid solution to remove the calcite, the calcareous shrimp crust in NaOH aqueous solution The present invention relates to a method for preparing chiropractic chitin, comprising the steps of removing the protein and filtering, washing, neutralizing and drying the prepared jochitin.
또한, 본 발명은 상기 방법에 의해 제조된 키틴을 NOaH수용액중에서 탈아세틸화하고, 수세 및 여과하는 단계를 포함하는 키토산의 제조방법에 관한 것이다.The present invention also relates to a method for producing chitosan comprising the step of deacetylating chitin prepared by the above method in aqueous NOaH solution, washing with water and filtering.
본발명을 더욱 상세히 설명하면 다음과 같다.The present invention will be described in more detail as follows.
우선 흐르는 물로 새우갑각을 세척함으로써 새우갑각에 잔류하는 육즙이나 부유물을 효과적으로 제거한다.First, wash the shrimp crust with running water to effectively remove any succulents or suspended matter remaining on the shrimp crust.
잔류하는 육즙이나 부유물은 새우갑각을 단시간내에 부패시켜 키틴/키토산의 품위를 손상시키고 잔류 불순뮬로 작용할 가능성이 있기 때문에 완벽히 제거되어야만 한다.Residual broth or suspended solids must be removed completely, as the shrimp shell may rot in a short time, possibly degrading the quality of chitin / chitosan and acting as a residual impurity.
세척된 새우갑각을 탈수기로 탈수시킨다음 아세톤, 에탄올, 메탄올, 메틸이텔케톤 및 디옥산 등의 유기용매에 24-48시간동안 침지시킨 후 탈수기로 탈수하여 그늘에서 건조시킴으로써 새우갑각의 부패를 촉진시키는 수분을 제거할 수 있으며 유기 용매자체에 의한 부패방지 효과를 얻을 수 있다.Dehydrated shrimp shells are dehydrated with a dehydrator and then immersed in organic solvents such as acetone, ethanol, methanol, methyl ether ketone and dioxane for 24-48 hours, dehydrated with a dehydrator and dried in the shade to promote the decay of shrimp shells. Moisture can be removed and the anti-corrosion effect by the organic solvent itself can be obtained.
용매 처리로부터 건조된 새우갑각을 직경 0.5-3mm의 크기로 분해하여 50g을 2l 용량의 3구 플라스크에 넣은후 -40℃ 내지 +30℃의 1-6N염산 수용액을 서서히 가한 다음 염산 수용액 표면에 부유된 새우갑각이 전부 밑으로 가라 앉으면 50-200rpm 속도로 1.5내지 24시간 교반함으로써 석회질을 제거한다. 이때 -10℃ 이하의 온도에서는 염산 수용액의 결빙을 방지하기 위해 염산 수용액에 유기 용매를 혼합하는 것이 유리하며, 바람직한 유기 용매는 메탄올, 에탄올, 이소프로판올, 부탄올, 아세톤 및 메틸에틸케톤이다. 또한, 상기 염산 수용액 처리시 염산 수용액의 농도에 따라 최종적으로 얻을 수 있는 키틴/키토산의 분자량이 달라지며, 저온(+10℃이하)에서는 비교적 고분자량의 키틴/키토산을, 고온(+20℃이상)에서는 비교적 저분자량의 키틴/키토산을 얻을 수 있다. 대롱 수염새우는 게갑각 또는 다른 종류의 새우류에 비해서 석회질의 함량이 월등히 커서 기포 발생이 격렬하기 때문에 용기 밖으로 내용물이 넘치지 않도록 각별한 주의가 필요하다.Shrimp shells dried from the solvent treatment were decomposed to a size of 0.5-3 mm in diameter, 50 g were placed in a 2-liter three-necked flask, and slowly added to a solution of 1-6 N hydrochloric acid at -40 ° C. to + 30 ° C. Once all the carapaces have subsided, they are decalcified by stirring at 50-200 rpm for 1.5 to 24 hours. In this case, it is advantageous to mix an organic solvent with an aqueous hydrochloric acid solution at a temperature below −10 ° C. to prevent freezing of the aqueous hydrochloric acid solution, and preferred organic solvents are methanol, ethanol, isopropanol, butanol, acetone, and methyl ethyl ketone. In addition, the molecular weight of the chitin / chitosan finally obtained according to the concentration of the hydrochloric acid aqueous solution when the hydrochloric acid aqueous solution is treated, and at a low temperature (below +10 ℃) high molecular weight chitin / chitosan, high temperature (+20 ℃ or more) ), Relatively low molecular weight chitin / chitosan can be obtained. Beef crayfish has much higher lime content than crab shellfish or other kinds of shrimps, so the bubbles are intense, so special care should be taken to prevent the contents from overflowing the container.
염산 수용액 처리에 의해서 석회질의 제거가 완료되면 여과,세척 및 중화시킨 다음 게갑각이나 다른 종류의 새우에서 요구되는 색소제거를 위한 용매처리등 모든 공정이 생략될 수 있으며 즉시 탈단백 공정에 들어갈 수 있다.When calcification is completed by hydrochloric acid aqueous solution, all processes such as filtration, washing and neutralization, solvent treatment for removing pigments required for crab shells and other kinds of shrimp can be omitted, and the deproteinization process can be entered immediately. .
탈단백 공정에서는 5-10%(w/w) NaOH 수용액을 사용하여 90℃ 내지 100℃에서 1차로 0.5시간 내지 6시간, 2차로 0.5시간 내지 5시간 동안 2회 가열처리함으로써 잔류단백질을 완전히 제거할 수 있다.In the deproteinization process, 5-10% (w / w) NaOH aqueous solution is used to heat the first two times at 90 ° C. to 100 ° C. for 0.5 hours to 6 hours and the second 0.5 hours to 5 hours to completely remove residual protein. can do.
상기 방법에 의해서 수득된 키틴을 질소 기류를 통과시키면서 70℃ 내지 120℃에서 2내지 8시간동안 40-50% 농도의 NaOH수용액으로 2 내지 4회 처리함으로써 탈아세틸화시켜 고순도, 고백도, 고점도(또는 저점도)를 갖는 키토산을 얻는다.The chitin obtained by the above method was deacetylated by treating with NaOH aqueous solution of 40-50% concentration for 2 to 8 hours at 70-120 ° C. for 2-8 hours while passing through a nitrogen stream to obtain high purity, high whiteness, high viscosity ( Or low viscosity) to obtain chitosan.
이하, 본 발명을 하기 실시예 및 비교예로써 보다 상세하게 설명하지만, 본 발명이 이에 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to the following Examples and Comparative Examples, but the present invention is not limited thereto.
실시예에서, 키틴 중의 잔류 CaCO3 함량은 키틴을 800℃에서 1시간 연소시킨 후의 강열 감량으로서 측정하였으며, 단백질 함량은 바이오-래드(Bio-Rad)사의 단백질 분석 키트(kit)를 아용하여 브래드포드(Bradford)법에 따라 미국 휴렛-팩커드(Hewlett-packard)사의 UV/VIS 분광분석계로 측정하였다. 또한, 금속함량은 일본 세이코사의 ICP-AES 및 미국 퍼킨-엘머(Perkin-Elmer)사의 AA분광계를 사용함으로써 측정하였다. 탈아세틸화도는 논문[J.Appl. polym. Sci. 28, 1909(1983)]에 게제된 IR이용법(Mima법)에 의거하여 측정하였다. 경시 백색도는 30일 이상 경과한 후의 외관상태를 육안으로 판별하여 우수(백색)와 불량(황색을 띰)으로 나누어 평가하였다. 또한, 점도는 브룩필드(Brookfield) 점도계에서 #4스핀들을 이용하여 60rpm으로 1% 아세트산용액 중의 0.5%키토산 용액으로써 측정하였다.In the examples, the residual CaCO3 content in the chitin was measured as the loss of ignition after burning the chitin at 800 ° C. for 1 hour, and the protein content was determined using Bradford (Bio-Rad) protein analysis kit. According to the Bradford method, it was measured by a UV / VIS spectrometer of Hewlett-packard. In addition, the metal content was measured by using ICP-AES manufactured by Seiko, Japan and AA spectrometer, manufactured by Perkin-Elmer, USA. Deacetylation degree is described in J. Appl. polym. Sci. 28, 1909 (1983)] was measured according to the IR method (Mima method) published in. The whiteness over time was visually determined by visual observation after 30 days or more and divided into excellent (white) and poor (yellow). Viscosity was also measured as a 0.5% chitosan solution in 1% acetic acid solution at 60 rpm using # 4 spins on a Brookfield viscometer.
실시예 1Example 1
단계 1 : 키틴의 제조Step 1: Preparation of Chitin
육질이 제거된 새우 갑각을 흐르는 물로 세척한 후 탈수하고 에탄올속에 24시간동안 침지한 후 건조시켰다.The meat shells were washed with running water, dehydrated and immersed in ethanol for 24 hours and dried.
용매처리, 건조된 새우 갑각(수분율 10% 내외) 60g을 2-3mm의 입경으로 고르게 분쇄하여 기계적 교반기가 장60g of solvent-treated and dried shrimp shells (about 10% water content) are crushed evenly to a particle diameter of 2-3mm,
치된 2ι 용량의 3구 플라스크에 넣은 다음 -10℃로 냉각된 2N 농도의 염산 수용액 1.0ι를 서서히 가한 후 염산 수용액 표면에 부유된 새우갑각이 전부 밑으로 가라앉을 때까지 -10℃를 유지하면서 방치하였다.Into a 3 volume flask equipped with 2ι volume, slowly add 1.0ι of aqueous 2N hydrochloric acid solution cooled to -10 ℃ and keep it at -10 ℃ until all the shrimp shells floating on the surface of hydrochloric acid solution subside. It was.
부유된 새우 갑각이 전부 밑으로 가라 앉으면 50-200rpm의 속도로 6시간 교반함으로써 석회질을 제거하고 여과, 중화 및 건조시켜 석회질이 제거된 새우갑각 16.8g을 얻었다. 석회질이 제거된 새우갑각 16.8g을 5%(w/w) 농도의 NaOH 수용액 1ι에 침지시킨 후 질소 가스를 주입시키면서 2시간동안 95℃를 유지하면서 가열시키는 제 1차 NaOH 수용액처리를 행하였다. 2시간 가열후 여과하고 탈이온수로 2-3회 세척후 즉시 제2차 NaOH 수용액 처리를 행하였는데 95℃를 유지하면서 1.5시간 가열시킨 후 내용물을 여과, 세척, 중화 및 건조시켜 백도가 우수하고 투명성을 갖는 12.8g의 키틴을 수득하였다.When all the floating shrimp shells sank underneath, it was stirred for 6 hours at a speed of 50-200 rpm to remove calcification, filtration, neutralization and drying to obtain 16.8 g of lime shells. 16.8 g of decalcified shrimp shells were immersed in a 1% aqueous NaOH solution at a concentration of 5% (w / w), followed by a first NaOH aqueous solution treatment which was heated at 95 ° C. for 2 hours while injecting nitrogen gas. After heating for 2 hours, filtered and washed 2-3 times with deionized water, and then immediately treated with a second NaOH aqueous solution, and heated for 1.5 hours while maintaining 95 ℃, the contents were filtered, washed, neutralized and dried to have excellent whiteness and transparency. 12.8 g chitin was obtained.
단계 2 : 키토산의 제조Step 2: Preparation of Chitosan
상술한 방법으로 제조된 키틴 15g을 1l용량의 3구 플라스크에 넣고 40% NaOH 수용액 600ml를 가하고 질소 가스를 연속적으로 주입시키면서 100℃에서 5시간 탈아세틸화 반응을 진행시켰다. 제1차 탈아세틸화 반응이 완료되면 NaOH수용액을 여과하고 탈이온수로 2-3회 세척후 즉시 제1차 탈아세틸화 반응과 동일한 방법으로 제2차 탈아세틸화 반응을 진행시켰는데 제2차 탈아세틸화 반응에서는 반응시간을 3시간으로 변화시켰다. 제2차 탈아세틸화 반응이 완료되면 여과하고 탈이온수로 중성이 될 때까지 세척한 다음 80/20(v/v)에탄올/물 용액에 20시간 방치 후 여과 건조시켜 11.69g의 키토산을 수득하였다. 수득된 키토산의 점도는 2400cpc (1%초산용액,0.5%키토산용액, Brookfield Viscometer, Spindle #4,60rpm)이었다.15 g of the chitin prepared by the above-described method was placed in a 1 L three-necked flask, and 600 ml of 40% NaOH aqueous solution was added thereto, followed by deacetylation at 100 ° C. for 5 hours while continuously injecting nitrogen gas. After completion of the first deacetylation reaction, the aqueous NaOH solution was filtered, washed 2-3 times with deionized water, and immediately proceeded to the second deacetylation reaction in the same manner as the first deacetylation reaction. In the deacetylation reaction, the reaction time was changed to 3 hours. After completion of the second deacetylation reaction, the mixture was filtered and washed with deionized water until neutral, and left in 80/20 (v / v) ethanol / water solution for 20 hours, followed by filtration and drying to obtain 11.69 g of chitosan. . The viscosity of the obtained chitosan was 2400 cpc (1% acetic acid solution, 0.5% chitosan solution, Brookfield Viscometer, Spindle # 4, 60 rpm).
실시예 2Example 2
실시예 1의 단계 1에서 염산 수용액에 의한 석회질의 제거 시간을 9시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.58g의 키토산을 얻었으며 키토산의 점도는 1500cps 이었다.Except for changing the removal time of the calcareous solution by the hydrochloric acid aqueous solution in step 1 of Example 1 was carried out in the same manner as in Example 1 to obtain 11.58g of chitosan and the viscosity of the chitosan was 1500cps.
실시예 3Example 3
실시예 1의 단계 1에서 염산 수용액 농도를 6N로 변화시키고 염산수용액의 처리온도를 -20℃로, 처리시간을 6시간으로 변화시킨 것을 제외하고는 실시예1과 동일하게 실시하여 11.87g의 키토산을 얻었으며 점도는 1740cps이었다.In the same manner as in Example 1, except that the aqueous hydrochloric acid concentration was changed to 6N in step 1 of Example 1, the treatment temperature of the aqueous hydrochloric acid solution was changed to -20 ° C, and the treatment time was changed to 6 hours, and 11.87 g of chitosan was used. And the viscosity was 1740 cps.
실시예 4Example 4
실시예 1의 단계 1에서 염산 수용액의 농도를 6N로 변화시키고 염산수용액의 처리온도를 -20℃로, 처리시간을 1.5시간으로 변화시킨 것을 제외하고는 실시예1과 동일하게 실시하여 11.92g의 키토산을 얻었으며 점도는 2440cps이었다.In the same manner as in Example 1 except that the concentration of the aqueous hydrochloric acid solution was changed to 6N in step 1 of Example 1, the treatment temperature of the aqueous hydrochloric acid solution was changed to -20 ° C, and the treatment time was changed to 1.5 hours. Chitosan was obtained and the viscosity was 2440 cps.
실시예 5Example 5
실시예1의 단계 1에서 염산 수용액의 농도를 6N로 변화시키고 염산 수용액의 처리온도를 -30℃로, 처리시간을 3시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 12.03g의 키토산을 얻었으며 점도는 2390cps이었다.Example 1 was carried out in the same manner as in Example 1 except that the concentration of the aqueous hydrochloric acid solution was changed to 6N, the treatment temperature of the aqueous hydrochloric acid solution was changed to -30 ° C, and the treatment time was changed to 3 hours. Chitosan was obtained and the viscosity was 2390 cps.
실시예 6Example 6
실시예1의 단계 1에서 염산수용액의 농도를 6N로 변화시키고 염산수용액의 처리온도를 -30℃로, 처리시간을 9시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.98g의 키토산을 얻었으며 점도는 2100cps이었다.Example 1 was carried out in the same manner as in Example 1 except that the concentration of the aqueous hydrochloric acid solution was changed to 6N, the treatment temperature of the aqueous hydrochloric acid solution was changed to -30 ° C, and the treatment time was changed to 9 hours. Chitosan was obtained and the viscosity was 2100 cps.
실시예 7Example 7
실시예1의 단계 1에서 염산 수용액의 농도를 6N로 변화시키고 염산 수용액의 처리온도를 -40℃로, 처리시간을 6시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 12.07g의 키토산을 얻었으며 점도는 1560cps이었다.Example 1 was carried out in the same manner as in Example 1 except that the concentration of the aqueous hydrochloric acid solution was changed to 6N, the treatment temperature of the aqueous hydrochloric acid solution was changed to -40 ° C, and the treatment time was changed to 6 hours. Chitosan was obtained and the viscosity was 1560 cps.
실시예 8Example 8
실시예1의 단계 1에서 염산 수용액의 농도를 6N로 변화시키고 염산 수용액의 처리온도를 -40℃로, 처리시간을 9시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 12.03g의 키토산을 얻었으며 점도는 2040cps이었다.12.03 g of Example 1 was changed in the same manner as in Example 1 except that the concentration of the aqueous hydrochloric acid solution was changed to 6N, the treatment temperature of the aqueous hydrochloric acid solution was changed to -40 ° C, and the treatment time was changed to 9 hours. Chitosan was obtained and the viscosity was 2040 cps.
실시예 9Example 9
실시예1의 단계 1에서 염산 수용액의 처리온도를 0℃로, 처리시간을 3시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.42g의 키토산을 얻었으며 점도는 2690cps이었다.In the same manner as in Example 1, except that the treatment temperature of the aqueous hydrochloric acid solution was changed to 0 ° C. and the treatment time was changed to 3 hours in Step 1 of Example 1, 11.42 g of chitosan was obtained and the viscosity was 2690 cps.
실시예 10Example 10
실시예1의 단계 1에서 염산 수용액의 처리온도를 0℃로, 처리시간을 6시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.28g의 키토산을 얻었으며 점도는 2200cps이었다.In Example 1, except that the treatment temperature of the aqueous hydrochloric acid solution was changed to 0 ° C. and the treatment time was changed to 6 hours, 11.28 g of chitosan was obtained and the viscosity was 2200 cps.
실시예 11Example 11
실시예1의 단계 1에서 염산 수용액의 처리온도를 10℃로, 처리시간을 3시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.23g의 키토산을 얻었으며 점도는 2260cps이었다.In the same manner as in Example 1, except that the treatment temperature of the aqueous hydrochloric acid solution was changed to 10 ° C. and the treatment time was changed to 3 hours in Step 1 of Example 1, 11.23 g of chitosan was obtained and the viscosity was 2260 cps.
실시예 12Example 12
실시예1의 단계 1에서 염산 수용액의 처리온도를 10℃로, 처리시간을 9시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.17g의 키토산을 얻었으며 점도는 1290cps이었다.In the same manner as in Example 1 except that the treatment temperature of the aqueous hydrochloric acid solution was changed to 10 ° C. and the treatment time to 9 hours in Step 1 of Example 1, 11.17 g of chitosan was obtained and the viscosity was 1290 cps.
실시예 13Example 13
실시예1의 단계 1에서 염산 수용액의 처리온도를 20℃로, 처리시간을 6시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.21g의 키토산을 얻었으며 점도는 782cps이었다.In the same manner as in Example 1, except that the treatment temperature of the aqueous hydrochloric acid solution was changed to 20 ° C. and the treatment time was changed to 6 hours in Step 1 of Example 1, 11.21 g of chitosan was obtained and the viscosity was 782 cps.
실시예 14Example 14
실시예1의 단계 1에서 염산 수용액의 처리온도를 20℃로, 처리시간을 9시간으로 변화시킨 것을 제외하고는 실시예 1과 동일하게 실시하여 11.18g의 키토산을 얻었으며 점도는 671cps이었다.In the same manner as in Example 1, except that the treatment temperature of the aqueous hydrochloric acid solution was changed to 20 ° C. and the treatment time to 9 hours in Step 1 of Example 1, 11.18 g of chitosan was obtained and the viscosity was 671 cps.
비교예 (1954. 헥크만법에 의거)Comparative Example (1954. Based on Heckman Act)
220g의 새우갑각에 2N 농도의 염산 수용액 5ℓ를 가하고 25℃를 유지하면서 5시간 방치후 여과, 세척 및 중화시킨다. 상기의 방법에 의하여 얻은 새우갑각에 2N농도의 염산 수용액 500ml를 첨가하고 0℃를 유지시키면서 48시간동안 석회질 제거공정을 행한 후 여과, 세척, 중화 및 건조하여 48.4g의 탈석회질화 새우갑각을 얻었다. 상기의 방법에 의하여 수득된 탈석회질화 새우갑각을 1N농도의 NaOH수용액 500ml에 첨가하고 100℃를 유지하면서 12시간 동안 가열하여 단백질을 제거하였다. 위와 동일한 방법의 단백질 제거공정을 4회 반복한 후 여과 및 중화시킨 다음 에탄올 및 에테르로 세척 및 건조하여 33g의 키틴을 얻었다. 상기의 방범에 의하여 수득된 키틴 40g을 40% NaOH수용액중에서 100℃를 유지하면서 1차로 5시간 및 2차로 3시간에 걸쳐서 2회 탈아세틸화시켜 28.38g의 키토산을 얻었으며 그의 점도는 432cps이었다. 수득된 키토산의 백색도는 황색을 띄고 있으며 불투명한 상태이다.5 L of 2N hydrochloric acid aqueous solution was added to 220 g of shrimp shells, and the mixture was left for 5 hours while maintaining at 25 ° C., filtered, washed and neutralized. 500 ml of 2N hydrochloric acid aqueous solution was added to the shrimp shell obtained by the above method, and decalcification was carried out for 48 hours while maintaining 0 ° C., and then filtered, washed, neutralized and dried to obtain 48.4 g of decalcified shrimp shell. . The decalcification shrimp shell obtained by the above method was added to 500 ml of 1N NaOH aqueous solution, and heated at 12 ° C. for 12 hours to remove protein. The protein removal process of the same method as described above was repeated four times, filtered and neutralized, washed with ethanol and ether, and dried to obtain 33 g of chitin. 40 g of chitin obtained by the above security was deacetylated twice over 5 hours for the first time and 3 hours for the second time while maintaining 100 ° C. in 40% NaOH aqueous solution to obtain 28.38 g of chitosan, and its viscosity was 432 cps. The whiteness of the obtained chitosan is yellowish and opaque.
상기 실시예1 내지 14 및 비교에서 사용된 반응조건 및 그로부터 수득된 키틴 및 키토산의 특성이 표1 및표2에 각각 나타나있다.The reaction conditions used in Examples 1 to 14 and the above and the properties of chitin and chitosan obtained therefrom are shown in Tables 1 and 2, respectively.
표 1Table 1
표 2TABLE 2
1) -40℃, -30℃ 및 -20℃에 사용된 6N Hcl 수용액의 제조법 : 진한 HCl 1600ml, 탈리 온수 1400ml 및 에탄올 200ml를 혼합하여 제조하였다.1) Preparation of 6N Hcl aqueous solution used at -40 ° C, -30 ° C and -20 ° C: 1600 ml of concentrated HCl, 1400 ml of tally hot water, and 200 ml of ethanol were prepared.
2) -10℃에 사용된 2N Hcl의 제조법 : 상기 방법에 의하여 제조된 6N Hcl 수용액을 H2O : 에탄올=1/1(v/v) 혼합액으로 3배 희석하여 2N Hcl 수용액을 제조하였다.2) Preparation of 2N Hcl used at -10 ° C: 6N Hcl aqueous solution prepared by the above method was diluted three times with H 2 O: ethanol = 1/1 (v / v) mixture to prepare a 2N Hcl aqueous solution.
상기 표 1 및 표 2에서 확인할 수 있는 바와 같이, 본 발명의 방법에 따라 고순도 및 고백도의 고분자량 및 저분자량 키틴/키토산을 동시에 수록할 수 있으며, 본 발명의 방법으로 제조된 키틴/키토산은 순도가 중요시되는 생체 임상의학분야에 특히 유용하다.As can be seen in Table 1 and Table 2, according to the method of the present invention can be recorded simultaneously high purity and high molecular weight chitin / chitosan of high purity, chitin / chitosan prepared by the method of the present invention It is particularly useful in the field of biomedical medicine where purity is important.
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1019930028901A KR0136552B1 (en) | 1993-12-21 | 1993-12-21 | Preparation of chitin and chitosan from solenocera prominentis shells |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1019930028901A KR0136552B1 (en) | 1993-12-21 | 1993-12-21 | Preparation of chitin and chitosan from solenocera prominentis shells |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR950018054A KR950018054A (en) | 1995-07-22 |
| KR0136552B1 true KR0136552B1 (en) | 1998-04-25 |
Family
ID=19371990
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR1019930028901A Expired - Fee Related KR0136552B1 (en) | 1993-12-21 | 1993-12-21 | Preparation of chitin and chitosan from solenocera prominentis shells |
Country Status (1)
| Country | Link |
|---|---|
| KR (1) | KR0136552B1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100481793B1 (en) * | 2002-05-24 | 2005-04-11 | 주식회사 만나피아 | A manufacturing method of water soluble chitosan |
| KR102206626B1 (en) | 2019-08-21 | 2021-01-22 | 조용수 | Continuously Variable Transmission shift system using rack and pinion gear system |
-
1993
- 1993-12-21 KR KR1019930028901A patent/KR0136552B1/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100481793B1 (en) * | 2002-05-24 | 2005-04-11 | 주식회사 만나피아 | A manufacturing method of water soluble chitosan |
| KR102206626B1 (en) | 2019-08-21 | 2021-01-22 | 조용수 | Continuously Variable Transmission shift system using rack and pinion gear system |
Also Published As
| Publication number | Publication date |
|---|---|
| KR950018054A (en) | 1995-07-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR100190723B1 (en) | Method for manufacturing chitin and chitosan for biomedical medicine | |
| Omar et al. | Upgrading the preparation of high-quality chitosan from Procambarus clarkii wastes over the traditional isolation of shrimp chitosan | |
| US20220356272A1 (en) | Processes for extracting and purifying chitin by using green solvents | |
| US20220135616A1 (en) | Method for extracting useful substances from shrimp shells | |
| CN114044835A (en) | Method for extracting chitin from crayfish shells by microwave-assisted eutectic solvent | |
| JP7075473B1 (en) | Chitin dissolving solvent and chitin elution method | |
| CN117820512A (en) | A method for removing protein from crayfish shells | |
| Trung et al. | Swollen-state preparation of chitosan lactate from moulted shrimp shells and its application for harvesting marine microalgae Nannochloropsis sp. | |
| KR20240032916A (en) | method | |
| KR0136551B1 (en) | Preparation of Chitin and Chitosan for In Vivo Clinical Medicine from Shrimp Crust | |
| US12077614B2 (en) | Method of industrial extraction of alginates from brown seaweed of the family sargassaceae of the order fucales | |
| CN105622778A (en) | Preparation method of water-soluble chitosan | |
| KR970009897B1 (en) | Preparation process of medical chitin and chitosan using low temperature treatment | |
| JP4468665B2 (en) | Production method of plant chitosan | |
| KR20030013804A (en) | Manufacturing process of chitin and chitosan | |
| CN117143364A (en) | A method for preparing lignin microspheres with controllable size and good biological activity | |
| CN104478010A (en) | Furfural-residue powdery processing agent for blue-green algae and preparation method thereof | |
| CN100396703C (en) | A kind of preparation method of chitosan | |
| CN1823856A (en) | Method of extracting polyphenol from pomegranate seed | |
| Loa-Ramírez et al. | Adaptation of the alginate production process for the brown alga Sargassum horridum (Fucales: Sargassaceae) | |
| CN115477602A (en) | Extraction process of astaxanthin ester in crayfish waste | |
| RU2147590C1 (en) | Method of preparing chitosan | |
| DE2036672B2 (en) | PROCESS FOR TREATMENT AND REMOVAL OF AQUATIC MEDIA CONTAMINATION | |
| KR0159971B1 (en) | Method for preparing low molecular weight chitosan of biomedical grade | |
| KR0139650B1 (en) | Process for preparing micro crystalline chitin |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A201 | Request for examination | ||
| PA0109 | Patent application |
St.27 status event code: A-0-1-A10-A12-nap-PA0109 |
|
| PA0201 | Request for examination |
St.27 status event code: A-1-2-D10-D11-exm-PA0201 |
|
| R17-X000 | Change to representative recorded |
St.27 status event code: A-3-3-R10-R17-oth-X000 |
|
| P11-X000 | Amendment of application requested |
St.27 status event code: A-2-2-P10-P11-nap-X000 |
|
| P13-X000 | Application amended |
St.27 status event code: A-2-2-P10-P13-nap-X000 |
|
| PG1501 | Laying open of application |
St.27 status event code: A-1-1-Q10-Q12-nap-PG1501 |
|
| E902 | Notification of reason for refusal | ||
| PE0902 | Notice of grounds for rejection |
St.27 status event code: A-1-2-D10-D21-exm-PE0902 |
|
| T11-X000 | Administrative time limit extension requested |
St.27 status event code: U-3-3-T10-T11-oth-X000 |
|
| T11-X000 | Administrative time limit extension requested |
St.27 status event code: U-3-3-T10-T11-oth-X000 |
|
| P11-X000 | Amendment of application requested |
St.27 status event code: A-2-2-P10-P11-nap-X000 |
|
| P13-X000 | Application amended |
St.27 status event code: A-2-2-P10-P13-nap-X000 |
|
| E701 | Decision to grant or registration of patent right | ||
| PE0701 | Decision of registration |
St.27 status event code: A-1-2-D10-D22-exm-PE0701 |
|
| GRNT | Written decision to grant | ||
| PR0701 | Registration of establishment |
St.27 status event code: A-2-4-F10-F11-exm-PR0701 |
|
| PR1002 | Payment of registration fee |
St.27 status event code: A-2-2-U10-U11-oth-PR1002 Fee payment year number: 1 |
|
| PG1601 | Publication of registration |
St.27 status event code: A-4-4-Q10-Q13-nap-PG1601 |
|
| R18-X000 | Changes to party contact information recorded |
St.27 status event code: A-5-5-R10-R18-oth-X000 |
|
| R18-X000 | Changes to party contact information recorded |
St.27 status event code: A-5-5-R10-R18-oth-X000 |
|
| PR1001 | Payment of annual fee |
St.27 status event code: A-4-4-U10-U11-oth-PR1001 Fee payment year number: 4 |
|
| PR1001 | Payment of annual fee |
St.27 status event code: A-4-4-U10-U11-oth-PR1001 Fee payment year number: 5 |
|
| PR1001 | Payment of annual fee |
St.27 status event code: A-4-4-U10-U11-oth-PR1001 Fee payment year number: 6 |
|
| PR1001 | Payment of annual fee |
St.27 status event code: A-4-4-U10-U11-oth-PR1001 Fee payment year number: 7 |
|
| PR1001 | Payment of annual fee |
St.27 status event code: A-4-4-U10-U11-oth-PR1001 Fee payment year number: 8 |
|
| PR1001 | Payment of annual fee |
St.27 status event code: A-4-4-U10-U11-oth-PR1001 Fee payment year number: 9 |
|
| FPAY | Annual fee payment |
Payment date: 20070122 Year of fee payment: 10 |
|
| PR1001 | Payment of annual fee |
St.27 status event code: A-4-4-U10-U11-oth-PR1001 Fee payment year number: 10 |
|
| LAPS | Lapse due to unpaid annual fee | ||
| PC1903 | Unpaid annual fee |
St.27 status event code: A-4-4-U10-U13-oth-PC1903 Not in force date: 20080124 Payment event data comment text: Termination Category : DEFAULT_OF_REGISTRATION_FEE |
|
| PC1903 | Unpaid annual fee |
St.27 status event code: N-4-6-H10-H13-oth-PC1903 Ip right cessation event data comment text: Termination Category : DEFAULT_OF_REGISTRATION_FEE Not in force date: 20080124 |
|
| P22-X000 | Classification modified |
St.27 status event code: A-4-4-P10-P22-nap-X000 |