DE1065260B - Flow-through dissolving system for the production of saturated sugar solutions - Google Patents

Description

(Ξ)

FEDERAL REPUBLIC OF GERMANY

GERMAN MMm, PATENT OFFICE

kl 53I 12

INTERNAT. KL. A 23 g

EXPLAINING EDITORIAL 1065 260

C 1 3 f '\ (49 H 30391III / 531

REGISTRATION DAY. IS. JUNE 1957

NOTICE THE REGISTRATION AND ISSUE OF THE EDITORIAL: SEPTEMBER 10, 1959

The invention relates to flow-through sugar dissolving systems for the production of saturated sugar solutions according to patent 1 034 469, like this one for feeding used by flow-through sugar boilers. The dissolving systems have an intensely heated preheating cell, which in constant enema with granulated sugar and water in a regulated, proportionate way Quantities is supplied, with an overflow and a subsequent long flow channel as a solution path with lateral, turbulence-generating bottom heat. tongue as well as a basin with an overflow and arranged at the sewer outlet heated syrup feed head.

While the system protected in the main patent mentioned over a very large length of the solution route Value must be placed, including the longitudinal subdivision of the entire 360 ° reaching Canal bend was required to move the mixture back and forth over a total of 720 ° in front of his To achieve inflow into the final basin, you can according to the additional invention without Enlargement of the diameter of such a pulping system has the same pulping success with a stronger one Achieve flow rate if the flow channel to be traversed by the mixture is only an as only once around the basin in a circle or, if it is straight, only once let the mixture run through. The vertical cross-section of the canal is much larger as the partial cross-section of each of the two required by the main patent, one after the other from the Mixture traversed concentric channel sections. With this one measure, however, you can achieve the desired Not yet successfully resolved. Rather, there is also the subdivision of this single, flow channel traversed only in one direction through a number of transverse walls into individual ones Cells required. Each of these transverse walls must also have a lower side hole in the area the underfloor heating, so firstly a constant flow of the more and more going into solution Mixture of granulated sugar and water allows from cell to cell and secondly within each Cell a certain lingering of the largest part of the cell contents with strong, due to the lateral floor heating effected transverse circulation and an effective exchange of the mixture components between the bottom area of the cell and the liquid surface is reached. All of these measures taken together lead to the desired complete dissolution of all sugar crystals before the enema the now homogeneous solution into the collecting basin, in which the solution still contains the necessary syrup is fed through a feed head.

Flow-through dissolving system for production
saturated sugar solutions

Addendum to patent 1 034 469

Applicant:

Hansella-Werke Albert Henkel AG,
Viersen, Kölnische Str. 1-3

Hermann Thürlings, Viersen,
has been named as the inventor

An exemplary embodiment can be seen from the drawing, in the

Fig. 1 a vertical middle section through the pulping system,

Fig. 2 shows a horizontal cross section along line AB of Fig. 1 and

Fig. 3 shows a vertical section through the overflow point from the last cell of the solution path into the basin along line CD in Fig. 2.

The sugar 1 is fed to a preheater 4 in a known manner via a cellular wheel 2 and a sugar lock 3. The solution water runs through the pipe 5 into the sugar lock, is mixed with the sugar here and reaches the preheater 4 with it constant turbulence caused by the one-sided floor heating 9 reaches the basin 10 as a crystal-free solution. The steam-heated pipe 9 serves as the heating element. The flow channel 6 is divided into individual cells by transverse walls 6 '. The transverse walls 6 'have lower throughflow holes 6 ". The holes 6' are so large that it can pass continuously flow a sufficient amount of mixture in the neighboring cell at the heating tube. The finished sugar solution runs from the last cell through the unspecified overflow hole into the basin 10, where the syrup is then mixed in.

Claims (1)

Claim. Sugar flow-through dissolving plant for production saturated sugar solutions suitable for feeding through-flow sugar boilers with a iiiteu- siv heated, in constant inlet with granulated sugar and water in regulated, proportionate Quantities supplied preheating cell with overflow and a subsequent long flow channel as a loosening section with lateral, turbulence-generating floor heating and one at the sewer outlet arranged, provided with an overflow basin with associated heated syrup feed head according to patent 1 034 469, characterized by a single one - preferably in plan ίο circularly around the basin (10) -, only in one main flow or circumferential direction of the mixture traversed flow channel (6) through lower lateral, im Area of the floor heating (9) arranged through-flow holes (6 ") having transverse walls (6 ') in individual cells is divided. Considered publications:
French patent specification No. 1 099 742. 1 sheet of drawings > 909 627M1 9.59