101 |
Dextrose in powder form and a process for the preparation thereof |
US09464024 |
1999-12-15 |
US06451122B1 |
2002-09-17 |
Franck Moraly; Erik Labergerie; José Lis; Philippe Lefevre |
The invention relates to a dextrose in powder form, characterized in that it has a dextrose content at least equal to 99%, a &agr; crystalline form content at least equal to 95%, a water content at most equal to 1% and a compressibility, determined according to a test A, at least equal to 80 N, preferably in the range 100 N and 200 N. The invention also relates to the use of said dextrose in powder form as a sweetener or excipient, particularly in food or pharmaceutical compositions, for example, for the preparation of confectionery or of tablets to be sucked, chewed, dissolved or swallowed. |
102 |
Process for separating arabinose from a mixture of aldoses |
US948384 |
1986-12-31 |
US4880919A |
1989-11-14 |
Santi Kulprathipanja |
Arabinose is separated from mixtures of monosaccharides containing arabinose and other aldopentoses and aldohexoses by adsorption on sulfonated polystyrene divinylbenzene crosslinked ion exchange resins exchanged with calcium-ammonium cationic and desorbing the adsorbate with water. The other saccharides are removed from the adsorption process in the raffinate. |
103 |
Method for glucose extraction from green crops |
US185178 |
1980-09-08 |
US4359532A |
1982-11-16 |
Melvin H. Brown |
An improved method suitable for extracting glucose from green crops, such as leaves, grasses, legumes, stems of green plants and tree leaves. The method comprises the steps of subjecting the green crops to a pulping action in an organic acid solution recirculated from a subsequent fermentation separation step to produce a pulp comprising a protein-rich liquid and fibrous material, separating protein-rich liquid in the pulp from the fibrous material and separating protein from the protein-rich liquid by initiating anaerobic fermentation in an acidic solution thereby providing a concentrated protein fraction suitable for preservation and an acidic solution. At least a portion of the acidic solution is recycled to the separation step, the recycling of the solution being provided for purposes of washing the fibrous material to remove residual protein therefrom. The fibrous material is then subjected to hydrolysis with at least one material selected from the group consisting of mineral acids and enzymes to permit increased recovery of glucose. |
104 |
Method for drying glucose solutions |
US3674556D |
1971-05-03 |
US3674556A |
1972-07-04 |
GRAY ROLAND H JR |
IN A PROCESS FOR PREPARING DRIED, SOLID, GLUCOSE-CONTAINING PRODUCTS FROM GLUCOSE-CONTAINING SOLUTIONS BY DRYING DROPLETS OF THE SOLUTION IN A CURRENT OF HEATED AIR AND IN THE PRESENCE OF SEPARATELY INTRODUCED RECYCLED DRIED PRODUCT SOLIDS, THE IMPROVEMENT WHICH COMPRISES MAINTAINING THE INLET TEMPERATURE OF THE HEATED AIR IN THE RANGE OF FROM 400* TO 500* FABRENHEIT AND THE AVERAGE AIR RESIDENCE TIME IN THE DRYING ZONE IN THE RANGE OF 2 TO 60 SECONDS.
|
105 |
System for continuously dissolving dextrose |
US20128762 |
1962-06-11 |
US3150006A |
1964-09-22 |
OPILA ROBERT L |
|
106 |
Conversion of lactose to glucose and galactose with a minimum production of oligosaccharides |
US50467355 |
1955-04-28 |
US2826502A |
1958-03-11 |
THEODORE SFORTUNATO; CONNORS WILLIAM M |
|
107 |
Solid corn syrup manufacture |
US42834442 |
1942-01-27 |
US2439384A |
1948-04-13 |
FETSER WALTER R |
|
108 |
Spray drying starch conversion syrup |
US58385945 |
1945-03-20 |
US2433818A |
1947-12-30 |
SCHOPMEYER HERMAN H |
|
109 |
Method for dewatering starch conversion syrup |
US57951445 |
1945-02-24 |
US2429964A |
1947-10-28 |
SCHOPMEYER HERMAN H; HAMMERSTEIN FRED J; LARMOUTH GENERAL W |
|
110 |
Dissolving dried starch conversion solids |
US44026742 |
1942-04-23 |
US2370123A |
1945-02-27 |
BUCHANAN BEN F |
|
111 |
Method of manufacturing dried starch conversion products |
US33175740 |
1940-04-26 |
US2245309A |
1941-06-10 |
WALSH JAMES F |
|
112 |
Dextrose solution |
US12554337 |
1937-02-13 |
US2151499A |
1939-03-21 |
HALL BUCHANAN JOHN |
|
113 |
Dried corn sirup product and method of producing the same |
US5940836 |
1936-01-16 |
US2149517A |
1939-03-07 |
FLEMING RAPHAEL S; PARKER FREDERICK D; GERE HAWLEY WILLIAM |
|
114 |
Production of cereal sugar in loaf or block form |
US75887524 |
1924-12-30 |
US1575975A |
1926-03-09 |
DALY RAYMOND E |
|
115 |
바이오매스로부터 글루코오즈의 제조방법 |
KR1020120018283 |
2012-02-23 |
KR1020130096798A |
2013-09-02 |
황인택; 박노중; 임희경; 이기인 |
PURPOSE: A manufacturing method of glucose from biomass in a natural state by using room temperature ionic liquid is provided. CONSTITUTION: Room temperature ionic liquid is treated in biomass including cellulose, hemicellulose and lignin to dissolve cellulose. The room temperature ionic liquid is removed to recrystallize cellulose. Cellulase is treated to the recrystallized cellulose to obtain glucose. The biomass is at least one type of plant selected from the group consisting of bagasse, yellow poplar, hybrid poplar, oak, pinus densiflora, and rice hulls. The biomass is biomass as natural state itself or biomass only treated physically. The removing of the room temperature ionic liquid is performed by treating with an antisolvent. |
116 |
고압 압출 분쇄 공정을 포함하는 해조류 또는 농산부산물의 당화방법 |
KR1020120039981 |
2012-04-17 |
KR101233277B1 |
2013-02-14 |
이현용; 최운용; 이춘근; 서용창; 김지선; 송치호; 정경환; 이상은; 강도형 |
PURPOSE: A method for saccharification of biomass such as marine algae or agricultural by-products is provided to enable hydrolysis of non-degradable polymers with a high saccharifying efficiency. CONSTITUTION: A method for saccharification of marine algae or agricultural by-products comprises: a step of homogenizing and crushing the marine algae or agricultural by-products; and a step of extruding the crushed marine algae or agricultural by-products through a pipe with a diameter of 10-500 um. The marine algae or agricultural by-products are homogenized by rotating at 10,000-50,000 rpm using a homogenizer. The method further comprises a step of extracting the extruded marine algae or agricultural by-products by hot water extraction or high pressure liquefaction and treating with an enzyme. The enzyme is cellulase, amyloglucosidase, beta-agarase, beta-galatosidase, beta-glucosidase, endo-1,4-beta-glucanase, alpha-amylase, or beta-amylase. The marine algae are red algae, brown algae, green algae, or microalgae. [Reference numerals] (AA) Bio mass(seaweed or agricultural byproducts); (BB) Homogenization; (CC) Extrusion(pulverized into nanoparticles); (DD) Hot water extraction; (EE) Extraction by high pressure liquefaction; (FF) Enzymatic saccharification process; (GG) Generating final saccharificated products |
117 |
해조류 추출물로부터 불균일계 촉매를 이용한 가수분해를 통해 바이오 연료를 제조하는 방법 |
KR1020090015275 |
2009-02-24 |
KR1020100096408A |
2010-09-02 |
윤영식; 고기호; 송종희; 오승훈; 조인호; 강신영; 박철희; 이성호 |
PURPOSE: A method for manufacturing biofuels is provided to reduce by-product process costs and production costs through hydrolysis of seaweed extract using a heterogeneous catalyst, to enable a user to recycle the heterogeneous catalyst, and to remarkably improving productivity. CONSTITUTION: A method for manufacturing biofuels comprises a step of hydrolyzing seaweed extract, which is extracted from red algae, brown algae, and green algae, using a heterogeneous catalyst and a step of fermenting Hydrolysates using microorganisms or through chemical reactions. The red algae include laver, gelidium amansii, and gracilaria. The brown algae include sea mustard, kelp, sea weed fusiforme, gulfweed, Ecklonia stolonifera, and sea oak. |
118 |
분말형 덱스트로우즈 및 이의 제조방법 |
KR1019990061153 |
1999-12-23 |
KR100652280B1 |
2006-11-29 |
모랄리프랑크; 라베르제리에릭; 리스죠제; 르페브르필립 |
본 발명은 적어도 99%의 덱스트로우즈 함량, 적어도 95%의 α결정형 함량, 최대 1%의 물 함량 및 적어도 80N, 바람직하게는 100N 내지 200N의, 테스트 A에 따라 결정된 압축성을 갖는 것을 특징으로 하는 분말형 덱스트로우즈에 관한 것이다. 또한, 본 발명은 흡수되거나, 씹혀지거나, 용해되거나 삼켜지는 정제 또는 제과의 제조를 위해 식품 또는 약학 조성물 내에 감미료 또는 부형제로서 상기 분말형 덱스트로우즈의 사용에 관한 것이다.
덱스트로우즈, 식품, 약학, 정제, 분말 |
119 |
분말형 덱스트로우즈 및 이의 제조방법 |
KR1019990061153 |
1999-12-23 |
KR1020000062227A |
2000-10-25 |
모랄리프랑크; 라베르제리에릭; 리스죠제; 르페브르필립 |
본발명은적어도 99%의덱스트로우즈함량, 적어도 95%의α결정형함량, 최대 1%의물 함량및 적어도 80N, 바람직하게는 100N 내지 200N의, 테스트 A에따라결정된압축성을갖는것을특징으로하는분말형덱스트로우즈에관한것이다. 또한, 본발명은흡수되거나, 씹혀지거나, 용해되거나삼켜지는정제또는제과의제조를위해식품또는약학조성물내에감미료또는부형제로서상기분말형덱스트로우즈의사용에관한것이다. |
120 |
바이오매스의 당화 |
KR1020177033867 |
2010-02-11 |
KR1020170132357A |
2017-12-01 |
메도프,마샬; 마스터맨,토마스 |
바이오매스(예컨대, 식물바이오매스, 동물바이오매스및 도시폐 바이오매스)가연료등과같은유용한생성물을생산하도록가공처리된다. 예를들어, 공급원료재료를당 용액으로전환시키고나서발효시켜에탄올을생성할수 있는시스템이기재되어있다. |