US1818618A - Method for the purification of carbohydrates obtained by hydrolysis of cellulose by means of hydrochloric acid - Google Patents
Method for the purification of carbohydrates obtained by hydrolysis of cellulose by means of hydrochloric acid Download PDFInfo
- Publication number
- US1818618A US1818618A US325122A US32512228A US1818618A US 1818618 A US1818618 A US 1818618A US 325122 A US325122 A US 325122A US 32512228 A US32512228 A US 32512228A US 1818618 A US1818618 A US 1818618A
- Authority
- US
- United States
- Prior art keywords
- carbohydrate
- hydrolysis
- cellulose
- purification
- hydrochloric acid
- 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
- 235000014633 carbohydrates Nutrition 0.000 title description 24
- 150000001720 carbohydrates Chemical class 0.000 title description 23
- 238000000034 method Methods 0.000 title description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 title description 8
- 230000007062 hydrolysis Effects 0.000 title description 8
- 238000006460 hydrolysis reaction Methods 0.000 title description 8
- 229920002678 cellulose Polymers 0.000 title description 4
- 239000001913 cellulose Substances 0.000 title description 4
- 238000000746 purification Methods 0.000 title description 4
- DSLZVSRJTYRBFB-LLEIAEIESA-N D-glucaric acid Chemical compound OC(=O)[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=O DSLZVSRJTYRBFB-LLEIAEIESA-N 0.000 description 10
- 238000000227 grinding Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 238000001704 evaporation Methods 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 238000005119 centrifugation Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 4
- 150000001342 alkaline earth metals Chemical class 0.000 description 4
- 150000001805 chlorine compounds Chemical class 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 235000011116 calcium hydroxide Nutrition 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 239000011343 solid material Substances 0.000 description 3
- 235000009508 confectionery Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 229960004903 invert sugar Drugs 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052573 porcelain Inorganic materials 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 125000000837 carbohydrate group Chemical group 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 238000001238 wet grinding Methods 0.000 description 1
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
- C13K1/02—Glucose; Glucose-containing syrups obtained by saccharification of cellulosic materials
Definitions
- This special method according to the invention consists in that the carbohydrate or sugar suitably after a preliminary partial removal of acid by evaporation is subjected to wet grinding together with an added oxide or hydroxide of an alkaline earth-metal preferably slaked lime.
- The, grinding is advantageously effected in a so-called ball-mill, the grinding bodies of which consist of porcelain.
- the effect of the grinding process consists in that the'carbohydrate is very completely converted into saccharate and that the acidresidue remaining, as above mentioned, in the carbohydrate even after evaporation is bound to the alkaline earth metal.
- the ground material is thereafter subjected'to a draining operation, preferably by subjecting it to centrifugation in a centrifuge having a bowl with pervious wall. If so treated, together with the liquid, also a considerable part of the chlorides dissolved therein are removed. Inorder to remove also the last traces of chlorides it is advisable to subject the material, which has been freed from liquid by centrifugation, to a washing process which may be effected in.
- the liquid which is separated off by the centrifugation process contains besides chlorides and other soluble substances also sugar material which does not form insoluble saccharates.
- the product which. is obtained after saturation is a pure tasteless carbohydrate, that is a carbohydrate which is neither sweet nor has any other characteristic taste. It is possible to convert it into a sweet sugar by a so-called inversion process, for instance by heating it in the presence ofsulfuric acid.
- the ground product consists of a thin impalpable pulp which is introduced ,into a centrifuge with pervious wall and subjected to centrifugation so as to remove the water contained therein.
- the 'solid constituents of the pulp form] a dense layer adhering to the wall of the bowl.
- the saccharate is retransformed into a pulp, this being advantageously done by re eated grinding with addition of water.
- guch saccharate pulp is introduced into pressure proof receptacles and subjected to saturation by treating it with carbonic acid at elevated pressure, for instance at a pressure of two atmospheres.
- the carbohydrate is separated from the saturation sludge and in usual manner converted into invert sugar by heating with 2% sulfuric acid.
- the invert sugar solution is freed from sulfuric acid asusual by addition of chalk and se aration e solution is treated with active carbon and thereafter concentrated by evaporation.
- the yield in pure sugar is about 65% by weight of the raw carbohydrate material or, if the raw carbohydrate had been obtained by hydrolysis of saw dust, about 45% by weight of the hydrolyzed wood..
- oxide of an alkaline earth-metal is intended to cover not only the oxide but also the hydroxide.
- What I claim is A method of treating carbohydrates which have been obtained by hydrolysis of cellulose with the aid of hydrochlorlc acid which comprises subjecting the carbohydrates in solution in admixture with an oxide of an alkaline earth metal to grinding, removing chloride containing liquid from the solid material, washing the separated solid material with fresh water, subjectin the washed solid material to reaction wit carbonic acid under elevated pressure so as to decompose the saccharate and to liberate the carbohydrates, separating the sludge from the carbohydrate solution, and inverting the carbohydrate contained in the separated solution.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- General Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Saccharide Compounds (AREA)
Description
Patented Aug. 11,- 1931 UNITED STATES PATENT OFFICE ERIK HAGGLUND, OF ABO, FINLAND, ASSIGNOR TO THE FIRM HOLZHYDROLYSE AKTIENGESELLSCHAFT, OF HEIDELBERG, GERMANY METHOD FOR THE PURIFICATION OF CARBOHYDRATES OE B'IAINED BY HYDROLYSIS OF CELLULOSE BY MEANS OF HYDROGHLOBIG ACID 7 No Drawing. Application filed December 10, 1928, Serial No. 825,129., and in Germany December 14, 1927.
It is known that by hydrolysis of cellulose containing material such as wood, preferably in the form of saw dust, by means of hydrochloric acid a carbohydrate product can be obtained. However this carbohydrate product or sugar is, even after having been subjected to an evaporation process with a view to removing the hydrochloric acid therefrom, not very well adapted for 10 use as food material owing to certain residues of acid in it which cannot be removed by evaporation, and which deteriorate the taste of the product and its salubrity. Attempts have already been made to overcome this difiiculty by subjecting the product of the hydrolysis to a purifying process consisting in transforming the carbohydrate into saccharate and subjecting the saccharate to a washing process and thereafter recoveringthe sugar by decomposition of the saccharateby carbonation. However the effect of this purification is not entirely satisfactory. Moreover a considerable loss in saccharate is caused by the washing process. Now this invention has for its object to avoid thedeficiency of the above mentioned known purification process by the application of a special method for the transformation of the carbohydrate into saccharate.
' This special method according to the invention consists in that the carbohydrate or sugar suitably after a preliminary partial removal of acid by evaporation is subjected to wet grinding together with an added oxide or hydroxide of an alkaline earth-metal preferably slaked lime. The, grinding is advantageously effected in a so-called ball-mill, the grinding bodies of which consist of porcelain.
The effect of the grinding process consists in that the'carbohydrate is very completely converted into saccharate and that the acidresidue remaining, as above mentioned, in the carbohydrate even after evaporation is bound to the alkaline earth metal. The ground material is thereafter subjected'to a draining operation, preferably by subjecting it to centrifugation in a centrifuge having a bowl with pervious wall. If so treated, together with the liquid, also a considerable part of the chlorides dissolved therein are removed. Inorder to remove also the last traces of chlorides it is advisable to subject the material, which has been freed from liquid by centrifugation, to a washing process which may be effected in.
the same centrifuge. This washing process requires only small quantities of water and does not cause a remarkable loss in saccharate. 1
In this way a saccharate is obtained which 7 is free from chlorides and which in known manner by saturation, that is treatment with carbonic acid, preferably under pressure can be converted into pure carbohydrate.
The liquid which is separated off by the centrifugation process contains besides chlorides and other soluble substances also sugar material which does not form insoluble saccharates. I
The product which. is obtained after saturation is a pure tasteless carbohydrate, that is a carbohydrate which is neither sweet nor has any other characteristic taste. It is possible to convert it into a sweet sugar by a so-called inversion process, for instance by heating it in the presence ofsulfuric acid.
Example 100 parts by weight of a carbohydrate or sugar material, obtained by hydrolyz'ing saw dust with hydrochloric acid and concentration of the product of hydrolysis by evaporation, are dissolved by 400 parts by weight of water and the solution introduced into a ball-mill with porcelain balls. 100 parts by weight of fresh slaked lime are added and stirred into the solution. The mixture is subjected to a grinding operation for a period of 1 hours. The ground product consists of a thin impalpable pulp which is introduced ,into a centrifuge with pervious wall and subjected to centrifugation so as to remove the water contained therein. The 'solid constituents of the pulp form] a dense layer adhering to the wall of the bowl. As soon as the water of thepulp has been removed ice-water is added, and
from the precipitated gypsum.
centrifu ation continued till no chlorine can be foun in the washing water. The saccharate is retransformed into a pulp, this being advantageously done by re eated grinding with addition of water. guch saccharate pulp is introduced into pressure proof receptacles and subjected to saturation by treating it with carbonic acid at elevated pressure, for instance at a pressure of two atmospheres. The carbohydrate is separated from the saturation sludge and in usual manner converted into invert sugar by heating with 2% sulfuric acid. The invert sugar solution is freed from sulfuric acid asusual by addition of chalk and se aration e solution is treated with active carbon and thereafter concentrated by evaporation. The yield in pure sugar is about 65% by weight of the raw carbohydrate material or, if the raw carbohydrate had been obtained by hydrolysis of saw dust, about 45% by weight of the hydrolyzed wood..
Considering the fact that about by weight of the wood can .be recovered as carbohydrate by hydrolysis a portion of raw carbohydrate equal to about 25% by weight of the wood remains in the solution separated oif by centrifugation from the product of grinding the mixture of raw carbohydrate and slaked lime. If desired, this solution can be subjected to fermentation or be used in the manufacture of yeast.
The essentially novel steps of my. above described method are recited in the annexed claims in connection with which it is to be understood that the term oxide of an alkaline earth-metal is intended to cover not only the oxide but also the hydroxide.
What I claim is A method of treating carbohydrates which have been obtained by hydrolysis of cellulose with the aid of hydrochlorlc acid which comprises subjecting the carbohydrates in solution in admixture with an oxide of an alkaline earth metal to grinding, removing chloride containing liquid from the solid material, washing the separated solid material with fresh water, subjectin the washed solid material to reaction wit carbonic acid under elevated pressure so as to decompose the saccharate and to liberate the carbohydrates, separating the sludge from the carbohydrate solution, and inverting the carbohydrate contained in the separated solution.
In testimony whereof I afiix my signature.
ERIK HKGGLUND.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1818618X | 1927-12-14 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1818618A true US1818618A (en) | 1931-08-11 |
Family
ID=7744621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US325122A Expired - Lifetime US1818618A (en) | 1927-12-14 | 1928-12-10 | Method for the purification of carbohydrates obtained by hydrolysis of cellulose by means of hydrochloric acid |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1818618A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040217063A1 (en) * | 2003-05-01 | 2004-11-04 | Yiheng Zhang | Cellodextrin production by mixed acid hydrolysis and chromographic separation |
| WO2012018740A1 (en) * | 2010-08-01 | 2012-02-09 | Hcl Cleantech Ltd | Methods and systems for solvent purification |
| US9663836B2 (en) | 2010-09-02 | 2017-05-30 | Virdia, Inc. | Methods and systems for processing sugar mixtures and resultant compositions |
-
1928
- 1928-12-10 US US325122A patent/US1818618A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20040217063A1 (en) * | 2003-05-01 | 2004-11-04 | Yiheng Zhang | Cellodextrin production by mixed acid hydrolysis and chromographic separation |
| WO2012018740A1 (en) * | 2010-08-01 | 2012-02-09 | Hcl Cleantech Ltd | Methods and systems for solvent purification |
| US9115467B2 (en) | 2010-08-01 | 2015-08-25 | Virdia, Inc. | Methods and systems for solvent purification |
| US9714482B2 (en) | 2010-08-01 | 2017-07-25 | Virdia, Inc. | Methods and systems for solvent purification |
| US11242650B2 (en) | 2010-08-01 | 2022-02-08 | Virdia, Llc | Methods and systems for solvent purification |
| US9663836B2 (en) | 2010-09-02 | 2017-05-30 | Virdia, Inc. | Methods and systems for processing sugar mixtures and resultant compositions |
| US10240217B2 (en) | 2010-09-02 | 2019-03-26 | Virdia, Inc. | Methods and systems for processing sugar mixtures and resultant compositions |
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