US471060A - Henry e - Google Patents
Henry e Download PDFInfo
- Publication number
- US471060A US471060A US471060DA US471060A US 471060 A US471060 A US 471060A US 471060D A US471060D A US 471060DA US 471060 A US471060 A US 471060A
- Authority
- US
- United States
- Prior art keywords
- pan
- liquor
- crystals
- sugar
- magma
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- CVHZOJJKTDOEJC-UHFFFAOYSA-N Saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 16
- 238000000034 method Methods 0.000 description 12
- 238000009835 boiling Methods 0.000 description 10
- 238000005469 granulation Methods 0.000 description 8
- 230000003179 granulation Effects 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 229940063680 RAW SUGAR Drugs 0.000 description 4
- 108060007338 SDHAF4 Proteins 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 235000020357 syrup Nutrition 0.000 description 4
- 238000001816 cooling Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000005712 crystallization Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000001737 promoting Effects 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
- C13K1/00—Glucose; Glucose-containing syrups
- C13K1/10—Crystallisation
Definitions
- This invention is applicable to the manufacture of raw sugar from cane-juice, and also to the treatment of raw-sugar solutions for the production of large-sized crystals therefrom.
- a vacuum pan is filled, say, half-full, of the thin liquor, and the liquor is then boiled down in the usual way to the granulating-point. Ordinarily it is held at that point for a greater or less period of time while granulation is taking place; but in dealing with a liquor of low grade, of a purity, say, of eighty or less, such granulation takes place very slowly, and, moreover, a considerable proportion of the crystals are so fine that when the resulting magma is subsequently drained in the centrifugal machine the fine crystals escape through the meshes of the sieve and so en-- rich the resulting sirup, but diminish the yield of the crystallized sugar.
- the objects of the present improvement are to lessen the time required for granulation and to obtain larger crystals, and hence a larger yield of crystallized sugar.
- the invention consists in introducing into the vacuum-pan, when the liquor therein has been boiled down to the gran ulating-point, a charge of sugar-magma of about the same purity as that of the liquor in the vacuum-pan. ⁇ Vhen the magma is rich in crystals, (containing fifty per cent. of crystals,) the charge will be equal to about ten per cent. of the volume of the concentrated liquor in the vacuum-pan. If the sugarmagma is less rich in crystals, a larger charge will be employed.
- the magma may be introduced all at once or from time to time, if desired.
- magma is herein used in the sensein which it is ordinarily used in sugar-refineries, as indicating a mixture of sugar-crystals and sirup. 'As in the ordinary process, the condition of concentration of the contents of the pan is kept under observation and additional thin liquor is introduced whenever the contents of the pan fall below the concentrating-point.
- What is claimed as the invention is The herein-described process of treating saccharine liquor for the purpose of producing large-sized sugar-crystals therein, which consists in boiling the saccharine liquor in a vacuum-pan down to the concentrating-point, and in then introducing into the pan a charge of sugar-magma equal to about ten per cent, more or less, of the quantity of concentrated liquor contained in the pan, and in maintaining the contents of the pan at the con'centratthe usual way preparatory to a repetition lug-point by introducing additional qnantiof the process with another lot of saccharine ties of saccharine liquor into the vacuum-pan liquor and another charge of sugar-magma.
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- General Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Medicines Containing Plant Substances (AREA)
- Saccharide Compounds (AREA)
Description
NlTED STATES ATENT OFFICE.
HENRY E. NIESE, OF JERSEY CITY, NEW JERSEY, ASSIGNOR TO THE AMERICAN SUGAR REFINING COMPANY, OF NElV YORK, N. Y.
METHOD OF TREATING CANE-JUICE AND OTHER SACCHARINE LIQUORS.
SBECIFICATION forming part of Letters Patent No. 471,060, dated March 15, 1892.
Application filed September 25, 1891- Serial No. 406,850. (No specimens.)
To 60% whom it may concern.-
Be it known that I, HENRY E. NIESE, of J ersey City, New Jersey, haveinvented a new and useful Method of Treating Cane-Juice and Saccharine Liquors for the Production of Large- Sized Crystals Therein, of which the following is a specification.
This invention is applicable to the manufacture of raw sugar from cane-juice, and also to the treatment of raw-sugar solutions for the production of large-sized crystals therefrom.
In carrying the process into effect a vacuum pan is filled, say, half-full, of the thin liquor, and the liquor is then boiled down in the usual way to the granulating-point. Ordinarily it is held at that point for a greater or less period of time while granulation is taking place; but in dealing with a liquor of low grade, of a purity, say, of eighty or less, such granulation takes place very slowly, and, moreover, a considerable proportion of the crystals are so fine that when the resulting magma is subsequently drained in the centrifugal machine the fine crystals escape through the meshes of the sieve and so en-- rich the resulting sirup, but diminish the yield of the crystallized sugar.
The objects of the present improvement are to lessen the time required for granulation and to obtain larger crystals, and hence a larger yield of crystallized sugar.
To these ends the invention consists in introducing into the vacuum-pan, when the liquor therein has been boiled down to the gran ulating-point, a charge of sugar-magma of about the same purity as that of the liquor in the vacuum-pan. \Vhen the magma is rich in crystals, (containing fifty per cent. of crystals,) the charge will be equal to about ten per cent. of the volume of the concentrated liquor in the vacuum-pan. If the sugarmagma is less rich in crystals, a larger charge will be employed. The magma may be introduced all at once or from time to time, if desired. The effect of the presence of sugarmagma is to greatly increase the rapidity of granulation from the original liquor and to increase the size of the crystals, because the concentrated saccharine liquor in a vacuumcrystallizable sugar present in the original liquor builds upon and enlarges the crystals of sugar contained in the magma. It will of course be understood that the term magma is herein used in the sensein which it is ordinarily used in sugar-refineries, as indicating a mixture of sugar-crystals and sirup. 'As in the ordinary process, the condition of concentration of the contents of the pan is kept under observation and additional thin liquor is introduced whenever the contents of the pan fall below the concentrating-point. The boiling process and the gradual addition of thin liquor as the boiling proceeds is continued usually until the pan is full. The contents of the pan are then dropped and carried to the usual cooling appliances, and are thereafter treated in the ordinary manner for the production of merchantable products therefrom. It is well known that the introduction of dry crystals into a solution of a crystallizable substance in a proper condition of concentration will have the efl'ect of promoting the crystallization of such substance, and hence the introduction of sugar-crystals into a suitablypan is not broadly claimed.
What is new in the present process is the introduction into the vacuum-pan containing the concentrated saccharine liquor of a sugarmagmathat is to say, a mixture of sugarcrystals and sirupfrom which two advantages result. First, there is no change in the test of the resulting contents of the pan, as there must be when dry crystals are introduced, and, secondly, owing to its semi-fluid quality the magma can be pumped into the vacuum-pan without losing any part of the Vacuum therein.
What is claimed as the invention is The herein-described process of treating saccharine liquor for the purpose of producing large-sized sugar-crystals therein, which consists in boiling the saccharine liquor in a vacuum-pan down to the concentrating-point, and in then introducing into the pan a charge of sugar-magma equal to about ten per cent, more or less, of the quantity of concentrated liquor contained in the pan, and in maintaining the contents of the pan at the con'centratthe usual way preparatory to a repetition lug-point by introducing additional qnantiof the process with another lot of saccharine ties of saccharine liquor into the vacuum-pan liquor and another charge of sugar-magma.
i from time to time, or additional charges of HENRY E. NIESE.
5 sugar-magma, if necessary, until the pan con- W'itnesses:
tains the desired quantity of material, and FGK. GEORG WINKLY,
in then dropping the contents of the pan in A. M. JONES.
Publications (1)
Publication Number | Publication Date |
---|---|
US471060A true US471060A (en) | 1892-03-15 |
Family
ID=2539920
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US471060D Expired - Lifetime US471060A (en) | Henry e |
Country Status (1)
Country | Link |
---|---|
US (1) | US471060A (en) |
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0
- US US471060D patent/US471060A/en not_active Expired - Lifetime
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