RU99121335A - METHOD FOR PRODUCING SOLID CARAMEL AND TABLETS - Google Patents

METHOD FOR PRODUCING SOLID CARAMEL AND TABLETS

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Publication number
RU99121335A
RU99121335A RU99121335/13A RU99121335A RU99121335A RU 99121335 A RU99121335 A RU 99121335A RU 99121335/13 A RU99121335/13 A RU 99121335/13A RU 99121335 A RU99121335 A RU 99121335A RU 99121335 A RU99121335 A RU 99121335A
Authority
RU
Russia
Prior art keywords
mixture
glucopyranosyl
sorbitol
zone
melt
Prior art date
Application number
RU99121335/13A
Other languages
Russian (ru)
Other versions
RU2185072C2 (en
Inventor
Ингрид Виллибальд-Эттле
Ондрей МИКЛА
Original Assignee
Зюдцукер Акциенгезелльшафт Маннхайм/Оксенфурт
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
Priority claimed from DE19709304A external-priority patent/DE19709304C2/en
Application filed by Зюдцукер Акциенгезелльшафт Маннхайм/Оксенфурт filed Critical Зюдцукер Акциенгезелльшафт Маннхайм/Оксенфурт
Publication of RU99121335A publication Critical patent/RU99121335A/en
Application granted granted Critical
Publication of RU2185072C2 publication Critical patent/RU2185072C2/en

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Claims (19)

1. Способ получения стекловидного расплава из по меньшей мере одной смеси подслащивающих веществ посредством экструдера, в частности двухшнекового экструдера, при этом смесь подслащивающих веществ подают в зону загрузки (110) экструдера (100), экструдируют в зоне плавления (120) при повышенной температуре, в зоне вакуумирования (130) при пониженном давлении и повышенной температуре и затем в зоне охлаждения (140) при пониженной температуре, и получают стекловидный расплав.1. A method of producing a vitreous melt from at least one mixture of sweeteners by means of an extruder, in particular a twin-screw extruder, wherein the mixture of sweeteners is fed into the loading zone (110) of the extruder (100), extruded in the melting zone (120) at elevated temperature, in the vacuum zone (130) at reduced pressure and elevated temperature and then in the cooling zone (140) at reduced temperature, a glassy melt is obtained. 2. Способ по п.1, отличающийся тем, что в зоне плавления (120) температура составляет от 130o до 210oC, предпочтительно от 170o до 210oC.2. The method according to claim 1, characterized in that in the melting zone (120) the temperature is from 130 o to 210 o C, preferably from 170 o to 210 o C. 3. Способ по пп.1, 2, отличающийся тем, что в зоне вакуумирования (130) температура составляет от 120o до 160oC, предпочтительно 133oC.3. The method according to claims 1, 2, characterized in that in the vacuum zone (130) the temperature is from 120 o to 160 o C, preferably 133 o C. 4. Способ по пп.1 - 3, отличающийся тем, что в зоне вакуумирования (130) давление составляет от 0,70 до 0,98 бар, предпочтительно 0,78 бар. 4. The method according to claims 1 to 3, characterized in that in the evacuation zone (130) the pressure is from 0.70 to 0.98 bar, preferably 0.78 bar. 5. Способ по пп. 1 - 4, отличающийся тем, что в зоне охлаждения (140) температура составляет от 60o до 130oC, предпочтительно от 80o до 120oC.5. The method according to PP. 1 to 4, characterized in that in the cooling zone (140) the temperature is from 60 o to 130 o C, preferably from 80 o to 120 o C. 6. Способ по пп.1 - 5, отличающийся тем, что зона плавления (120) разделена на несколько имеющих различную температуру сегментов (2, 3, 4, 5), предпочтительно на четыре сегмента (2, 3, 4, 5) с температурами 177oC, 205oC, 188oC и 191oC, соответственно.6. The method according to claims 1 to 5, characterized in that the melting zone (120) is divided into several segments having different temperature (2, 3, 4, 5), preferably into four segments (2, 3, 4, 5) s temperatures of 177 o C, 205 o C, 188 o C and 191 o C, respectively. 7. Способ по пп.1 - 6, отличающийся тем, что зона охлаждения (140) разделена на несколько имеющих различную температуру сегментов (1, 8, 9), предпочтительно три сегмента (7, 8, 9) с температурами 120oC, 120oC и 80oC, соответственно.7. The method according to claims 1 to 6, characterized in that the cooling zone (140) is divided into several segments with different temperatures (1, 8, 9), preferably three segments (7, 8, 9) with temperatures of 120 o C, 120 o C and 80 o C, respectively. 8. Способ по пп.1 - 7, отличающийся тем, что стекловидный расплав отводят снизу из последнего сегмента (9) экструдера (100). 8. The method according to claims 1 to 7, characterized in that the vitreous melt is removed from the bottom from the last segment (9) of the extruder (100). 9. Способ по пп.1 - 8, отличающийся тем, что после выхода из экструдера (100) стекловидный расплав охлаждают далее, в частности на ленточном транспортере для охлаждения. 9. The method according to claims 1 to 8, characterized in that after leaving the extruder (100), the vitreous melt is cooled further, in particular on a conveyor belt for cooling. 10. Способ по пп.1 - 9, отличающийся тем, что экструдер (100) работает с частотой вращения 8 оборотов в минуту. 10. The method according to claims 1 to 9, characterized in that the extruder (100) operates at a speed of 8 revolutions per minute. 11. Способ по пп.1 - 10, отличающийся тем, что в зоне охлаждения (140) в расплав вводят ароматизирующие вещества, минералы, соли, вкусовые, душистые вещества, красители или фармакологически активные вещества. 11. The method according to claims 1 to 10, characterized in that in the cooling zone (140) flavoring substances, minerals, salts, flavoring, aromatic substances, colorants or pharmacologically active substances are introduced into the melt. 12. Способ по пп. 1 - 11, отличающийся тем, что содержащиеся в смеси подслащивающие вещества представляют собой моносахарид, дисахарид, полисахарид, спирт, дающий при окислении моносахарид, полидекстрозу, мальтодекстрин, инулин или смесь этих веществ. 12. The method according to PP. 1 to 11, characterized in that the sweeteners contained in the mixture are a monosaccharide, disaccharide, polysaccharide, alcohol, which gives monosaccharide, polydextrose, maltodextrin, inulin or a mixture of these substances during oxidation. 13. Способ по пп.1 - 12, отличающийся тем, что подслащивающие вещества, содержащиеся в смеси, представляют собой ксилозу, рибулозу, глюкозу, маннозу, галактозу, фруктозу, мальтозу, инвертный сахар, гидратированный и негидратированный гидролизат крахмала, сорбит, ксилит, лактит, маннит, галактит, мальтит, 1,1-ГПМ (1-0-α-Д-глюкопиранозил-Д-маннит), 1,1-ГПС (1-0-α-Д-глюкопиранозил-Д-сорбит), 1,6-ГПС (6-0-α-Д-глюкопиранозил-Д-сорбит), изомальтулозу, мальтулозу, сахарозу, трегалюлозу, лактулозу или смесь этих веществ. 13. The method according to claims 1 to 12, characterized in that the sweeteners contained in the mixture are xylose, ribulose, glucose, mannose, galactose, fructose, maltose, invert sugar, hydrated and non-hydrated starch hydrolyzate, sorbitol, xylitol, lactitol, mannitol, galactitol, maltitol, 1,1-GPM (1-0-α-D-glucopyranosyl-D-mannitol), 1,1-GPS (1-0-α-D-glucopyranosyl-D-sorbitol), 1,6-GPS (6-0-α-D-glucopyranosyl-D-sorbitol), isomaltulose, maltulose, sucrose, trehalulose, lactulose or a mixture of these substances. 14. Способ по пп.1 - 13, отличающийся тем, что смесь подслащивающих веществ представляет собой предпочтительно почти эквимолярную смесь 1,6-ГПС (6-0-α-Д-глюкопиранозил-Д-сорбита) и 1,1-ГПМ (1-0-α-Д-глюкопиранозил-Д-маннита). 14. The method according to claims 1 to 13, characterized in that the mixture of sweeteners is preferably an almost equimolar mixture of 1,6-GPS (6-0-α-D-glucopyranosyl-D-sorbitol) and 1,1-GPM ( 1-0-α-D-glucopyranosyl-D-mannitol). 15. Способ по пп.1 - 14, отличающийся тем, что подслащивающие вещества, содержащиеся в смеси, представляют собой смесь 1,6-ГПС (6-0-α-Д-глюкопиранозил-Д-сорбита), 1,1-ГПМ (1-0-α-Д-глюкопиранозил-Д-маннита), 1,1-ГПС (1-0-α-Д-глюкопиранозил-Д-сорбита), маннита и сорбита. 15. The method according to claims 1 to 14, characterized in that the sweeteners contained in the mixture are a mixture of 1,6-GPS (6-0-α-D-glucopyranosyl-D-sorbitol), 1,1-GPM (1-0-α-D-glucopyranosyl-D-mannitol), 1,1-GPS (1-0-α-D-glucopyranosyl-D-sorbitol), mannitol and sorbitol. 16. Стекловидный расплав, полученный одним из способов по пп.1 - 15. 16. The glassy melt obtained by one of the methods according to claims 1 to 15. 17. Стекловидный расплав по п. 16 для получения таблеток или твердой карамели. 17. The glassy melt according to claim 16 for the production of tablets or hard candy. 18. Таблетка, содержащая стекловидный расплав, полученный одним из способов по пп.1 - 15. 18. A tablet containing a glassy melt obtained by one of the methods according to claims 1 to 15. 19. Твердая карамель, содержащая стекловидный расплав, полученный одним из способов по пп.1 - 15. 19. Hard caramel containing a glassy melt obtained by one of the methods according to claims 1 to 15.
RU99121335/13A 1997-03-07 1998-02-11 Glassy melt production method, glassy melt, pellet and hard boiled candy containing glassy melt RU2185072C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19709304A DE19709304C2 (en) 1997-03-07 1997-03-07 Process for the production of hard caramels and tablets
DE19709304.3 1997-03-07

Publications (2)

Publication Number Publication Date
RU99121335A true RU99121335A (en) 2001-09-20
RU2185072C2 RU2185072C2 (en) 2002-07-20

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RU99121335/13A RU2185072C2 (en) 1997-03-07 1998-02-11 Glassy melt production method, glassy melt, pellet and hard boiled candy containing glassy melt

Country Status (15)

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US (2) US6248386B1 (en)
EP (1) EP0966204B1 (en)
JP (1) JP4350169B2 (en)
AT (1) ATE239380T1 (en)
AU (1) AU722053B2 (en)
BR (1) BR9808828A (en)
CA (1) CA2282689C (en)
DE (2) DE19709304C2 (en)
DK (1) DK0966204T3 (en)
ES (1) ES2197467T3 (en)
IL (1) IL131540A (en)
NZ (1) NZ337584A (en)
PT (1) PT966204E (en)
RU (1) RU2185072C2 (en)
WO (1) WO1998039978A1 (en)

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