US2094693A - Nitration of sugars and their glycosides - Google Patents

Nitration of sugars and their glycosides Download PDF

Info

Publication number
US2094693A
US2094693A US27049A US2704935A US2094693A US 2094693 A US2094693 A US 2094693A US 27049 A US27049 A US 27049A US 2704935 A US2704935 A US 2704935A US 2094693 A US2094693 A US 2094693A
Authority
US
United States
Prior art keywords
nitrated
sugar
acid
nitration
nitrating
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
Application number
US27049A
Inventor
Joseph A Wyler
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Trojan Powder Co
Original Assignee
Trojan Powder Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Trojan Powder Co filed Critical Trojan Powder Co
Priority to US27049A priority Critical patent/US2094693A/en
Application granted granted Critical
Publication of US2094693A publication Critical patent/US2094693A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C201/00Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
    • C07C201/02Preparation of esters of nitric acid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H1/00Processes for the preparation of sugar derivatives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H11/00Compounds containing saccharide radicals esterified by inorganic acids; Metal salts thereof
    • C07H11/02Nitrates; Nitrites
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H15/00Compounds containing hydrocarbon or substituted hydrocarbon radicals directly attached to hetero atoms of saccharide radicals
    • C07H15/02Acyclic radicals, not substituted by cyclic structures
    • C07H15/04Acyclic radicals, not substituted by cyclic structures attached to an oxygen atom of the saccharide radical

Definitions

  • My invention relates to improvements in the nitration of sugars and their glycosides, and more particularly relatesto improved means for bringing about the nitration of sugars such as cane sugar, glucose, levulose, lactose, and the like, or the glycosides thereof, with the production of products having satisfactory physical characteristics and also having satisfactory chemical characteristics particularly with reference to stability.
  • One of the objects of my invention is to provide improved means for the nitration of the various sugars and their glycosides, and another of the objects of my invention is to provide improved means for the preparation of the nitrated sugars and their glycosides in Very pure condition.
  • My present invention rests upon my discovery that the nitrated esters of certain hydroxy acids dissolve nitrated sugar readily and produce mix- 'tures which may contain as much as 70% of nitrated sugar, while still having such physical characteristics as will permit them to be purified and stabilized by known washing and stabilizing methods.
  • glucose, levulose, lactose, etc. are nitrated by the ordinary methods known up to this time, thick, gummy, pasty or very viscous nitrated products are obtained which are very difficult to purify and to stabilize. If such agents as glycerin, glycols, and chlorhydrins are used as partial solvents, thick solutions are obtained which, if they contain more than 25% of nitrated sugar, are too viscous to be treated by the usual washing and stabilizing methods.
  • nitrated esters which I may employ in the practice of my present invention
  • nitrated methyl glycollate nitrated ethyl glycollate, nitrated propyl glycollate, nitrated butyl glycollate, nitrated amyl glycollate, nitrated methyl lactate, nitrated ethyl lactate, nitrated propyl lactate, nitrated butyl lactate, nitrated amyl lactate, nitrated methyl tartronate, nitrated ethyl tartronate, nitrated methyl malate, nitrated ethyl malate, nitrated dimethyl tartrate, nitrated diethyl tartrate, and the higher homologues.
  • the purpose of the work is to prepare the crystalline sugar nitrate I find the use of nitrated butyl lactate is particularly advantageous.
  • nitrated esters may be used either directly as such, or they may be produced in the same nitration operation as is the nitrated sugar or the nitrated glycoside, by the addition or the esters to the nitration mixture.
  • sugars to be used in the procedure of my invention I may use cane sugar, glucose, lactose, levulose, etc. and as glycosides, I may use methyl glucoside, ethyl glucoside, methyl lactoside, ethyl lactoside, etc. 5
  • Example 1 To 990 parts of mixed acid consisting of 40% H2SO4 and 60% HNOa add 60 parts of dibutyl tartrate, keeping the temperature below 30 G. Then add 60 parts of powdered cane sugar, maintaining the temperature below 30 C., and preferably below 20 C. Stir continuously-throughout the nitration.
  • the nitration mixture is settled and the solution of nitrated sugar in the dinitrated butyl tartrate forms the upper layer.
  • the latter is separated, washed in dilute alkali, stabilized and settled or filtered to remove moisture and mechanical impurities.
  • Example 2 To 150 parts of 98% ENG: cooled to below 20 0., add 20 parts of methyl glucoside with constant stirring and cooling. Then add 20 parts of butyl lactate, keeping the temperature below 20 G. Then add 200 parts of 105% oleum to complete the nitration and to cause a separation of the nitrated products as a solution floating upon the spent acid. The separated nitrated glucoside solution is then washed, neutralized,
  • Example 3.-108 parts of ethyl lactate are run into 1126 parts of a mixed acid consisting of 40% H2SO4 and 60% I-INOs mantained at a temperature below 30 C. Thenadd 80 parts of cane sugar, a littleat a time, keeping the tem perature below 25 C. and preferably lower than 10 C. The nitration mixture is then allowed to stand, when separation into two layers will occur. The upper layer is the nitrated product and can be readily separated, and should then be washed, filtered and neutralized according to the methods well known in the art.
  • Example 4.1126 parts of a mixed acid con- 'sisting of I-INOs and 40% H2804 are placed time of nitration is often about four hours.
  • the nitrated charge is then run to a settler where the mixture separates into two layers.
  • the lower layer is' the spent acid and contains only a' small amount of nitrated products.
  • the upper layer consists of the nitrated ethyl lactate and nitrated sugar. At times this upper layer has a small amount of crystalline nitrated sugar suspended in it.
  • the upper layer is then drowned intap water,
  • the lower layer is a mixture of nitrated ethyl lactate and sucrose nitrate'with some occluded Water. By settling overnight only a small amount of water remains in suspension.
  • Example 5 -l126 parts of a'mixed acid con- ,sisting 01 .5% nitric acid and 50% sulfuric acid and 5%. water are placed in a suitable nitrating vessel and cooled to about 0 0. Then, with continued stirring and cooling, add 108 parts of nitrated butyl lactate. When all the nitrated'butyl lactate has been added, add parts of powdered dried sucrose, maintaining the temperature around 0 C. The stirring and cooling is continued for about one hour after the feeding of the sugar in order to complete the nitration. V
  • the nitrated'charge is handled in the'manner as described in Example 4.
  • nitrating cane sugar which comprises the addition of an alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a mixed acid consisting of approximately 60% HNOs and 40% H2804 followed by the addition of the cane sugar, maintaining the temperature of the mixture below 30 C. and separating nitrated products from the spent acid.
  • nitrating cane sugar which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, the separation of the nitrated sugar-nitrated hydroxy acid ester mixture from the excess of water, and the solution of the nitrated hydroxy acid ester in a solvent in which nitrated sugar is substantially insoluble.
  • nitrating glucose which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, the separation of the nitrated sugar-nitrated hydroxy acid ester mixture from the excess of water, and the solution of the nitrated hydroxy acid ester in a solvent in which nitrated sugar is substantially insoluble.
  • nitrating a sugar which comprises the addition of the sugar and the alkyl ester of a saturated'hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, and the solution of the nitrated hydroxy acid ester in a solvent selected from the group of ethyl alcohol, propyl al- .cohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
  • a solvent selected from the group of ethyl alcohol, propyl al- .cohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
  • nitrating cane sugar which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, and the solution of the nitrated hydroxy acid ester in a solvent selected from the group of ethyl alcohol, propyl alcohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
  • a solvent selected from the group of ethyl alcohol, propyl alcohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
  • a solvent selected from the group of ethyl a1- cohol, propyl alcohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
  • lactose and their glycosides in the presence of an alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Molecular Biology (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Saccharide Compounds (AREA)

Description

Patented Oct. 5, 1937 5. QFFICE NITRATION F SUGARS AND THEIR GLYCOSIDES Joseph A.- Wyler, Allentown, Pa., assignor to Tro- .ian Powder Company, a corporation of New York No Drawing. Application June 17, 1935,
Serial No. 27,049
22 Claims. (Cl. 260-145) My invention relates to improvements in the nitration of sugars and their glycosides, and more particularly relatesto improved means for bringing about the nitration of sugars such as cane sugar, glucose, levulose, lactose, and the like, or the glycosides thereof, with the production of products having satisfactory physical characteristics and also having satisfactory chemical characteristics particularly with reference to stability. One of the objects of my invention is to provide improved means for the nitration of the various sugars and their glycosides, and another of the objects of my invention is to provide improved means for the preparation of the nitrated sugars and their glycosides in Very pure condition. This application is a continuation in part of my application S. N. 728,679, filed June 2, 1934.
My present invention rests upon my discovery that the nitrated esters of certain hydroxy acids dissolve nitrated sugar readily and produce mix- 'tures which may contain as much as 70% of nitrated sugar, while still having such physical characteristics as will permit them to be purified and stabilized by known washing and stabilizing methods. glucose, levulose, lactose, etc. are nitrated by the ordinary methods known up to this time, thick, gummy, pasty or very viscous nitrated products are obtained which are very difficult to purify and to stabilize. If such agents as glycerin, glycols, and chlorhydrins are used as partial solvents, thick solutions are obtained which, if they contain more than 25% of nitrated sugar, are too viscous to be treated by the usual washing and stabilizing methods.
As examples of the nitrated esters which I may employ in the practice of my present invention I will mention nitrated methyl glycollate, nitrated ethyl glycollate, nitrated propyl glycollate, nitrated butyl glycollate, nitrated amyl glycollate, nitrated methyl lactate, nitrated ethyl lactate, nitrated propyl lactate, nitrated butyl lactate, nitrated amyl lactate, nitrated methyl tartronate, nitrated ethyl tartronate, nitrated methyl malate, nitrated ethyl malate, nitrated dimethyl tartrate, nitrated diethyl tartrate, and the higher homologues. When the purpose of the work is to prepare the crystalline sugar nitrate I find the use of nitrated butyl lactate is particularly advantageous.
The nitrated esters may be used either directly as such, or they may be produced in the same nitration operation as is the nitrated sugar or the nitrated glycoside, by the addition or the esters to the nitration mixture.
It is well known that when cane sugar,
As sugars to be used in the procedure of my invention, I may use cane sugar, glucose, lactose, levulose, etc. and as glycosides, I may use methyl glucoside, ethyl glucoside, methyl lactoside, ethyl lactoside, etc. 5
As examples of the application of my present invention, for the purpose of illustrating its general features, I give the following:
Example 1.To 990 parts of mixed acid consisting of 40% H2SO4 and 60% HNOa add 60 parts of dibutyl tartrate, keeping the temperature below 30 G. Then add 60 parts of powdered cane sugar, maintaining the temperature below 30 C., and preferably below 20 C. Stir continuously-throughout the nitration.
At the completion of the nitration the nitration mixture is settled and the solution of nitrated sugar in the dinitrated butyl tartrate forms the upper layer. The latter is separated, washed in dilute alkali, stabilized and settled or filtered to remove moisture and mechanical impurities.
Example 2.--To 150 parts of 98% ENG: cooled to below 20 0., add 20 parts of methyl glucoside with constant stirring and cooling. Then add 20 parts of butyl lactate, keeping the temperature below 20 G. Then add 200 parts of 105% oleum to complete the nitration and to cause a separation of the nitrated products as a solution floating upon the spent acid. The separated nitrated glucoside solution is then washed, neutralized,
stabilized and settled or filtered to remove moisture and mechanical impurities.
Example 3.-108 parts of ethyl lactate are run into 1126 parts of a mixed acid consisting of 40% H2SO4 and 60% I-INOs mantained at a temperature below 30 C. Thenadd 80 parts of cane sugar, a littleat a time, keeping the tem perature below 25 C. and preferably lower than 10 C. The nitration mixture is then allowed to stand, when separation into two layers will occur. The upper layer is the nitrated product and can be readily separated, and should then be washed, filtered and neutralized according to the methods well known in the art.
Example 4.1126 parts of a mixed acid con- 'sisting of I-INOs and 40% H2804 are placed time of nitration is often about four hours.
The nitrated charge is then run to a settler where the mixture separates into two layers. The lower layer is' the spent acid and contains only a' small amount of nitrated products. The upper layer consists of the nitrated ethyl lactate and nitrated sugar. At times this upper layer has a small amount of crystalline nitrated sugar suspended in it. c
The upper layer is then drowned intap water,
Washed, neutralized by stirring in 2% sodium bicarbonate, washed with water and allowed to settle. The lower layer is a mixture of nitrated ethyl lactate and sucrose nitrate'with some occluded Water. By settling overnight only a small amount of water remains in suspension.
This lower layer is then treated with .ethyl alcohol, while the mixture is being stirred untila crystalline precipitate of sucrose octonitrate separates. Only enough alcohol is added to cause this precipitation. 'The'mixture is filtered, the precipitate is washed with alcohol and dried at about 40 C. The yield of crystals is about 145 parts; i r
Example 5.-l126 parts of a'mixed acid con- ,sisting 01 .5% nitric acid and 50% sulfuric acid and 5%. water are placed in a suitable nitrating vessel and cooled to about 0 0. Then, with continued stirring and cooling, add 108 parts of nitrated butyl lactate. When all the nitrated'butyl lactate has been added, add parts of powdered dried sucrose, maintaining the temperature around 0 C. The stirring and cooling is continued for about one hour after the feeding of the sugar in order to complete the nitration. V
The nitrated'charge is handled in the'manner as described in Example 4.
Insteadof drowning the nitrated sugar mixture in water, and thereafter extracting the nitrated mixture with a solvent, it is of course possible to drown the. nitrated sugar mixture directly in a mixture of ethyl alcohol and a hydrocarbon to obtain directly, the precipitated crystalline nitrated sugar. w
While the above examples represent preferred methods'of nitration, itshould be noted that I do not confine myself to these narrowlimits. The characteristic'part of my invention'is the pres ence of a nitrated ester of a'hydr'oxy acid in'the nitration mixture at the time of the separation of the nitrated sugar or glycoside from the spent acid, and'it will readily be understood that I may vary the strengths and proportions of acids, the temperatures of the components and the temperature of nitration, the ratio of nitrated ester to sugar or to acids, the order ofxadditionqof materials to be nitrated, etc. without departing from the essence of this invention.
I have discovered that when a sugar is nitrated in the presence of a nitrated hydroxy acid the resulting nitrated mixture is capable of being separated to give the pure nitrated sugars in higher purity and in better yield than can be obtain'edby methods previously known, and this can beaccomplished without the use of repeated extractions or fracticnations. I' have discovered, for example, that thenitration products made in accordance with my present'invention may be extracted with such solvents as ethyl alcohol or propyl alcohol, or with such solvents as propane, butane, heptane, pentane, hexane,benzene, or ordinary commercial gasoline, or with mixed solvents such as pentane, hexane, etc. with chloroform or carbon tetrachloride, or withmfixed in order to complete the nitration. The total solvents such as an alcohol'anda chlorinated hydrocarbon, all of these solvents and solvent mixtures possessing. greater solvent action for the V nitrated hydroxyacid esters than they do for the sucrose octonitrate in the form of crystals from the nitration mixture of nitrated butyl lactate ,and cane sugar," without any recrystallization whatever, using in this case either ethyl alcohol or pentane as the differential solvent for dissolving the nitrated hydroxy acid ester and thus sep arating it from the insoluble nitrated sugar, and that these crystalsQbya simple stabilizing treatment such as stirring them in a two percent solution of bicarbonateof soda, or'by first stirring them in a two percent solution of bicarbonate of soda, and thereafter washing them in a one percent solution of ammonia, maybe obtained as the pure sucrose octonitrate having substantially the theoretical nitrogen content, and possessing substantially the same stability as the sucrose octoni trate previously obtained as the result of extensive recrystallization and stabilization treatments.
As many modifications may be made within the limits of the disclosure of my invention as herein set forth, it is to be understood that the examples herein given are for purposes of illustration and the figures therein given are not to be considered as limitations, and no limitations should be placed upon the scope of my invention except such as are indicated in the appended claims.
I claim: 1
l. The process of nitrating a member of the group consisting of a sugar and a sugar glycoside in the presence'of a nitrated alkyl ester of a saturated hydroxy aliphatic carboxylic acid, said car'- boxylic acid containing not more than two carboxyl groupsr V 2..The process of nitrating cane sugar in the presence of a nitrated alkyl ester of a saturated hydroxy'aliphaticicarboxylic acid, said carboxylic acid containing not more than two carboxyl groups. r
3. The process the-presence of a nitrated alkyl ester of a, saturated'hydroxy aliphatic carboxylic acid, said carboxylie acid containing not'mo're than two car boxyl groups 4. The p-rocess of nitratin g a sugarin the presence of a member of the group consisting of nitrated methyl glycollate, nitrated ethyl glycollate, nitrated propyl glycollate, nitrated butyl glycollate, nitrated .amyl glycollate, nitrated methyl lactate, nitrated ethyl lactate; nitrated propyl lactate nitrated butyl lactate, nitrated amyl lactate, nitrated methyl tartronate, nitrated ethyl tartronate, nitrated ethyl malate,"nitrated dimethyl tartr'ate and nitrated diethyl tartrate.
5. The process of nitrating glucose in the presenceof a member of the'groupoonsisting of nirated methyl glycollate, nitrated ethyl glycollate,
of nitrating methyl glucoside in nitrated propyl .glycollate, nitrated butyl glycollycollate, nitrated propyl glycollate, nitrated butyl glycollate, nitrated amyl glycollate, nitrated 7 methyl lactate, nitrated ethyl lactate, nitrated propyl lactate, nitrated butyl lactate, nitrated amyl lactate, nitrated methyl'tartronate, nitrated ethyl tartronate, nitrated ethyl malate, nitrated dimethyl tartrate and nitrated diethyl tartrate.
'7. The process of nitrating a sugar which corn;- prises the addition of the sugar and of the alkyl ester of a saturated hydroxy aliphatic-carboxylic acid containing not more thg'an two carboxyl groups, to a nitrating acid and the separation of the products of nitration from the spent acid.
8. The process of nitrating cane sugar which comprises the addition of an alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a mixed acid consisting of approximately 60% HNOs and 40% H2804 followed by the addition of the cane sugar, maintaining the temperature of the mixture below 30 C. and separating nitrated products from the spent acid. I
9. The process of nitrating cane sugar which comprises the addition of ethyl lactate to a mixed acid consisting of approximately 60% HNO3 and 40% H2SO4 followed by the addition of the cane sugar, maintaining the temperature of the mix ture below 30 C. and separating nitrated products from the spent acid.
10. The process of nitrating a sugar which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning cf the nitrated sugar-nitrated hydroxy acid ester mixture in Water, the separation of the nitrated sugar-nitrated hydroxy acid ester mixture from the excess of water, and the solution of the nitrated hydroxy acid ester in a solvent in which nitrated sugar is substantially insoluble.
11. The process of nitrating cane sugar which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, the separation of the nitrated sugar-nitrated hydroxy acid ester mixture from the excess of water, and the solution of the nitrated hydroxy acid ester in a solvent in which nitrated sugar is substantially insoluble.
12. The process of nitrating glucose which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, the separation of the nitrated sugar-nitrated hydroxy acid ester mixture from the excess of water, and the solution of the nitrated hydroxy acid ester in a solvent in which nitrated sugar is substantially insoluble.
13. The process of nitrating methyl glucoside which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, the separation of the nitrated sugar-nitrated hydroxy acid ester mixture from the excess of water, and the solution of the nitrated hydroxy acid ester in a solvent in which nitrated sugar is substantially insoluble. I
14. The process of nitrating a sugar which comprises the addition of the sugar and the alkyl ester of a saturated'hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, and the solution of the nitrated hydroxy acid ester in a solvent selected from the group of ethyl alcohol, propyl al- .cohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
15. The process of nitrating cane sugar which comprises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, and the solution of the nitrated hydroxy acid ester in a solvent selected from the group of ethyl alcohol, propyl alcohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
16. The process of nitrating glucose which com prises the addition of the sugar and the alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugar-nitrated hydroxy acid ester mixture in water, and the solution of the nitrated hydroxy acid ester in a solvent selected from the group of ethyl alcohol, propyl alcohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
1'7. The process of nitrating methyl glucoside which comprises the addition of the glucoside and the alkyl ester of a saturated hydroxy alie phatic carboxylic acid containing not more than two carboxyl groups, to a nitrating acid, the separation of the products of nitration from the spent acid, the drowning of the nitrated sugarnitr'ated hydroxy acid ester mixture in water,
and the solution of the nitrated hydroxy acid ester in a solvent selected from the group of ethyl a1- cohol, propyl alcohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform.
18. The process of nitrating a sugar in the presence of a nitrated alkyl ester of a saturated hydroxy aliphatic carboxylic acid, said carboxylic acid containing not more than two carboxyl groups.
19. The process ofnitrating a sugar which comprises the addition of an alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups, to a mixed acid consisting of roughly 60% nitric acid and 40% sulfuric acid followed by the addition of the sugar, maintaining the temperature of the mixture below 30 C. and separating nitrated products from the spentacid.
20. The process of nitrating a sugar which comprises the addition of ethyl lactate to a mixed acid, roughly 60% nitric acid and 40% sulfuric acid, followed by the addition of the sugar, maintaining the temperature of the mixture below 30 C., and separating nitrated products from the spent acid.
10 lected from the group of ethyl alcohol, propyl alcohol, propane, butane, pentane, benzene, gasoline, hexane, heptane, carbon tetrachloride and chloroform. V
22. The process of nitrating a member of the 'group consisting of cane sugar, glucose, levulose,
lactose, and their glycosides in the presence of an alkyl ester of a saturated hydroxy aliphatic carboxylic acid containing not more than two carboxyl groups.
JOSEPH A. WYLER. 10
US27049A 1935-06-17 1935-06-17 Nitration of sugars and their glycosides Expired - Lifetime US2094693A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US27049A US2094693A (en) 1935-06-17 1935-06-17 Nitration of sugars and their glycosides

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US27049A US2094693A (en) 1935-06-17 1935-06-17 Nitration of sugars and their glycosides

Publications (1)

Publication Number Publication Date
US2094693A true US2094693A (en) 1937-10-05

Family

ID=21835384

Family Applications (1)

Application Number Title Priority Date Filing Date
US27049A Expired - Lifetime US2094693A (en) 1935-06-17 1935-06-17 Nitration of sugars and their glycosides

Country Status (1)

Country Link
US (1) US2094693A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2602733A (en) * 1947-04-12 1952-07-08 Atlas Powder Co Process for the preparation of liquid nitric esters
US2662078A (en) * 1948-02-03 1953-12-08 Searle & Co Hyaluronic acid nitrates and the production thereof
US2969354A (en) * 1957-12-19 1961-01-24 Atlas Powder Co Aldohexose nitroureide tetranitrate and salts thereof
FR2358660A1 (en) * 1976-07-13 1978-02-10 Du Pont METHOD AND TEST KIT FOR DETERMINATION OF AMYLASE IN THE SERUM
US4147860A (en) * 1976-07-13 1979-04-03 E. I. Du Pont De Nemours And Company Process for preparing nitroaromatic glycosides
US4195174A (en) * 1977-04-14 1980-03-25 Chembiomed Ltd. Synthesis of 2-amino-2-deoxyglycoses and 2-amino-2-deoxyglycosides from glycals
US4362720A (en) * 1977-04-14 1982-12-07 Chembiomed Ltd. Synthesis of 2-amino-2-deoxyglycoses and 2-amino-2-deoxyglycosides from glycals

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2602733A (en) * 1947-04-12 1952-07-08 Atlas Powder Co Process for the preparation of liquid nitric esters
US2662078A (en) * 1948-02-03 1953-12-08 Searle & Co Hyaluronic acid nitrates and the production thereof
US2969354A (en) * 1957-12-19 1961-01-24 Atlas Powder Co Aldohexose nitroureide tetranitrate and salts thereof
FR2358660A1 (en) * 1976-07-13 1978-02-10 Du Pont METHOD AND TEST KIT FOR DETERMINATION OF AMYLASE IN THE SERUM
US4147860A (en) * 1976-07-13 1979-04-03 E. I. Du Pont De Nemours And Company Process for preparing nitroaromatic glycosides
US4195174A (en) * 1977-04-14 1980-03-25 Chembiomed Ltd. Synthesis of 2-amino-2-deoxyglycoses and 2-amino-2-deoxyglycosides from glycals
US4308376A (en) * 1977-04-14 1981-12-29 Chembiomed Ltd. Synthesis of 2-amino-2-deoxyglycoses and 2-amino-2-deoxyglycosides from glycals
US4362720A (en) * 1977-04-14 1982-12-07 Chembiomed Ltd. Synthesis of 2-amino-2-deoxyglycoses and 2-amino-2-deoxyglycosides from glycals

Similar Documents

Publication Publication Date Title
US2013034A (en) Sugar acylation
US2094693A (en) Nitration of sugars and their glycosides
US2204059A (en) Process for crystallizing organic explosive compounds
US2435125A (en) Purification of tryptophane
US1660651A (en) Nitration process
DE2004280C3 (en) Procedure for crystallizing vitamin D deep 3
US3408383A (en) Preparation of pentaerythritol trinitrate
US2857378A (en) Purification of beta-glucose pentaacetate
US2039046A (en) Nitration of sugars
US2500576A (en) Production of 7-dehydrosterols
US2520127A (en) Method of purifying rutin
US2417380A (en) Process for the preparation of alpha-nitro-isobutene
US2186975A (en) Crystalline calcium lactobionate calcium bromide and process for making the same
US1750948A (en) Process of making nitrated sugar explosives
US4119661A (en) Process for producing alkali salts of alkylsulphonic acids
US2525252A (en) Cyclo-trimethylenetrinitramine
US3231562A (en) Process for recovering unreacted sucrose from reaction solution of fatty acid sucrose ester
US2039045A (en) Nitration of sugars and their glycosides
US2878290A (en) Nitroguanidine preparation
EP0009290B1 (en) 3-azabicyclo(3.1.0)hexane derivatives and process for their preparation
US1503956A (en) Explosive and process of making same
US2073207A (en) Manufacture of ascorbic acid and its analogues
US2302324A (en) Nitric acid esters of monoacyl glycerines and their production
US2411169A (en) Isolation of dehydrocholic acid
US1691954A (en) Production of erythritol tetranitrate