US434074A - Process of sugar-refining - Google Patents
Process of sugar-refining Download PDFInfo
- Publication number
- US434074A US434074A US434074DA US434074A US 434074 A US434074 A US 434074A US 434074D A US434074D A US 434074DA US 434074 A US434074 A US 434074A
- Authority
- US
- United States
- Prior art keywords
- lime
- glucose
- sugar
- solution
- compounds
- 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
- 238000000034 method Methods 0.000 title description 22
- 238000007670 refining Methods 0.000 title description 20
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 56
- 235000015450 Tilia cordata Nutrition 0.000 description 56
- 235000011941 Tilia x europaea Nutrition 0.000 description 56
- 239000004571 lime Substances 0.000 description 56
- WQZGKKKJIJFFOK-GASJEMHNSA-N D-Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 50
- 239000008103 glucose Substances 0.000 description 50
- 235000000346 sugar Nutrition 0.000 description 38
- 150000001875 compounds Chemical class 0.000 description 24
- IATRAKWUXMZMIY-UHFFFAOYSA-N Strontium oxide Chemical compound [O-2].[Sr+2] IATRAKWUXMZMIY-UHFFFAOYSA-N 0.000 description 16
- CVHZOJJKTDOEJC-UHFFFAOYSA-N Saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 12
- 238000000354 decomposition reaction Methods 0.000 description 12
- 235000020357 syrup Nutrition 0.000 description 12
- QVQLCTNNEUAWMS-UHFFFAOYSA-N Barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 10
- 229910001864 baryta Inorganic materials 0.000 description 10
- 238000009835 boiling Methods 0.000 description 10
- 238000000605 extraction Methods 0.000 description 10
- 235000013379 molasses Nutrition 0.000 description 10
- 239000000047 product Substances 0.000 description 10
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 8
- 239000012535 impurity Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- 239000002244 precipitate Substances 0.000 description 8
- 235000015192 vegetable juice Nutrition 0.000 description 8
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 6
- 238000001914 filtration Methods 0.000 description 6
- 150000002303 glucose derivatives Chemical class 0.000 description 6
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 6
- 230000000266 injurious Effects 0.000 description 6
- DSLZVSRJTYRBFB-LLEIAEIESA-L D-glucarate(2-) Chemical compound [O-]C(=O)[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O DSLZVSRJTYRBFB-LLEIAEIESA-L 0.000 description 4
- 108060007338 SDHAF4 Proteins 0.000 description 4
- RQPZNWPYLFFXCP-UHFFFAOYSA-L barium dihydroxide Chemical compound [OH-].[OH-].[Ba+2] RQPZNWPYLFFXCP-UHFFFAOYSA-L 0.000 description 4
- 239000003518 caustics Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 4
- 150000008163 sugars Chemical class 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N D-sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 235000007201 Saccharum officinarum Nutrition 0.000 description 2
- 240000000111 Saccharum officinarum Species 0.000 description 2
- 229960004793 Sucrose Drugs 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 235000012255 calcium oxide Nutrition 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000001376 precipitating Effects 0.000 description 2
- 230000000717 retained Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B35/00—Extraction of sucrose from molasses
- C13B35/02—Extraction of sucrose from molasses by chemical means
- C13B35/04—Extraction of sucrose from molasses by chemical means by precipitation as alkaline earth metal saccharates
Definitions
- the invention consists in boiling a solution of molasses, sirup, or vegetable juice of a density of, say, 10 to 15 Baum, for aperiod of two hours, more or less, after mixing with such solution a quantity of either caustic lime, caustic strontia, or caustic baryta equaling in weight, say, fifteen to thirty per cent. of the weight of the dry sugar plus the weight of the glucose present.
- the glucose will be decomposed, and the products of such decomposition, by combining with the lime, strontia, or baryta, as the case may be, will form, first, compounds which remain insoluble so long as the solution is alkaline, and which are immediately separated in a filterpress; secondly, compounds which are precipit-ated by treating the solution with carbonic acid in an ordinary blow-up, and are thus removed, and, finally, certain liquid compounds, the presence of which is not injurious, because they do not interfere with the subsequent extraction of the sugar.
- Vater may be used as the diluent for the molasses, sirup, or vegetable-juice to be treated in such proportion that the solution will not contain more than twenty per cent.
- washing-liquids resulting from various processes of sugar-refining may be used instead of wateras, for example, the thin washing-liquid from the filters, or the so-called washing-lye resulting from washing the saccharate of lime obtained by the process of sugar-refinin g described in Letters Patentof the United States No. 277,521, dated May 15, 1883.
- glucose is readily decomposed, and its products and also crystallizable sugar are capable of forming compounds with lime, strontia, or baryta.
- lime process of refining sugar-liquids of low grade described in Letters Patent of the United States No. 240,879, dated May 3, 1881, wherein it is sought to precipitate the impurities of the sugar by forming them into insoluble compounds with lime, care is taken to use only a small quantity of lime and to keep the temperature of the solution under treatment down to 120 Fahrenheit or under during thefirst step of the process, so that the glucose present will'not be affected, and the lime compounds will be formed only with the impurities of the sugar.
- lime, strontia, or baryta may be employed in the manner herein set forth; but lime is preferred because of its small cost, and also because it does not attack cyrstaltoo lizable sugar so strongly as caustic strontia or caustic baryta.
- the saccharine solution containing, say,twcnty per cent, or less, of sugar has been formed, and either before or after the addition to it of the lime, it is heated to the boiling-point.
- Either quicklime or hydrate of lime may be employed.
- the quantity of lime will depend upon the quantity of glucose present in the saccharine solution. It is desirable that the quantity of lime shall equal in Weight, say, fifteen to thirty per cent, of the Weight of the sugar plus the Weight of the glucose present, so that there will be more than sufficient lime to decompose all the glucose and form compounds with all the products of such decomposition.
- the solution After the introduction of the lime and the almost immediately following decomposition of the glucose the solution is kept boiling continuously until the products of such decomposition, by uniting with the lime, form the herein-mentioned compounds. It has usually been found desirable to continue the boiling for a period of about two hours; but of course this period can be varied Without departing from the invent-ion. At the conclusion of this treatment the solution will be found to yield, a precipitate consisting in part of the salts of lime resulting from the destruction of the glucose, in part of any impurities originally contained in the lime employed, and possibly in part of a portion of the lime present.
- the solution is then run through a filter-press, by which the resulting precipitate is removed, after which the clear solution is run into vats provided With the devices commonly known as blow-ups, and is saturated with carbonic acid until it is only slightly alkaline.
- the result of the carbonic-acid treatment is that substantially all the remaining impurities present are precipitated with the resulting carbonate of lime. Care must be taken not to supersaturate the solution and thereby cause any part of the precipitate to redissolve. To this end from two to ten one-hundredths of one per cent. of lime must be retained in the solution.
- ⁇ Vhat I claim as my invention is 1.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Saccharide Compounds (AREA)
Description
UNITED STATES ATENT OFFICE.
LOTHAR STERNBERG, OF NEW' YORK, N. Y., ASSIGNOR TO F. O. MATTHIESSEN & \VIECHERS SUGAR REFINING COMPANY, OF JERSEY CITY, NEW JERSEY.
PROCESS OF SUGAR-REFINING.
SPECIFICATION forming part of Letters Patent No. 434,074, dated August 12, 1890.
Application filer" December 21, 1889. Serial No. 334,568. (No specimens.)
To all whom it may concern.-
Be it known that I, LOTHAR STERNBERG, of the city and State of New York, have invented a new and useful Process of Sugar-Refining, of which the following is a specification.
This improvement is intended for employment in the art of refining molasses, sirups,
- and vegetable-j uices, particularly the sirups produced from sugar-cane, which contain glucose; and its object is to get rid of the glucose as a preliminary step to the extraction of the crystallizable sugar, because glucose, when present, prevents a certain proportion of sugar from crystallizing, and also renders the product impure.
The invention consists in boiling a solution of molasses, sirup, or vegetable juice of a density of, say, 10 to 15 Baum, for aperiod of two hours, more or less, after mixing with such solution a quantity of either caustic lime, caustic strontia, or caustic baryta equaling in weight, say, fifteen to thirty per cent. of the weight of the dry sugar plus the weight of the glucose present. By this means the glucose will be decomposed, and the products of such decomposition, by combining with the lime, strontia, or baryta, as the case may be, will form, first, compounds which remain insoluble so long as the solution is alkaline, and which are immediately separated in a filterpress; secondly, compounds which are precipit-ated by treating the solution with carbonic acid in an ordinary blow-up, and are thus removed, and, finally, certain liquid compounds, the presence of which is not injurious, because they do not interfere with the subsequent extraction of the sugar. Vater may be used as the diluent for the molasses, sirup, or vegetable-juice to be treated in such proportion that the solution will not contain more than twenty per cent. of sugar, or the washing-liquids resulting from various processes of sugar-refining may be used instead of wateras, for example, the thin washing-liquid from the filters, or the so-called washing-lye resulting from washing the saccharate of lime obtained by the process of sugar-refinin g described in Letters Patentof the United States No. 277,521, dated May 15, 1883.
As is well known, glucose is readily decomposed, and its products and also crystallizable sugar are capable of forming compounds with lime, strontia, or baryta. Thus in the socalled lime process of refining sugar-liquids of low grade, described in Letters Patent of the United States No. 240,879, dated May 3, 1881, wherein it is sought to precipitate the impurities of the sugar by forming them into insoluble compounds with lime, care is taken to use only a small quantity of lime and to keep the temperature of the solution under treatment down to 120 Fahrenheit or under during thefirst step of the process, so that the glucose present will'not be affected, and the lime compounds will be formed only with the impurities of the sugar.
In the class of processes of refining canesugar in which large percentages of lime, strontia, or baryta are added to the saccharine solution under conditions which lead to the formation of either mono or multi-basic' saccharates of lime, strontia, or baryta, as the case may be, not only is a certain proportion of otherwise crystallizable sugar prevented from crystallizing by the glucose which is originally present, but the saccharate thus produced is rendered impure by the inclusion with it of the compounds resulting from the decomposition of the glucose; hence the importance of the result secured by the present process in the removal of the glucose from the saccharine solution under treatment as the preliminary step to the subsequent extraction therefrom of the crystallizable sugar by any suitable method-as, for example, by either of the so-called lime or strontia processes.
In the present process, even if the glucose is thrown away, more than its equivalent in value is realized from the increased purity of the final product and from the increase in the yield of crystallized sugar due to the absence of the glucose, which has been removed by the preliminary treatment of the solution, as herein described. For this preliminary treatment either lime, strontia, or baryta may be employed in the manner herein set forth; but lime is preferred because of its small cost, and also because it does not attack cyrstaltoo lizable sugar so strongly as caustic strontia or caustic baryta.
In carrying out the present invention, after the saccharine solution containing, say,twcnty per cent, or less, of sugar has been formed, and either before or after the addition to it of the lime, it is heated to the boiling-point. Either quicklime or hydrate of lime may be employed. The quantity of lime will depend upon the quantity of glucose present in the saccharine solution. It is desirable that the quantity of lime shall equal in Weight, say, fifteen to thirty per cent, of the Weight of the sugar plus the Weight of the glucose present, so that there will be more than sufficient lime to decompose all the glucose and form compounds with all the products of such decomposition. After the introduction of the lime and the almost immediately following decomposition of the glucose the solution is kept boiling continuously until the products of such decomposition, by uniting with the lime, form the herein-mentioned compounds. It has usually been found desirable to continue the boiling for a period of about two hours; but of course this period can be varied Without departing from the invent-ion. At the conclusion of this treatment the solution will be found to yield, a precipitate consisting in part of the salts of lime resulting from the destruction of the glucose, in part of any impurities originally contained in the lime employed, and possibly in part of a portion of the lime present. The solution is then run through a filter-press, by which the resulting precipitate is removed, after which the clear solution is run into vats provided With the devices commonly known as blow-ups, and is saturated with carbonic acid until it is only slightly alkaline. The result of the carbonic-acid treatment is that substantially all the remaining impurities present are precipitated with the resulting carbonate of lime. Care must be taken not to supersaturate the solution and thereby cause any part of the precipitate to redissolve. To this end from two to ten one-hundredths of one per cent. of lime must be retained in the solution. If, however, the carbonization has been carried too far, an excess of lime must be added and the carbonic-acid treatmentrepeated until the solution again exhibits a merely slight alkaline reaction. The solution is again run through the filter-presses to complete its separation from the precipitate, and will be found upon examination to be free from glucose and from any of the injurious compounds resulting from the decomposition of the glucose, so that it may be advantageously subjected to further treatment for the extraction of its crystallizable sugar.
\Vhat I claim as my invention is 1. The improvement in the art of refining low-grade sugars, molasses, sirups, or vegetable juices containing glucose, herein described, which consists in boiling the saccharine solution under treatment, together With a suitable quantity of lime or its equivalent, until the glucose present is decomposed and insoluble glucose compounds are formed, and in then separating the said glucose compounds by filtration.
2. The improvement in the art of refining low-grade sugars, molasses, sirups, or vegetable-juices containing glucose, herein described, which consists, first, in boiling the saccharine solution under treatment together with a suitable quantity of lime, or its equivalent, and thereby decomposing the glucose present, and then separating the resulting insoluble glucose compounds by filtration, and, secondly, in treating the remaining solution With acid, and precipitating and removing by a second filtration the resulting lime compounds and the remainingimpurities present, preparatory to subjecting the solution thus freed from glucose and from injurious compounds resulting from the decomposing of the glucose to further treatment for the extraction of the crystallizable sugar therefrom.
LOTHAR STERNBERG.
Witnesses:
THos. WM. CLARKE, A. M. J ONES.
Publications (1)
Publication Number | Publication Date |
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US434074A true US434074A (en) | 1890-08-12 |
Family
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US434074D Expired - Lifetime US434074A (en) | Process of sugar-refining |
Country Status (1)
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US (1) | US434074A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050056647A1 (en) * | 2001-12-03 | 2005-03-17 | Hsi-Ming Cheng | Mesh container, system using mesh containers, and method for making mesh containers |
-
0
- US US434074D patent/US434074A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050056647A1 (en) * | 2001-12-03 | 2005-03-17 | Hsi-Ming Cheng | Mesh container, system using mesh containers, and method for making mesh containers |
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