序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
1 一种赤砂糖干燥装置 CN201510411922.6 2015-07-14 CN104975114A 2015-10-14 欧承晏
发明公开了一种赤砂糖干燥装置,包括设有进料口和出料口的箱体、设于所述箱体上的滚动装置和进装置,所述滚动装置垂直安装于所述箱体上,且所述滚动装置的一端伸入所述箱体内;所述箱体的壁上开有进气口和出气口,所述进风装置安装于所述进气口上;所述赤砂糖通过进料口与所述滚动装置相接触,所述进风装置产生气流通过进气口吹向赤砂糖,所述滚动装置旋转驱动赤砂糖向外抛散,形成抛物线冷却结构。本发明的赤砂糖向外抛出而散开,使得赤砂糖的散热面积和运动距离增加,从而极大地提升了冷却干燥的效果,具有结构简单、冷却干燥效果好和使用方便的有益效果。
2 Sweeteners and its manufacturing method JP7373389 1989-03-24 JP2842610B2 1999-01-06 BURITA KURISUTEINA GUTSUDOEIKAA; ANDORYUU GIRUBAATO PEMUBUROKU; DEIPATSUKU PURABURURARU SHUKURA
3 Sweetener and its production JP7373389 1989-03-24 JPH0223900A 1990-01-26 BURITA KURISUTEINA GUTSUDOEIKA; ANDORIYUU GIRUBAATO PEMUBUROUK; DEIPATSUKU PURABURURARU SHIYUK
PURPOSE: To obtain a new sweetener having low bulk density, not containing any additive, exhibiting sparkling appearance and containing pure sucrose as a base. CONSTITUTION: This sweetener comprises hollow spheroids or part spheroids of microcrystalline sucrose. The sweetener is obtained by drying sucrose syrup with simultaneous injection of an inert pressurized gas and bringing the sprayed syrup into contact with crystals of sucrose during the spray drying step and/or after completion of the step. COPYRIGHT: (C)1990,JPO
4 Method for producing high-purity crystalline fructose with fructose syrup containing a small amount of fructose made from sucrose and the product JP2003520866 2002-05-17 JP2004537326A 2004-12-16 ソアレ、セルジオ、ムリロ スタミル; メンドンサ フェレイラ、ジョアン、アルフォンソ ド; テイゼイラ、クラウディオ、オクタヴィオ マットス
平均直径250ミクロン乃至350ミクロンの狭いサイズ分布をもつ微結晶からなる粒子を有する、サトウキビスクロースから作られる結晶質フルクトース。 その製造工程は、酸加分解によるスクロースの化学的変換と、グルコースからのフルクトースのクロマトグラフ分離と、フルクトースを豊富に含むシロップの調製と、水性アルコール性メディアからのフルクトースの結晶化、遠心分離による回収と、洗浄と、結晶の乾燥とからなる。
5 Heating-pressing-expansion method or drying pure sugar or starch hydrolysate for preparing free-flowing powder JP23648583 1983-12-16 JPS59166100A 1984-09-19 ANDORE ERU I RAPAIRU; DANIERU ESU IYOTSUTO SUPUROITO
6 PROCESS AND SYSTEM FOR PROCESSING AQUEOUS SOLUTIONS US15738855 2016-06-23 US20180187275A1 2018-07-05 Peter M. Koenig; Charles Louis Ley; Michael Guy Morin; John Marvin Heapy; Andrei Bortnov
A system can be used to process liquid materials, such as aqueous-based syrup solutions containing sugar molecules. In some examples, the system includes a processing vessel having multiple individually-controllable temperature zones arranged in series. In operation, an aqueous solution can be introduced into an inlet port of the processing vessel and passed sequentially through the series of temperature zones. Water from the aqueous solution can be evaporated within the initial stage(s) of the processing vessel to form a concentrated solution that is then cooled in subsequent stage(s). Accordingly, a supersaturated solution may be formed from the aqueous solution in the processing vessel that is then solidified to subsequently form a substantially dry solid material (e.g., sugar), still within the processing vessel. The substantially dry solid material can discharge through an exit port of the processing vessel.
7 Apparatus for drying and cooling particulated material US41265064 1964-11-20 US3261109A 1966-07-19 HEINRICH TILLMANNS
8 Dry pulverulent sugar products and process for producing same US16512162 1962-01-09 US3140201A 1964-07-07 REIMERS FREDERICK E; MILLER MARVIN D; FREEMAN BUSH
9 Process for the production of crystalline fructose of high purity utilizing fructose syrup having a low content of fructose made from sucrose and product obtained US10486516 2002-05-17 US07150794B2 2006-12-19 João Afonso De Mendonca Ferreira; Cláudio Otávio Mattos Teixeira; Sérgio Murilo Stamile Soares
Crystalline fructose, from sugar cane sucrose, having particles composed of microcrystals which exhibit a narrow size distribution with a mean diameter of 250 to 350 microns. A process comprising chemical conversion of sucrose by acid hydrolysis; chromatographic separation of the fructose from the glucose; preparing fructose-rich syrup; crystallization of the fructose from an aqueous alcoholic medium, recovery by centrifugation; washing and; drying of the crystals.
10 Method for an equipment for making dry products from sugar syrup US706535 1985-02-27 US4651715A 1987-03-24 Udo Breithaupt; Herta Benecke
To convert syrups deriving from sugar production and other foodstuffs into a powder or granulated form subsequent to appropriate preliminary concentration and while preserving the product subject to the most extensive possible maintenance of the original composition, a sugar solution with at least 70% dry matter and up to 15% non-sucrose materials in the dry matter is brought by product-preserving rapid heating to a high temperature. Subsequently the vapors are allowed to escape to a dry-matter content of at least 90% and the thickened syrup is converted into a dry and pourable product just by cooling and sudden extraction of the residual water through crystallization. This preferably occurs in equipment comprising a steam-heated spiral-tube heat exchanger with a spiral tube that tapers out to 150 to 200% of its original free cross-section and has built-in twist generating baffles, a vapor precipitator to atmospheric pressure, and a crystallizer below the precipitator.
11 Method for drying crystallized sugar US3756855D 1971-05-28 US3756855A 1973-09-04 DUCHATEAU G; DEWULF P
METHOD FOR DRYING CRYSTALLIZED SUGAR IN THE PRESENCE OF A HEATED ENVIRONMENT, WHEREIN SAID ENVIRONMENT HAS A RELATIVE HUMIDITY LESS THAN, BUT CLOSE TO THE EQUILIBRUM RELATIVE HUMIDITY OF THE SUGAR TO BE DRIED, AT THE TEMPERATURE OF THE ENVIRONMENT. THIS METHOD PERMITS CRYSTLLIZED SUGAR TO BE OBTAINED IN BRIGHT CRYSTALS AND TO EXHIBIT PHYSICAL CHARACTERISTICS SIMILAR TO THOSE OF PRODUCTS PRO-

DUCED BY THE ADANT METHOD, SUCH AS HARDNESS, RESISTANCE TO ABRASION, POROSITY, RATE OF DISSOLUTION, AND DENSITY.
12 Production of soft sugar US3584617D 1969-03-14 US3584617A 1971-06-15 STACHENKO STEPHEN; ROBERTS ALAN J; MAGEE JOHN H
Soft sugar or brown sugar is produced by atomizing syrup under pressure onto a falling curtain of white sugar. The white sugar particles should present a sufficiently large surface area. The process is of general applicability and can be reproduced. The product is uniform. The composition of the syrup can be controlled.
13 Apparatus for drying and simultaneously cooling the white sugar coming from a centrifuge station US25281563 1963-01-21 US3229383A 1966-01-18 HEINRICH KAMP
14 Vibratory apparatus for treating granular material US11708661 1961-06-14 US3173768A 1965-03-16 WITTE JOHAN F
15 Process for preventing caking of sugar US85537459 1959-11-25 US3063158A 1962-11-13 MCFARLAND WILLIAM E; GAMBEL ADAM C
16 Brown sugar in powdered form US55053455 1955-12-02 US2910389A 1959-10-27 ALFRED LACHMANN
17 Verfahren und Vorrichtung zur Herstellung von Trockenprodukten aus Zuckersirup EP84112248.4 1984-10-11 EP0153447B1 1990-06-27 Breithaupt, Udo; Benecke, Herta
18 Vorrichtung zum Trocknen und Kühlen von feinkristallinem Zucker, insbesondere Fructose EP83110553.1 1983-10-22 EP0114939B1 1986-09-03 Laske, Gerd; Pöschel, Bruno
19 Naturbelassener Vollrohrzucker und Verfahren zu seiner Herstellung EP84112249.2 1984-10-11 EP0153448A2 1985-09-04 Langen, Arnold; Benecke, Herta; Breithaupt, Udo

Zur Herstellung eines naturbelassenen Vollrohrzuckers, der etwa die Farbe und den Geschmack von frisch gepreßtem Zuckerrohrsaft hat und noch wertvolle Aminosäuren und Vitamine enthält, wird aus reifem, entblättertem, sauberem Zuckerrohr mit hohem Saccharosegehalt der Zuckerrohrsaft nur bis zu 50 % des Rohrgewichts abgepreßt, der erhaltene Saft bei einer Temperatur über dem zweiten Flockpunkt der Wachse, Fette, Eiweißstoffe und Pentosane pasteurisiert, die Flockung abgetrennt, der gereinigte Saft unter der Pasteurisierungstemperatur schonend eingedickt und der erhaltene Sirup durch plötzlichen Entzug des restlichen Wassers in eine trockenes, rieselfähiges Produkt überführt.

20 PROCESS FOR THE PRODUCTION OF CRYSTALLINE FRUCTOSE OF HIGH PURITY UTILIZING FRUCTOSE SYRUP HAVING A LOW CONTENT OF FRUCTOSE MADE FROM SUCROSE AND PRODUCT OBTAINED EP02794717.5 2002-05-17 EP1417354A1 2004-05-12 DE MENDONCA FERREIRA, Joao Afonso; MATTOS TEIXEIRA, Cláudio Octávio; STAMILE SOARES, Sérgio Murilo
Crystalline fructose, from sugar cane sucrose, having particles composed of microcrystals which exhibit a narrow size distribution with a mean diameter of 250 to 350 microns. A process comprising: chemical conversion of sucrose by acid hydrolysis; chromatographic separation of the fructose from the glucose; preparing fructose-rich syrup; crystallization of the fructose from an aqueous alcoholic medium, recovery by centrifugation; washing and; drying of the crystals.
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