[특허]Methods and apparatus for low heat spray drying

ZoomEssence, Inc.

검색어에 아래의 연산자를 사용하시면 더 정확한 검색결과를 얻을 수 있습니다.
검색연산자

검색도움말
검색연산자	기능	검색시 예
()	우선순위가 가장 높은 연산자	예1) (나노 (기계 \| machine))
공백	두 개의 검색어(식)을 모두 포함하고 있는 문서 검색	예1) (나노 기계) 예2) 나노 장영실
\|	두 개의 검색어(식) 중 하나 이상 포함하고 있는 문서 검색	예1) (줄기세포 \| 면역) 예2) 줄기세포 \| 장영실
!	NOT 이후에 있는 검색어가 포함된 문서는 제외	예1) (황금 !백금) 예2) !image
*	검색어의 *란에 0개 이상의 임의의 문자가 포함된 문서 검색	예) semi*
""	따옴표 내의 구문과 완전히 일치하는 문서만 검색	예) "Transform and Quantization"

과학기술 지식인프라 ScienceON

연합인증

연합인증 가입 기관의 연구자들은 소속기관의 인증정보(ID와 암호)를 이용해 다른 대학, 연구기관, 서비스 공급자의 다양한 온라인 자원과 연구 데이터를 이용할 수 있습니다.

이는 여행자가 자국에서 발행 받은 여권으로 세계 각국을 자유롭게 여행할 수 있는 것과 같습니다.

연합인증으로 이용이 가능한 서비스는 NTIS, DataON, Edison, Kafe, Webinar 등이 있습니다.

한번의 인증절차만으로 연합인증 가입 서비스에 추가 로그인 없이 이용이 가능합니다.

다만, 연합인증을 위해서는 최초 1회만 인증 절차가 필요합니다. (회원이 아닐 경우 회원 가입이 필요합니다.)

연합인증 절차는 다음과 같습니다.

최초이용시에는
ScienceON에 로그인 → 연합인증 서비스 접속 → 로그인 (본인 확인 또는 회원가입) → 서비스 이용

그 이후에는
ScienceON 로그인 → 연합인증 서비스 접속 → 서비스 이용

연합인증을 활용하시면 KISTI가 제공하는 다양한 서비스를 편리하게 이용하실 수 있습니다.

특허 상세정보

MyON담기

내보내기 페이스북 공유 트위터 공유 카카오톡 공유

Methods and apparatus for low heat spray drying

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	B05B-005/00
미국특허분류(USC)	239/690; 239/690.1
출원번호	US-0245369 (2011-09-26)
등록번호	US-8939388 (2015-01-27)
발명자 / 주소	Beetz, Charles P. Corbett, Robert Salem, David
출원인 / 주소	ZoomEssence, Inc.
대리인 / 주소	Hultquist, PLLC
인용정보	피인용 횟수 : 6 인용 특허 : 150

초록
▼

Methods and apparatus provide for spray drying a liquid product into a dried powder without applying heat, including: forming a slurry including a liquid solvent, a carrier, and an active ingredient; applying an electrostatic charge to the slurry; atomizing the charged slurry to produce a plurality of electrostatically charged, wet particles; suspending the electrostatically charged, wet particles for a sufficient time to permit repulsive forces induced by the electrostatic charge on at least some wet particles to cause at least some of such particles to divide into wet sub-particles; and continuing the suspending step, without the presence of any heated drying fluids, for a sufficient time to drive off a sufficient amount of the liquid solvent within most of the wet particles to leave a plurality of dried particles (the powder), each dried particle containing the active ingredient encapsulated within the carrier.

대표
청구항
▼

1. A system for spray drying a liquid product into a dried powder, comprising: a drying chamber, including an inlet end, an outlet end, and an internal volume within which the liquid product is dried in contact with a drying fluid therein;an atomizer adapted to receive the liquid product in a form including a liquid solvent, a carrier, and an active ingredient, and to discharge atomized liquid product into the drying chamber for contact with the drying fluid to form the dried powder containing the active ingredient encapsulated within the carrier;further comprising a source of said liquid solvent, a source of carrier, and a source of active ingredient(s), a tank equipped with a stirring device and arranged to receive liquid solvent, carrier, and active ingredient(s) from said sources to form the liquid product comprising a slurry having viscosity in a range of from 500 to 16,000 mPa-s, wherein the liquid solvent comprises water, wherein the carrier comprises starch, and wherein the drying fluid comprises air at temperature that is above freezing temperature of the liquid solvent and below 100° C. 2. A method for spray drying a liquid product into a dried powder without applying heat, comprising: providing a system according to claim 1;forming the liquid product as a slurry including a liquid solvent, a carrier, and an active ingredient;applying an electrostatic charge to the slurry;utilizing the atomizer, atomizing the charged slurry to produce a plurality of electrostatically charged, wet particles and discharging the electrostatically charged, wet particles into the drying chamber;suspending the electrostatically charged, wet particles in the drying chamber in contact with the drying fluid for a sufficient time to permit repulsive forces induced by the electrostatic charge on at least some wet particles to cause at least some of such particles to divide into wet sub-particles; andcontinuing the suspending step in the drying chamber, without the presence of any heated drying fluids at temperature in a range of 180 to 200° C., for a sufficient time to drive off a sufficient amount of the liquid solvent within most of the wet particles to leave a plurality of dried particles in the dried powder, each dried particle containing the active ingredient encapsulated within the carrier. 3. The method for spray drying of claim 2, wherein the drying fluid comprises a non-heated drying fluid. 4. The method for spray drying of claim 3, wherein a temperature of the drying fluid is less than about 100° C. at introduction into the drying chamber. 5. The method for spray drying of claim 4, wherein the temperature of the drying fluid is at least one of: less than about 75° C. at introduction into the drying chamber; less than about 45° C. at introduction into the drying chamber; less than about 35° C. at introduction into the drying chamber; less than about 30° C. at introduction into the drying chamber; and at about an ambient temperature of a room within which the drying chamber is located. 6. The method for spray drying of claim 3, further comprising dehumidifying the drying fluid prior to introduction into the drying chamber. 7. The method for spray drying of claim 3, further comprising applying the drying fluid under pressure to suspend and agitate the wet particles within the drying chamber. 8. The method for spray drying of claim 3, further comprising applying the drying fluid under pressure and in one or more direction to impart a swirling motion to the wet particles within the drying chamber. 9. The method for spray drying of claim 3, further comprising applying one or more electric fields within the drying chamber to urge at least one of the wet particles and the dried particles to travel in a direction defined from an inlet end of the drying chamber to an outlet end of the drying chamber. 10. The method for spray drying of claim 2, further comprising controlling a viscosity of the slurry during formation such that the viscosity of the slurry at the atomization step is at least one of: greater than about 300 mPa-s; greater than about 350 mPa-s; greater than about 400 mPa-s; greater than about 500 mPa-s; greater than about 600 mPa-s; greater than about 700 mPa-s; between about 500-16,000 mPa-s; and between about 1000-4000 mPa-s. 11. The method for spray drying of claim 2, wherein the liquid solvent comprises water, said method further comprising controlling a ratio of water within the slurry during formation such that the ratio of water within the slurry at the atomization step is at least one of: between about 20-50 weight percentage; between about 20-45 weight percentage; between about 20-45 weight percentage; between about 20-40 weight percentage; about 30 weight percentage. 12. The method for spray drying of claim 2, wherein the step of atomizing is carried out using at least one of: a nozzle technique, a centrifugal technique, a pneumatic technique, and an ultrasonic technique. 13. The method for spray drying of claim 2, wherein at least one of: the active ingredient includes at least one of foods, flavors, fragrances, medicaments, pigments, probiotics, bacteria;the carrier includes a modified starch; andthe liquid solvent includes water. 14. The system of claim 1, further comprising: a first electrode located at or near the inlet end of the drying chamber; anda second electrode located at or near the outlet end of the drying chamber,wherein application of a source of voltage potential between the first and second electrodes induces an electric field within the drying chamber sufficient to urge particles of the liquid product, produced by way of atomization, from the inlet end toward the outlet end of the drying chamber. 15. The system of claim 14, wherein the first and second electrodes are disposed external to the drying chamber, yet induce an electric field within the internal volume of the drying chamber by virtue of the formation of the drying chamber from the non-electrically conductive material. 16. The system of claim 1, wherein the atomizer comprises: a nozzle operating to atomize the liquid product comprising a slurry to produce a plurality of wet particles as said atomized liquid product discharged into the drying chamber for contact with the drying fluid. 17. The system of claim 16, further comprising at least one electrode operating to contact the slurry and apply an electrostatic charge thereto, such that the nozzle operates to produce a plurality of electrostatically charged wet particles. 18. The system of claim 17, wherein the at least one electrode is disposed within the nozzle such that the slurry contacts the electrode and becomes electrostatically charged while flowing from an inlet end to an outlet end of the nozzle. 19. The system of claim 16, wherein the nozzle includes an inlet for receiving a source of pressurized, drying fluid and an outlet end including a plurality of channels operating to direct the drying fluid to swirl as it leaves the nozzle, thereby imparting a swirling agitation to the plurality of wet particles as they leave the nozzle. 20. A dried powder, comprising: a plurality of dried particles formed by the method of claim 2, which individually contain an amount of final active ingredient encapsulated within the carrier resulting from drying the slurry containing initial active ingredient, the liquid solvent and the carrier, wherein:the initial active ingredient includes one or more constituent components, at least one of which is among one or more principle molecular types from which at least one of a desirable food, flavor, fragrance, medicament, and pigment is obtained;the final active ingredient includes one or more of the constituent components corresponding with those of the initial active ingredient as modified by the drying of the slurry; anda weight percentage of at least one of the one or more principle molecular types in the final active ingredient is within about 5% of a weight percentage of the corresponding principle molecular types in the initial active ingredient. 21. The dried powder of claim 20, wherein the weight percentage of at least one of the one or more principle molecular types in the final active ingredient is within about 3% of a weight percentage of the corresponding principle molecular types in the initial active ingredient. 22. The dried powder of claim 20, wherein the weight percentage of at least one of the one or more principle molecular types in the final active ingredient is within about 2% of a weight percentage of the corresponding principle molecular types in the initial active ingredient. 23. The dried powder of claim 20, wherein the weight percentage of at least one of the one or more principle molecular types in the final active ingredient is within about 1% of a weight percentage of the corresponding principle molecular types in the initial active ingredient. 24. A dried powder, comprising: a plurality of dried particles formed by the method of claim 2, which individually contain an amount of the active ingredient encapsulated within the carrier, wherein:the active ingredient includes one or more constituent components, at least one of which is among one or more principle molecular types from which at least one of a desirable food, flavor, fragrance, medicament, and pigment is obtained; anda weight percentage of at least one of the one or more principle molecular types in the active ingredient does not vary by more than about 5% during aging of the dried powder during any period of elevated temperature of about 95° F. up to about 1000 hours. 25. The dried powder of claim 24, wherein the weight percentage of at least one of the one or more principle molecular types in the active ingredient does not vary by more than about 3% during aging of the dried during any period of elevated temperature of about 95° F. up to about 1000 hours. 26. The dried powder of claim 24, wherein the weight percentage of at least one of the one or more principle molecular types in the active ingredient does not vary by more than about 2% during aging of the dried during any period of elevated temperature of about 95° F. up to about 1000 hours. 27. The dried powder of claim 24, wherein the weight percentage of at least one of the one or more principle molecular types in the active ingredient does not vary by more than about 1% during aging of the dried during any period of elevated temperature of about 95° F. up to about 1000 hours. 28. The system of claim 1, further comprising a source of said liquid solvent, a source of carrier, and a source of active ingredient(s), a tank equipped with a stirring device and arranged to receive liquid solvent, carrier, and active ingredient(s) from said sources to form the liquid product comprising a slurry having viscosity in a range of from 500 to 16,000 mPa-s, wherein the liquid solvent comprises water, wherein the carrier comprises starch, and wherein the drying fluid comprises air at temperature that is above freezing temperature of the liquid solvent and below 100° C. 29. A method of forming a dry powder comprising an active ingredient encapsulated within a carrier, said method comprising: providing a system according to claim 28;forming the slurry in the mixing tank from the liquid solvent, carrier, and active ingredient(s) while stirring the mixing tank with the stirring device;atomizing the slurry in the atomizer and discharging atomized slurry into the drying chamber for contact with the drying fluid to form the dried powder containing the active ingredient encapsulated within the carrier. 30. A dried powder containing an active ingredient encapsulated within a carrier, formed by the method of claim 29. 31. The system of claim 1, wherein the drying chamber is formed from a non-electrically conductive material.

이 특허에 인용된 특허 (150)

Kensil Charlotte A. (Milford MA) Soltysik Sean (Worcester MA) Marciani Dante J. (Birmingham AL). Modified saponins isolated from Quillaja saponaria. USP1995085443829.

Sprecker Mark A. (Sea Bright NJ) Hanna Marie R. (Hazlet NJ) Tokarzewski Richard J. (Keyport NJ) Belko Robert P. (Woodbridge NJ) Watkins Hugh (Lincroft NJ) Vock Manfred H. (Locust NJ). Mono-oxomethyl substituted polyhydrodimethanonaphthalene derivatives, organoleptic uses thereof and processes for prepar. USP1984104476042.

Nakamura Masayoshi (Koshigaya JPX) Abe Seizi (Tokyo JPX) Arai Takeshi (Kawasaki JPX). Multistage spray drying method for detergent slurry. USP1981044261793.

Boden Richard M. (Ocean NJ) Grim Claude (Keansburg NJ). Norbornyl pyridine derivatives. USP1987064677207.

Boden, Richard M.; Grim, Claude. Norbornyl pyridine derivatives, organoleptic uses of same, and the processes for preparing same. USP1985094539143.

Anthony Blake CH; Philip Attwool GB. Particulate flavor compositions and process to prepare same. USP200209RE37860.

Blake Anthony,CHX ; Attwool Philip,CHX. Particulate flavor compositions and process to prepare same. USP1998075786017.

Subramaniam Anandaraman (East Windsor NJ). Particulate hydrogenated starch hydrolysate based flavoring materials and use of same. USP1996045506353.

Holzner,G？nter; Moser,Andr？. Perfuming or flavoring microcapsules comprising a fireproofing agent. USP2007047204998.

Klesse Wolfgang (Mainz DEX) Rauch Hubert (Weiterstadt DEX) Arndt Peter J. (Seeheim-Jugenheim DEX) Suetterlin Norbert (Muehital-Nieder-Beerbach DEX). Polymer powders of low fines content and method for making the same by spray drying. USP1990014892910.

Weyand John D. (Greensburg PA). Powder treatment process. USP1988024724121.

Hagiwara Yoshihide (Takarazuka JPX) Hagiwara Hideaki (Takarazuka JPX). Powders of plant green juice and process for their production. USP1995085445839.

Williams ; Wilmore. Preparation of a tuberculosis test medium by reconstituting a storage stabilized dry powdered Lowenstein-Jensen medium. USP1978024072570.

Percel Phillip J. (Parma OH) Perkins Douglas W. (Medina OH) Petricca Anthony V. (Rocky River OH). Preparation of acidulated meat emulsions. USP1985044511592.

Hansen,Ove Emil. Process and apparatus for agglomeration of powders. USP2006107128936.

Getler Jens,DKX ; Thomsen Poul,DKX ; Peters Lars Valentin,DKX. Process and apparatus for converting liquid whey into powder. USP2000046048565.

Pisecky Jan (Taastrup DKX) Hansen Soren P. (Humlebaek DKX). Process and spray drying apparatus for producing stable particle agglomerates. USP1992035100509.

Mookherjee Braja D. (Holmdel NJ) Trenkle Robert W. (Bricktown NJ) Wolff Robin K. (Point Pleasant NJ) Boden Richard M. (Ocean NJ) Yoshida Takao (West Long Branch NJ). Process for augmenting or enhancing the tropical fruit aroma or taste of a foodstuff or chewing gum using a mixture of a. USP1984114481221.

Keller, A. Kent. Process for drying high-lactose aqueous fluids. USP2010017651713.

Larsen Torben Brinch,DKX. Process for extracting roasted and ground coffee. USP1998115840360.

Reijmer Henricus Gerardus Maria,NLX ; Shefer Adi. Process for forming solid phase controllably releasable fragrance-containing consumable articles. USP2001036200949.

Jaeggi Kurt (Dubendorf CH) Krasnobajew Victor (Zollikerberg CH) Weber Peter (Greifensee CH) Wild Jost (Uster CH). Process for making and flavorants from milk products and compositions containing same. USP1977014001437.

Pittet Alan O. (Atlantic Highlands NJ) Muralidhara Ranya (Fair Haven NJ) Hagedorn Myrna L. (Edison NJ). Process for preparing 4,4A,5,6-tetrahydro-7-methyl-2-(3H)-naphthalenone, intermediates used in said process and novel cr. USP1988124794193.

Boden Richard M. (Ocean NJ) Tyszkiewicz Theodore J. (Sayreville NJ) Licciardello Michael (Farmingdale NJ) Vock Manfred H. (Locust NJ) Vinals Joaquin F. (Rumson NJ) Whalen Patrick (Matawan NJ) Hanna M. Process for preparing a methoxybenzaldehyde from the corresponding phenolic benzaldehyde. USP1985054515987.

Seiter Wolfgang (Lorbeerweg 7 4040 Neuss 21 DEX) Koch Otto (Vogelwarte 15 5653 Leichlingen DEX). Process for preparing a phosphate-reduced granular detergent. USP1989074849125.

Sprecker Mark A. (Sea Bright NJ) Wiegers Wilhelmus J. (Red Bank NJ) Belko Robert P. (Woodbridge NJ) Boden Richard M. (Ocean NJ). Process for preparing alkyl substituted and unsubstituted para-carboalkoxy cyclohexanones. USP1987074681976.

Sprecker Mark A. (Sea Bright NJ) Wiegers Wilhelmus J. (Red Bank NJ) Belko Robert P. (Woodbridge NJ) Boden Richard M. (Ocean NJ). Process for preparing alkyl substituted para-carboalkoxy cyclohexanones. USP1986094614831.

Bouwmeesters, Johnny Franciscus; De Roos, Kris Bart. Process for preparing beads as food additive and product thereof. USP2005086929814.

De Roos Kris Bart,CHX ; Wetli Markus,CHX. Process for preparing beads as food or tobacco additive. USP2001126325859.

Buckholz ; Jr. Lawrence L. (Middletown NJ) Kasper-Lehmann Robin (Elberon NJ). Process for preparing marinaded proteinaceous product and product produced thereby. USP1991045004618.

Sugiura Masahisa (Tsu JPX) Okada Kazuhiro (Tsu JPX) Nagata Sadao (Saitama-ken JPX). Process for preparing powdered seasonings. USP1997125702749.

Jensen, John. Process for producing a milk or whey product having a reduced spores and bacteria content. USP2003116652898.

Pisecky Jan (Tstrup DKX) Krag Jens (Copenhagen DKX) Sorensen Ib H. (Frederikssund DKX). Process for producing an agglomerated powdery milk product. USP1984124490403.

Pisecky Jan (Tastrup DK) Westergaard Vagn (Tastrup DK). Process for producing powder from milk or similar liquids. USP1976053956521.

Newhall Ralph P. (Princeton NJ) Voyton Ronald A. (Princeton NJ). Process for the aromatization of dry vegetable matter. USP1992035094860.

Keller Alfred (Zurich CHX) Krasnobajew Victor (Ksnacht CHX) Mor Juan-Ramon (Zurich CHX) Steiner Rudolf (Bassersdorf CHX). Process for the manufacture of novel coffee flavorants. USP1992075130149.

Ove Emil Hansen DK; Per Bo S?rensen DK; J?rgen Ilkjaer DK; Jens Mourits S?rensen DK. Process for the preparation of a water soluble coffee or tea product from a non-rewetted particulate material obtained from an extract by drying. USP2002126497911.

Balliello Paolo (Rheinfelden DEX) Bruttel Beat (Bckten CHX) Will Hanspeter (Frenkendorf CHX). Process for the preparation of granules containing an active substance and to the use thereof as speckles for treating s. USP1988084762636.

Benczedi, Daniel; Bouquerand, Pierre-Etienne. Process for the preparation of granules for the controlled release of volatile compounds. USP2003086607771.

Seiter Wolfgang (Neuss DEX) Wegener Ingo (Duesseldorf DEX) Reuter Herbert (Hilden DEX). Process for the production of a spray-dried nonionic washing aid. USP1987044661281.

Johnson David A. (Hudson WI) Lorch Jeffrey D. (Hudson WI). Process of treating water containing effluent from cheese-making operations. USP1994085338553.

Bauer Herbert Edward (Saddle Brook NJ) Goossens Bertus (Vlaardinger NL) Kock Theodorus Joannes (Heenvliet NL) Manders Johannes Laurentius Cornelis (Roosendaal NL). Production of detergent compositions. USP1977064032465.

Seino Junzaburo (Osaka JPX) Ikeda Hiroshi (Nara JPX) Abo Washohati (Osaka JPX) Minami Iwao (Osaka JPX) Fuji Joji (Aomori JPX). Production of dyestuff powders. USP1982124362273.

Lars Valentin Peters DK; Ole Teglhus Kragh DK. Production of protein-containing powdery product. USP2002056391361.

Lowery Richard E. (Tulsa OK) Fentress Denton C. (Pawhuska OK) Godbehere Don W. (Ochelata OK). Rapidly dispersible compositions of antimony pentoxide. USP1989024804496.

Mutka, Jerry Richard; McIver, Robert Clark; Palmer, Christine Ann; Benczedi, Daniel; Bouquerand, Pierre-Etienne; Firmenich, Antoine. Solid delivery systems for aroma ingredients. USP2003086607778.

Chickering, III, Donald E.; Keegan, Mark J.; Randall, Greg; Bernstein, Howard; Straub, Julie. Spray drying apparatus and methods of use. USP2003056560897.

Tanaka Toshiyuki (Yokohama JPX) Kodera Akira (Yokohama JPX). Spray drying apparatus equipped with a spray nozzle unit. USP1993075227017.

Bordelon Kent J. (Lake Charles LA) Eschenbacher Robert C. (Lake Charles LA) Bridendall William H. (Cleveland TN). Spray drying apparatus for available chlorine-containing compounds. USP1983124422900.

Pisecky Jan (Tastrup DKX) Sorensen Ib H. (Frederikssund DKX). Spray drying atomizer wheel. USP1979024141783.

Petersen Mogens (No. 31 Tjornevej 2800 Lyngby DK) Gude Klaus Erik (No. 22 Viekaer 2950 Vedbaek DK). Spray drying device for the production of powder, e.g. milk powder. USP1976063963559.

Bach Poul,DKX ; Masters Keith,DKX. Spray drying method and apparatus and cleaning method for such an apparatus. USP2000056058624.

Platz, Robert M.; Patton, John S.; Foster, Linda; Eljamal, Mohammed. Spray drying of macromolecules to produce inhaleable dry powders. USP2003066582728.

Ribnitz Peter (St. Gall CHX) Giesinger Hans (St. Gall CHX) Buschor Karl (St. Gall CHX). Spray method and spray device, particularly for the spray-coating of articles with powder. USP1981114302481.

Subramaniam, Anandaraman; McIver, Robert Clark; Vlad, Florin Joseph; Benczedi, Daniel. Spray-dried compositions and method for their preparation. USP2004046723359.

Bokovi Marijan A. (Ridgefield CT) Vidal Susan M. (Patterson NY) Saleeb Fouad Z. (Pleasantville NY). Spray-dried fixed flavorants in a carbohydrate substrate and process. USP1992065124162.

Cannalonga Marco Alfred (Fort Lee NJ) Czarecki Louis Vincent (Succasunna NJ). Spray-drying technique for preparing agglomerated powders. USP1976063962384.

Gordon Marc S. ; Clark Andrew ; Brewer Thomas K.. Systems and processes for spray drying hydrophobic drugs with hydrophilic excipients. USP2000066077543.

Hall John B. (Rumson NJ) Yoshida Takao (West Long Branch NJ). Tertiary pentamethylindanol derivatives and organoleptic uses thereof. USP1985084535192.

Boden Richard M. (Ocean NJ) McGhie Joseph A. (South Orange NJ). Tetrahydro-5-isopropyl-2-methyl-2-thiophene acetonitrile, organoleptic uses thereof and process for preparing same. USP1989114883884.

Boden Richard M. (Ocean NJ) McGhie Joseph A. (South Orange NJ). Tetrahydro-5-isopropyl-2-methyl-2-thiophene acetonitrile, organoleptic uses thereof and process for preparing same. USP1990084950495.

Agawa, Tetsuro; Okada, Katsuhiko; Tanaka, Hiroo; Hashimoto, Masaya; Asakura, Takaaki. Thermosetting powder coating composition, method of preparation thereof and coated article therewith. USP2003116649267.

Pittet Alan O. (Atlantic Highlands NJ) Muralidhara Ranya (Fair Haven NJ) Vock Manfred H. (Locust NJ) Miller Kevin P. (Middletown NJ) Luccarelli ; Jr. Domenick (Neptune NJ). Thiogeranyl esters and organoleptic uses thereof. USP1986074600576.

Lipp Charles W. (Baton Rouge LA). Two-fluid nozzle for atomizing a liquid-solid slurry. USP1987074679733.

Hall John B. (Rumson NJ) Yoshida Takao (West Long Branch NJ). Use in augmenting or enhancing the aroma or taste of foodstuffs or chewing gums of tetrahydro-1,1,2,3,3-pentamethyl-3A[4. USP1985054520032.

Mookherjee Braja D. (Holmdel NJ) Trenkle Robert W. (Point Pleasant NJ) Calderone Nicholas (Laurel Hollow NY) Sands Keith P. (Marlboro NJ) Hagedorn Myrna L. (Edison NJ). Use of Schiff base reaction product of methyl anthranilate and canthoxal in augmenting or enhancing aroma or taste of fo. USP1989064840801.

Ley,Jakob Peter; Krammer,Gerhard; Muche,Sylvia; Kindel,G��nter; Reiβ,Ingo. Use of ferulic acid amides as flavor compounds. USP2008057378121.

Rossy Phillip A. ; Davidson Richard H. ; Miller Kevin P. ; Warder Ira T. ; Schulman Marvin ; Pittet Alan Owen ; Bolen Paul L. ; Hawn Regina D.. Use of spray-dried and freeze-dried sugarcane leaf essence in improving taste of flavored calcium supplements, foodstuffs, beverages, chewing gum, oral care compositions and calcium supplement. USP2001066251463.

Penzel Erich (Ludwigshafen DEX) Franzmann Gernot (Bobenheim DEX) Angel Maximilian (Schifferstadt DEX) Pakusch Joachim (Ludwigshafen DEX) Schuler Bernhard (Mannheim DEX). Use of unsaturated sulfonic acid polymers as spray drying assistants. USP1995105462978.

Hall John B. (Rumson NJ). Uses of methyl phenyl pentanol derivatives in augmenting or enhancing the aroma or taste of consumable materials. USP1986124632831.

Deming John M. (Hazelwood MO) Surgant ; Sr. John M. (Ladue MO). Water-dispersible granules and process for the preparation thereof. USP1994105354742.

이 특허를 인용한 특허 피인용횟수: 6

IPC 상위 출원인

내보내기

상세정보
내보내기 구분	파일저장 인쇄 메일전송
구성항목	관리번호, 국가코드, 자료구분, 상태, 출원번호, 출원일자, 공개번호, 공개일자, 등록번호, 등록일자, 발명명칭(한글), 발명명칭(영문), 출원인(한글), 출원인(영문), 출원인코드, 대표IPC 관리번호, 국가코드, 자료구분, 상태, 출원번호, 출원일자, 공개번호, 공개일자, 공고번호, 공고일자, 등록번호, 등록일자, 발명명칭(한글), 발명명칭(영문), 출원인(한글), 출원인(영문), 출원인코드, 대표출원인, 출원인국적, 출원인주소, 발명자, 발명자E, 발명자코드, 발명자주소, 발명자 우편번호, 발명자국적, 대표IPC, IPC코드, 요약, 미국특허분류, 대리인주소, 대리인코드, 대리인(한글), 대리인(영문), 국제공개일자, 국제공개번호, 국제출원일자, 국제출원번호, 우선권, 우선권주장일, 우선권국가, 우선권출원번호, 원출원일자, 원출원번호, 지정국, Citing Patents, Cited Patents
저장형식	Text(ASCII format) Excel format PIAS분석(.xls)
메일정보	받는사람 (필수) @ 보내는사람 (선택) @ 제목 내용 KISTI 검색결과 이메일 서비스
안내	> 총 건의 자료가 검색되었습니다. > 다운받으실 자료의 인덱스를 입력하세요. (1-10,000) > 검색결과의 순서대로 최대 10,000건 까지 다운로드가 가능합니다. > 데이타가 많을 경우 속도가 느려질 수 있습니다.(최대 2~3분 소요) > 다운로드 파일은 UTF-8 형태로 저장됩니다. 파일의 내용이 제대로 보이지 않을실 때는 웹브라우저 상단의 보기 -> 인코딩 -> 자동선택 여부를 확인하십시오 > ~ > Text(ASCII format) Excel format

과학기술 지식인프라 ScienceON

ScienceON Chatbot

연합인증

특허 상세정보

Methods and apparatus for low heat spray drying

초록
▼

대표
청구항
▼

이 특허에 인용된 특허 (150)

이 특허를 인용한 특허 피인용횟수: 6

IPC 상위 출원인

과제정보

상세정보조회

원문조회

IPC 상세정보(version : 201201)

연구과제 성과물(0)

참여연구원의 다른 문헌(0)

처리중입니다.

잠시만 기다려주세요.

ScienceON Chatbot

연합인증

특허 상세정보

Methods and apparatus for low heat spray drying

초록 ▼

대표청구항 ▼

이 특허에 인용된 특허 (150)

이 특허를 인용한 특허 피인용횟수: 6

IPC 상위 출원인

과제정보

상세정보조회

원문조회

IPC 상세정보(version : 201201)

연구과제 성과물(0)

참여연구원의 다른 문헌(0)

처리중입니다.

잠시만 기다려주세요.

초록
▼

대표
청구항
▼