US1599462A - Manufacture of sugar - Google Patents
Manufacture of sugar Download PDFInfo
- Publication number
- US1599462A US1599462A US37329A US3732925A US1599462A US 1599462 A US1599462 A US 1599462A US 37329 A US37329 A US 37329A US 3732925 A US3732925 A US 3732925A US 1599462 A US1599462 A US 1599462A
- Authority
- US
- United States
- Prior art keywords
- sugar
- acid
- wood
- solution
- manufacture
- 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
- 235000000346 sugar Nutrition 0.000 title description 25
- 238000004519 manufacturing process Methods 0.000 title description 3
- 239000002253 acid Substances 0.000 description 14
- SRBFZHDQGSBBOR-LECHCGJUSA-N alpha-D-xylose Chemical compound O[C@@H]1CO[C@H](O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-LECHCGJUSA-N 0.000 description 8
- 229960003487 xylose Drugs 0.000 description 8
- 230000007062 hydrolysis Effects 0.000 description 7
- 238000006460 hydrolysis reaction Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 6
- 239000004571 lime Substances 0.000 description 5
- 239000006188 syrup Substances 0.000 description 5
- 235000020357 syrup Nutrition 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 229960000443 hydrochloric acid Drugs 0.000 description 3
- 235000011167 hydrochloric acid Nutrition 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 235000021310 complex sugar Nutrition 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 150000004676 glycans Chemical class 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229920001282 polysaccharide Polymers 0.000 description 2
- 239000005017 polysaccharide Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 206010013457 Dissociation Diseases 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N 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 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 235000021551 crystal sugar Nutrition 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 208000018459 dissociative disease Diseases 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229960004793 sucrose Drugs 0.000 description 1
- 238000007738 vacuum evaporation 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
- sugar from cellulose-containing material by means of concentrated hydrochloric acid, which for the sake of briefness will hereinafter be referred to as wood-sugar,
- This sugar is a kind that has not yet been defined exactly, but amongst other things I proves to be a complex sugar by reason of the fact that hydrolysis is necessary to convert it into a ferment-able sugar.
- the preferably 2030% sugar solution after neutralizatiom' which is preferably effected by means of calcium car- 1 bonate, is stirred up, at a temperature below 20 C., with finely powdered or, finely dispersed calcium oxide. After ashort time there separates a copious precipitateof sugar-lime compound.
- the moist compound is decomposed by acids, such as carbonic acid or sulphurous acidj In this manner there are obtained very pure solutions of polysaccharides without any considerable losses. If theoperation MANUFACTURE OF SUGAR.
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Patented Sept. 14, 1926.
UNITED STATES I 1,599,462. PATENT OFFICE.
EDUARD EKRBER, or ninrnnnnnae; G RMANY, assreNon'ro THE INTERNATIONAL seem AND ALCOHOL COMPANY LIMITED, A BRITISH COMPANY, LONDON, ENG- LAND.
No Drawing. Application filed June 15, 1925,
As is well known it is possible to produce sugar from cellulose-containing material by means of concentrated hydrochloric acid, which for the sake of briefness will hereinafter be referred to as wood-sugar, This sugar is a kind that has not yet been defined exactly, but amongst other things I proves to be a complex sugar by reason of the fact that hydrolysis is necessary to convert it into a ferment-able sugar.
Hitherto ity-has not been possible in a satisfactory manner to purify this complex sugar, i. e. to'free it from acid and other detrimental accompanying substances. Experiments by electrolysis, dialysis, and other methods have not led to a technical result. It was also not to beexpected that it would be possible for this purpose to use alkaline earths, similar to the methods known for cane sugar. Wood sugar being, as stated, a kind of sugar that hitherto has. not been examined chemically, it was not even to be presumed whether it would in fact pass into an insoluble compound with alkaline earth oxides. By reason of the sensitiveness of this sugar towards alkalies it was further tobe feared that considerable losses would be incurred by the alkali action. I
In a surprising manner it has,fhoweyer, been found that with alkaline earths it is possible to obtain a precipitation and puri-- fication of the wood-sugar by keeping within determined conditions. For this purposeit is necessary to introduce finely divided calcium oxide into the strong sugar' solution in the cold. The separated sugar-lime compound is filtered ofli and. suspended in water, is decomposed by acids 'whichform' insoluble lime salts.
For examplethe preferably 2030% sugar solution after neutralizatiom'which is preferably effected by means of calcium car- 1 bonate, is stirred up, at a temperature below 20 C., with finely powdered or, finely dispersed calcium oxide. After ashort time there separates a copious precipitateof sugar-lime compound. I After pressing and washingwith as small quantities of water as possible the moist compound is decomposed by acids, such as carbonic acid or sulphurous acidj In this manner there are obtained very pure solutions of polysaccharides without any considerable losses. If theoperation MANUFACTURE OF SUGAR.
Serial No. 37,329, and in Germany June 26, 1924.
kinds ofsugan- According to the present.
invention this is effectedby introducing water into the molecule 'of the compound, that 1s to'say it is hydrolyzed, Mineral acid is used as catalyst. The hydrolysis must be elfected u'nder-very-special conditions. The sugar is so sensitive to the action of acid at high temperatures that it is only possible to conductthe hydrolysis satisfactorily within very narrow limits of sugar and acid concentration, time and temperature. Even with very slight variations of the conditions considered as being favorable, the sugar is easily damaged or destroyed on the one hand other hand.
It is not absolutely necessary for the lime precipitation described to precede the hyd rolysis as by hydrolysis itself apartial preliminary purification takes place at the same time by subsiduary' reaction, .The. hydrolysis takes place atvarious temperatures either at ordinary or increased pressure. The selection of the kind or conditions of heating depends essentially on the nature of the origin alsubstance.
If a syrup is under consideration, which has still a relatively high content of acid, the procedure for example is as follows The syrup .is dissolved in water in such a'mannor that the concentration of syrup amounts to'about 20% and hydrochloricacid about 3%, then it is allowed to boil under ordinary pressure for about 2-2 hours.
and is not completely hydrolyzed on the 4 If however a great bulk of material, freed from acid. is available or if a neutral sugar solution has been obtained by previous treatment with lime, then hydrolysis is effected ample under ordinary pressure then not more than 25% sugar and 3% hydrochloric acid must be present in the solution as otherwise damage or destruction of the sugar and simultaneously reversions take place. *The duration of boiling depends on'the content of sugar and acid of the solutions. The concentration of sugar is chosen as high as possible in view of the further treatment of the solution which is necessary later on.
When operating under pressure according to the second example, the concentration may be at 40% and even higher, the acid content being below 1%, preferably 0.3%, in order to enable the operation to be carried out in large metal vessels. Also in this case the duration and'degree of heating-depend on the content of the solutions. About 130 C. may be regarded as the upper temperature limit.
By such hydrolytic dissociations the wood-sugar not only becomes directly fermentable but also cry'Stallizable'. Inorder to obtain crystal sugar from the hydrolyzed solutions, it is necessary first to reduce the acidity to the point of neutral reaction and their to rapidly evaporate up to a degree of concentration suitable for crystallization. If there still existed an acid reaction the evaporation. could not be effected without loss and reconversion of the sugar, and even in the case of a neutral reaction it is advantageous to efi'ect the evaporation as quickly as possible.
-A fermentable wood-sugar solution prepared in accordance with one of the two ydrolyzing processes is neutralized, for example, by carbonate of sodium. In a vacuum evaporation or even in a roll drier, such, for example as used for drying potatoes, wherein the material to be only a part of a revolution, a syrup is produced therefrom, from which the se arated chloride of sodium-is removed while 01:. If then'the' syrup has a concentration of 7 0-80 A dried is run over a hot rotating roll on which it remains for per cent by weight of sugar, it is allowed tocool and crystallize out.
It is surprising that from the solutions obtained from a number of kinds of sugar it is possible to obtain in this manner sugar in the form of crystals.
What I claim and desire to secure by Letters Patent of the United States is 1. A method for the production of pure, fermentable', and .crystallizable sugar from wood sugar, comprising, introducing a finely subdivided alkaline earth oxide into a strong, raw, wood sugar solution, separating out the resulting sugar-alkaline earthcompounds, then liberating the polysaccharides from the separated sugar-alkaline earth compounds by means of acid, which form insoluble alkaline-earth metal and ing about 40% of sugar, and an acid content up to about 1%, to about 130 C.
4. A method according to claim 1, wherein the preliminarily purified wood sugar solution is hydrolyzed by heating a solution containing 40% of sugar and an acid content of 0.3%, up to 130 C.
5. A method according to "claim 1,,w'here in the purified and hydrolyzed sugar solution is exactl neutralized, and is then evaporated rapid y to a degree of concentration suitable for crystallization.
EDUARD FARBER.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1599462X | 1924-06-26 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1599462A true US1599462A (en) | 1926-09-14 |
Family
ID=7736840
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US37329A Expired - Lifetime US1599462A (en) | 1924-06-26 | 1925-06-15 | Manufacture of sugar |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1599462A (en) |
-
1925
- 1925-06-15 US US37329A patent/US1599462A/en not_active Expired - Lifetime
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