SU135835A1 - Continuous decomposition method of glucose double compound with sodium chloride - Google Patents
Continuous decomposition method of glucose double compound with sodium chlorideInfo
- Publication number
- SU135835A1 SU135835A1 SU647752A SU647752A SU135835A1 SU 135835 A1 SU135835 A1 SU 135835A1 SU 647752 A SU647752 A SU 647752A SU 647752 A SU647752 A SU 647752A SU 135835 A1 SU135835 A1 SU 135835A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- glucose
- double compound
- sodium chloride
- decomposition method
- continuous decomposition
- Prior art date
Links
Description
Известен непрерывный способ разложени двойного соединени глюкозы с хлористым натрием при температуре ниже 28,5°.A continuous process is known for the decomposition of a glucose double compound with sodium chloride at a temperature below 28.5 °.
Предлагаемый способ в отличие от известного повышает выход глюкозы. Это достигаетс тем, что процесс растворе1П1 двойного соединени глюкозы ведут при энергичном кратковременном перемешивании с водой в течение 20-40 сек, а выделение н рост кристаллов гидратной глюкозы ведут в течение 20-40 мин. без применени перемешивани , непрерывно отдел полученный утфе.ть от кристаллической глюкозы.The proposed method in contrast to the known increases the yield of glucose. This is achieved by the fact that the process of solution of 1P1 double glucose compound is carried out with vigorous short-term stirring with water for 20-40 seconds, and the release and growth of hydrate glucose crystals are carried out for 20-40 minutes. without stirring, continuously separating the resulting content from crystalline glucose.
Услови разложени кристаллов двойного соединени оказывают си.чьное вли ние на форму выдел юш,ихс кристаллов гидратной глюкозы . Дл получени нежелательных призматических, идеальных криста.ч.тов гидратной глюкозы необходимо после осун.ествлени пропесса растворени кристаллов двойного соединени избегать излишнего перемешивани массы в процессе выде.тени и роста кристаллов глюкозы. С уменьшением размеров кристаллов двойного соединени увеличиваетс скорость процесса их разложени .The conditions of decomposition of double compound crystals have a significant effect on the shape of the separated, their hydrated glucose crystals. In order to obtain undesirable prismatic, ideal crista parts of hydrated glucose, it is necessary, after drying the dissolution of the double compound crystals, to avoid excessive mass mixing during the extraction process and the growth of glucose crystals. With a decrease in the size of the double compound crystals, the rate of their decomposition increases.
При полном растворении всех кристаллов двойного соединени , поступивших на разложение, наличие хлористого патри п полученных криста.тлах глюкозы обусловливаетс только степенью отделени их мсжкриста.чьного раствора в прсщессе центрифуп ювани .With the complete dissolution of all the crystals of the double compound, which are received for decomposition, the presence of patrimonium chloride of the resulting crista glucose is only determined by the degree of separation of their crystalline solution in the juvani centrifuge.
Пред м е т и з о б р е т е и и PREPARATION AND RESULTS
Пепрерывный сиособ раз.южени двойного соединени г.тюкозы с хлористым натрием при температуре ниже 28,5, о т л и ч а ю HI и йс те.м, что, с целью повышени выхода глюкозы, процесс растворени двойного соедипени ведут при энергичном кратковременном пере .мешивании его с водой в течение 20-40 сек, а выделение и рост кристаллов гидратной глюкозы ведут в течение 20-40 мин. без применени перемешивани , с последуюнщм непрерывным отделением криетал.юв глюкозы от межкристального раствораThe continuous sioosos of breaking up the double compound of the city of tukoza with sodium chloride at a temperature below 28.5, is not limited to that, in order to increase the yield of glucose, the process of dissolving the double compound is carried out with energetic short-term mixing it with water for 20-40 seconds, and the release and growth of hydrated glucose crystals lead for 20-40 minutes. without the use of mixing, followed by continuous separation of the criset. glucose from the inter-crystal solution
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU647752A SU135835A1 (en) | 1959-12-18 | 1959-12-18 | Continuous decomposition method of glucose double compound with sodium chloride |
| SU647752K SU135836A1 (en) | 1959-12-18 | 1959-12-18 | Plant for producing crystalline glucose |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU647752A SU135835A1 (en) | 1959-12-18 | 1959-12-18 | Continuous decomposition method of glucose double compound with sodium chloride |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU135835A1 true SU135835A1 (en) | 1960-11-30 |
Family
ID=48292132
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU647752A SU135835A1 (en) | 1959-12-18 | 1959-12-18 | Continuous decomposition method of glucose double compound with sodium chloride |
| SU647752K SU135836A1 (en) | 1959-12-18 | 1959-12-18 | Plant for producing crystalline glucose |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU647752K SU135836A1 (en) | 1959-12-18 | 1959-12-18 | Plant for producing crystalline glucose |
Country Status (1)
| Country | Link |
|---|---|
| SU (2) | SU135835A1 (en) |
-
1959
- 1959-12-18 SU SU647752A patent/SU135835A1/en active
- 1959-12-18 SU SU647752K patent/SU135836A1/en active
Also Published As
| Publication number | Publication date |
|---|---|
| SU135836A1 (en) | 1960-11-30 |
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