US260340A - August weenicke - Google Patents
August weenicke Download PDFInfo
- Publication number
- US260340A US260340A US260340DA US260340A US 260340 A US260340 A US 260340A US 260340D A US260340D A US 260340DA US 260340 A US260340 A US 260340A
- Authority
- US
- United States
- Prior art keywords
- sugar
- acetic acid
- acid
- august
- molasses
- 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
- QTBSBXVTEAMEQO-UHFFFAOYSA-N acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 78
- CVHZOJJKTDOEJC-UHFFFAOYSA-N Saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 16
- 239000002253 acid Substances 0.000 description 16
- 235000013379 molasses Nutrition 0.000 description 16
- 229940063680 RAW SUGAR Drugs 0.000 description 12
- 235000020357 syrup Nutrition 0.000 description 12
- 108060007338 SDHAF4 Proteins 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000003756 stirring Methods 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 4
- 238000004821 distillation Methods 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000011780 sodium chloride Substances 0.000 description 4
- VSGNNIFQASZAOI-UHFFFAOYSA-L Calcium acetate Chemical compound [Ca+2].CC([O-])=O.CC([O-])=O VSGNNIFQASZAOI-UHFFFAOYSA-L 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 210000003608 Feces Anatomy 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-M bisulphate group Chemical group S([O-])(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-M 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 235000011092 calcium acetate Nutrition 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910052571 earthenware Inorganic materials 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 235000011167 hydrochloric acid Nutrition 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000010871 livestock manure Substances 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229940072033 potash Drugs 0.000 description 2
- 235000015320 potassium carbonate Nutrition 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 239000001117 sulphuric acid 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
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/02—Crystallisation; Crystallising apparatus
Definitions
- the method of obtaining crystal'lizable sugar which forms the subject-matter of the present invention is based on the property of acetic acid of being a solvent of all foreign matter contained in raw sugar, in saccharine juices, in sirup, and in molasses, while crystallizable sugar is absolutely insoluble therein.
- the sugar is washed on the machine with some pure acetic acid, whereupon it is dried in a closed iron cylinder provided with a stirring apparatus, and heated by steam to a tem-
- the vapors are conducted into a condensing-Worm.
- it may also be freed from the residue of motherlye by means of a solution of sugar.
- the liquid is concentrated as much as possible z'. 6., to from to Baum-by evaporation in vacuum.
- the concentrated acetic acid is added, of which in this case from seventy-five to ninety per cent. of the weight of the saccharine liquor is required, according as it is more or less concentrated.
- the mixing with the acid which requires but a few minutes of time, is again carried out in a closed vessel with stirring apparatus; also, the further treatment of the liquor and of the sugar separating or crystallizing out therefrom is substantially the same as hereinbefore described.
- the sugarobtained by this process is generally sufiiciently white. In the contrarycase it must be subjected to a further purification by dissolving, filtering, and reconcentrating it.
- the acetic acid to be employed must be of a high degree of concentration,especially when saccharine liquors, sirup, or molasses are to be treated. In this case it is preferable to use an acid containing from ninety-eight to one hundred per cent. of pure acid. For sirups and other saccharine liquors which are evaporated to a density of from 50 to 52 Baum, an acid of a strength of ninety per cent. would, how ever, be sufficient, and for raw mlgar an acid still somewhatless concentrated might be used.
- the latter In order to recover the acetic acid from the mother-l ye, the latter is distilled preferably in a still made of cast-iron and provided with a cover and a condensing-worm of earthenware.
- the acid thus obtained is subsequently to be freed from the water which it has taken up from the sugar, molasses, &c. This may be done by means of bisulphate of soda or of chloride of in anhydrous state. If the latter salt is used, it is necessary to cause the muriatic acid evolved during the process of distillation to be absorbed by the medium of dry acetate of 5 soda, which is put into a vessel inserted between the head of the still and the condenser.
- the acid has to be converted by addition of lime into acetate of lime, which, after having been completely desiccated, is decomposed again by sulphuric acid for the purpose of liberating the acetic acid, which is then completely concentrated.
- the residue from the distillation of the acetic acid may be utilized as manure or for producing ammonia, methyl, potash, 85c.
- ⁇ Ve claim as our invention- The method of obtaining crystallizable or 20 crystallized sugar from raw sugar, saccharine juices, sirup, and molasses by adding concentrated acetic acid to the raw sugar or the saccharine liquor, allowing the sugar to separate or crystallize out, liberatiu g the sugar from the mother-lye by mechanical means, and finally 2 5 evaporating the residue of acetic acid or water or of acid and water, substantially as hereinbefore described.
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Saccharide Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
5o perature of about 106 to 110 centigrade. calcium, either of which has to be employed I00 7 UNITED STATES PATENT OFFICE.
AUGUST WERNIOKE, or HALLE-ON-THE-SAALE, AND WILHELM PFITZINGER OF STANCE, PRUSSIA, GERMANY.
METHOD OF EXTRACTING CRYSTALLIZABLE SUGAR FROM MOLASSES, dc.
SPECIFICATION forming part of Letters Patent No. 260,340, dated June 27, 1882,
Application filed May 23, 1882. (No specimens.)
To all whom it may concern:
Be it known that we, AUGUST WERNICKE, of Halle-on-the-Saale, Prussia, Germany, engineer, and WILHELM PFITZINGER, of Stanch, Prussia, Germany, temporarily residing at Prague, Austria, chemist, have invented an Improved Method of Obtaining Grystallizable Sugar from Raw Sugar, Saccharine Juices, Sirup, and Molasses, of which the following is a specification.
The method of obtaining crystal'lizable sugar which forms the subject-matter of the present invention is based on the property of acetic acid of being a solvent of all foreign matter contained in raw sugar, in saccharine juices, in sirup, and in molasses, while crystallizable sugar is absolutely insoluble therein.
In order to obtain crystallizable sugar from raw sugar, it is advantageous, first of all, to free the latter from the greater part of the water which it contains by a drying process carried out with application of heat. After having been cooled to below 70 centigrade the sugar is intimately mixed with from fifty to seventy per cent., or 'thereabout, of its weight of concentrated acetic acid, the mixing being carried out in a closed receptacle having by preference the form of a horizontal cylinder, and provided with a stirring apparatus. The mixture is thereupon drawn off and allowed to remain at rest and to cool in other vessels fitted with covers, and which may have a capacity of eight cubic feet. After a certain time-say from thirty-six to fortyeight hours--nearly all sugar has separated or crystallized out in pure state, while the motherlye consists in the acetic acid containing, in solution, all the foreign substances with but traces of sugarr The bulk of this liquid having been drained off from the sugar, the rest is extracted on a centrifugal drying-machine or in any other known manner. If it should be required, the sugar is comminuted before it is brought into the said machine. In order to complete its purification of adhering lye, the sugar is washed on the machine with some pure acetic acid, whereupon it is dried in a closed iron cylinder provided with a stirring apparatus, and heated by steam to a tem- For the purposeof recovering the acetic acid which is evaporated from the sugar, the vapors are conducted into a condensing-Worm. Instead of washing out the sugar on the centrifugal machine by means of acetic acid, it may also be freed from the residue of motherlye by means of a solution of sugar.
When the sugar contained in saccharine juices, molasses, or sirup is to be extracted the liquid is concentrated as much as possible z'. 6., to from to Baum-by evaporation in vacuum. After having been cooled to below centigrade the concentrated acetic acid is added, of which in this case from seventy-five to ninety per cent. of the weight of the saccharine liquor is required, according as it is more or less concentrated. The mixing with the acid, which requires but a few minutes of time, is again carried out in a closed vessel with stirring apparatus; also, the further treatment of the liquor and of the sugar separating or crystallizing out therefrom is substantially the same as hereinbefore described.
In case the raw sugar, the molasses, &c., are not mechanically mixed with impurities, the sugarobtained by this process is generally sufiiciently white. In the contrarycase it must be subjected to a further purification by dissolving, filtering, and reconcentrating it.
The acetic acid to be employed must be of a high degree of concentration,especially when saccharine liquors, sirup, or molasses are to be treated. In this case it is preferable to use an acid containing from ninety-eight to one hundred per cent. of pure acid. For sirups and other saccharine liquors which are evaporated to a density of from 50 to 52 Baum, an acid of a strength of ninety per cent. would, how ever, be sufficient, and for raw mlgar an acid still somewhatless concentrated might be used.
In order to recover the acetic acid from the mother-l ye, the latteris distilled preferably in a still made of cast-iron and provided with a cover and a condensing-worm of earthenware. The acid thus obtained is subsequently to be freed from the water which it has taken up from the sugar, molasses, &c. This may be done by means of bisulphate of soda or of chloride of in anhydrous state. If the latter salt is used, it is necessary to cause the muriatic acid evolved during the process of distillation to be absorbed by the medium of dry acetate of 5 soda, which is put into a vessel inserted between the head of the still and the condenser. If the degree of concentration attained by the aforesaid salts should not be sufficient, the acid has to be converted by addition of lime into acetate of lime, which, after having been completely desiccated, is decomposed again by sulphuric acid for the purpose of liberating the acetic acid, which is then completely concentrated.
1 5 The residue from the distillation of the acetic acid may be utilized as manure or for producing ammonia, methyl, potash, 85c.
\Ve claim as our invention- The method of obtaining crystallizable or 20 crystallized sugar from raw sugar, saccharine juices, sirup, and molasses by adding concentrated acetic acid to the raw sugar or the saccharine liquor, allowing the sugar to separate or crystallize out, liberatiu g the sugar from the mother-lye by mechanical means, and finally 2 5 evaporating the residue of acetic acid or water or of acid and water, substantially as hereinbefore described.
In testimony whereof we have signed our names to this specification in the presence of 30 two subscribing witnesses.
AUGUST WERNICKE. WILHELM PFITZINGER.
Witnesses for A. Wernicke:
CARL PIEPER, B. R01.
Witnesses for Pfitzinger: CARL RUPPERT, LEO SE RELTs.
Publications (1)
Publication Number | Publication Date |
---|---|
US260340A true US260340A (en) | 1882-06-27 |
Family
ID=2329619
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US260340D Expired - Lifetime US260340A (en) | August weenicke |
Country Status (1)
Country | Link |
---|---|
US (1) | US260340A (en) |
-
0
- US US260340D patent/US260340A/en not_active Expired - Lifetime
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