TH69241B - Crystallized maltitol powder with coarse particle size, its preparation process and its use, especially in chocolate. - Google Patents

Abstract

DC60 (18/05/52) The invention involved crystallized maltitol powders with a maltol content greater than 99.5% by weight, characterized by particle size distribution by volume. Measured by Laser Granulometers Containing less than 20% particles less than 200 μm in size, less than 6% particles less than 100 μm in size, less than 2% particles less than 40 μm in size and pouring values of less than or equal to 10. S, air density greater than 0.85 g / ml, a compact density greater than 0.97 g / ml, and the ability to Compressed at less than 17%, and with its use in the entire pharmaceutical and food sectors above Especially In chocolate recipes or tableware sweeteners

Claims (3)

Disclaimer (all) which will not appear on the advertisement page. : ------ 13/07/2018 ------ (OCR) Page 1 of 2 pages Disclaimer 1. Process for pretreatment of crystallized maltitol powder. Specifically, the process consists of: a) giving a zig-zag separator. It has a multi-stage cavity tilted at 120 degrees with a crystallized maltitol powder with particle size distribution by volume. For the mean, the median diameter was composed of between 180 and 230 μm: - More than 20% particles less than 200 μm in terms of size, - More than 7% Particles less than 100 μm in terms of size, - More than 2. % Particles less than 40 μm in terms of size, 6) Primary air flow rate control loudly to recover the crystallized maltitol fraction. Where particle size by volume distribution is: - less than 20%, desirable is less. 15%, desirable is less 10% and more desirable is less than 5% particles less than 200 μm in terms of size, - less than 6% particles less than 100 μm in terms of size, - less than 2% particles less than 40 Micrometers in terms of size, 2. The process in which claim 1 is unique is that the process consists of: a) giving to a Sig-Shag separator The slit consists of 7 steps tilted at 120 degrees, the width being assembled between 2 and 3 centimeters, the length of which is between 4 and 5 centimeters, and the thickness is 4 centimeters. Crystallized For mean The diameter arithmetic was composed of between 180 and 230 μm. Particle size distribution by volume: - More than 20% Particles less than 200 μm in terms of size, - More than 7% Particles less than 100 μm in terms of size, - More than 2. % Particles less than 40 μm in terms of size, at the composite flow rate between 400 and 600 g / min, 6) Determination of the primary air flow rate at the composite values between 2 and 5 cubic meters per H, c) recovery of powder fraction containing For an arithmetic mean, the diameter was composed between 200 and 350 μm, a particle size distribution by volume of less than 20%, desirable was less than 15%, particles less than 200 μm in terms of size -------. ----- ------ 13/11/2017 ------ (OCR) Page 1 of 2 pages Disclaimer 1. Process for preparation of crystallized maltitol powder. According to any claim One of the unique clauses 1 to 3 is: The process consists of: a) giving a zig-zag separator. With a multistage cavity tilted at 120 degrees with a crystallized maltitol powder with particle size distribution by volume.For arithmetic mean, the diameter was comprised between 180 and 230 μm at: - more than 20%. Particles less than 200 μm in terms of size, - More than 7% Particles less than 100 μm in terms of size, - More than 2% Particles less than 40 μm in terms of size, b) Air flow control Primary As to recover a fraction of crystallized maltitol powder with a particle size distribution by volume: - less than 20%, desirable was less than 15%, desirable was less than 10%. And more desirable is less than 5% particles less than 200 μm in terms of size, - less than 6% particles less than 100 μm in terms of size, - less than 2% particles less than 40 μm in size. In terms of size, 2. The process in which claim 1 is unique is that process consists of: a) giving to a zig-zag separator. It has a cavity composed of 7 steps tilted at 120 degrees, the composite width is between 2 and 3 centimeters, the length of which is assembled between 4 and 5 centimeters, and the thickness is 4 centimeters with the molten powder. Crystallized with For average The diameter arithmetic was composed of between 180 and 230 micrometers. Size distribution. Particles by volume: - More than 20% Particles less than 200 μm in terms of size, - More than 7% Particles less than 100 μm in terms of size, - More than 2% Particles less than 40 μm in terms of size, At the composite flow rate between 400 and 600 g / min, b) determination of the primary air flow rate at the composite values between 2 and 5 m3 / h, c) recovery of the powder fraction at have For an arithmetic mean, the diameter was composed between 200 and 350 μm, a particle size distribution by volume of less than 20%, desirable was less than 15%, particles less than 200 μm in terms of size -------. ----- Edit 24/03/2017 1. The process for the preparation of the crystallized maltitol powder according to which claim? One of the unique clauses 1 to 3 is: The process consists of: a) giving to a zig-zag separator. With a multistage cavity tilted at 120 degrees with a crystallized maltitol powder with particle size distribution by volume.For arithmetic mean, the diameter was comprised between 180 and 230 μm at: - more than 20%. Particles less than 200 μm in terms of size, - More than 7% Particles less than 100 μm in terms of size, - More than 2% Particles less than 40 μm in terms of size, b) Air flow control Primary As to recover a fraction of the crystallized maltitol powder with a particle size distribution by volume at: - less than 20%, desirable was less than 15%, desirable was less than 10%, and where Also more desirable is less than 5% particles less than 200 μm in terms of size, - less than 6% particles less than 100 μm in terms of size, - less than 2% particles less than 40 μm in terms of size, 2. The process according to claim 1 is unique in that it consists of: a) giving to a zig-zag separator. The slit consists of 7 steps tilted at 120 degrees, the width of which is between 2 and 3 centimeters, the length of which is between 4 and 5 centimeters, and the thickness is 4 centimeters with the molten powder. Crystallized For mean The diameter arithmetic was composed of between 180 and 230 micrometers. Size distribution. Particles by volume: - More than 20% Particles less than 200 μm in terms of size, - More than 7% Particles less than 100 μm in terms of size, - More than 2% Particles less than 40 μm in terms of size, At the composite flow rate between 400 and 600 g / min, b) determination of the primary air flow rate at the composite values between 2 and 5 m3 / h, c) recovery of the powder fraction at have For the arithmetic mean, the diameter was composed between 200 and 350 μm, the particle size distribution by volume of less than 20%, desirable was less than 15%, particles less than 200 μm in terms of size. 3. The unique procedure for claim 1 is that it consists of: a) giving to a zig-zag separator. The slit consists of 7 steps tilted at 120 degrees, the width of which is between 2 and 3 centimeters, the length of which is between 4 and 5 centimeters, and the thickness is 4 centimeters with the molten powder. Crystallized For mean The diameter arithmetic was composed of between 180 and 230 micrometers. Size distribution. Particles by volume: - More than 20% Particles less than 200 μm in terms of size, - More than 7% Particles less than 100 μm in terms of size, - More than 2% Particles less than 40 μm in terms of size, At the composite flow rate between 450 and 550 g / min, b) determination of the primary air flow rate at the composite values between 40 and 50 m3 / h, c) recovery of the powder fraction at have For the mean arithmetic, the diameter was composed between 450 and 600 μm. The particle size distribution by volume was less than 10%, desirable was less than 5%, for particles less than 200 μm in terms of size. --------------------