Process for isolation of 2-keto-L-gulonic acid from fermented meat soup and use thereof
本发明公开了一种使存在于发酵水溶液中的2-酮基-L-古洛糖酸钠盐转变成其游离酸的醇溶液并且,如果需要,转变成该酸的烷基酯的方法。 Conversion of the sodium salt of 2-keto-L-gulonic acid, present in an aqueous fermentation solution, into an alcoholic solution of the free acid and optionally into an alkyl ester of the acid, comprises: (a) recovering sodium 2-keto-L-...
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creator | TOMISLAV KEGLEVIC RALF DUMPELMANN |
description | 本发明公开了一种使存在于发酵水溶液中的2-酮基-L-古洛糖酸钠盐转变成其游离酸的醇溶液并且,如果需要,转变成该酸的烷基酯的方法。
Conversion of the sodium salt of 2-keto-L-gulonic acid, present in an aqueous fermentation solution, into an alcoholic solution of the free acid and optionally into an alkyl ester of the acid, comprises: (a) recovering sodium 2-keto-L- gulonate-monohydrate by evaporation, cooling or displacement crystallisation and optionally comminuting the crystalline material by milling; (b1) suspending the recovered sodium 2-keto-L- gulonate-monohydrate from (a) in a low alcohol, allowing the crystals to swell and then adding an acid (I) with a low water content such that the measured pH is > 1.5; (b2) incorporating the recovered sodium -2-keto-L-gulonate-monohydrate from (a) together with a stoichiometric amount of an acid (I) with a low water content into a low alcohol using a wet milling procedure, the measured pH being > 1.5, or (b3) a combination of steps (b1) and (b2) with recycling of the materials streams; (c) separating the salt of the acid (I) formed in stage (b1),(b2) or (b3) to yield an alcoholic solution of the 2-keto-L-gulonic acid, and optionally (d) treating the alcoholic solution of the 2-keto-L-gulonic acid formed in (c) with a catalytic amount of an acid or an acid ion exchanger to esterify the 2-keto-L-gulonic acid with the alcohol to form the corresponding 2-keto-L-gulonic acid low alkyl ester. Stage (a) is preferably accomplished by continuous evaporative crystallisation. The low alcohol used in stage (b) is e.g. methanol, ethanol, propanol or glycol, especially methanol. The acid (I) is e.g. concentrated sulphuric acid, phosphoric acid, hydrochloric acid or nitric acid or gaseous HCl, and especially > 95 % H2SO4. The pH in stage (b) is 2.5-3.5. The temperature in stage (b) is 20-70 degrees C. The salt formed during stage (b) is removed e.g. by filtration and/or centrifuging, especially centrifuging. |
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Conversion of the sodium salt of 2-keto-L-gulonic acid, present in an aqueous fermentation solution, into an alcoholic solution of the free acid and optionally into an alkyl ester of the acid, comprises: (a) recovering sodium 2-keto-L- gulonate-monohydrate by evaporation, cooling or displacement crystallisation and optionally comminuting the crystalline material by milling; (b1) suspending the recovered sodium 2-keto-L- gulonate-monohydrate from (a) in a low alcohol, allowing the crystals to swell and then adding an acid (I) with a low water content such that the measured pH is > 1.5; (b2) incorporating the recovered sodium -2-keto-L-gulonate-monohydrate from (a) together with a stoichiometric amount of an acid (I) with a low water content into a low alcohol using a wet milling procedure, the measured pH being > 1.5, or (b3) a combination of steps (b1) and (b2) with recycling of the materials streams; (c) separating the salt of the acid (I) formed in stage (b1),(b2) or (b3) to yield an alcoholic solution of the 2-keto-L-gulonic acid, and optionally (d) treating the alcoholic solution of the 2-keto-L-gulonic acid formed in (c) with a catalytic amount of an acid or an acid ion exchanger to esterify the 2-keto-L-gulonic acid with the alcohol to form the corresponding 2-keto-L-gulonic acid low alkyl ester. Stage (a) is preferably accomplished by continuous evaporative crystallisation. The low alcohol used in stage (b) is e.g. methanol, ethanol, propanol or glycol, especially methanol. The acid (I) is e.g. concentrated sulphuric acid, phosphoric acid, hydrochloric acid or nitric acid or gaseous HCl, and especially > 95 % H2SO4. The pH in stage (b) is 2.5-3.5. The temperature in stage (b) is 20-70 degrees C. The salt formed during stage (b) is removed e.g. by filtration and/or centrifuging, especially centrifuging.</description><edition>7</edition><language>chi ; eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; APPARATUS THEREFOR ; BEER ; BIOCHEMISTRY ; CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; ENZYMOLOGY ; FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIREDCHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERSFROM A RACEMIC MIXTURE ; GENERAL METHODS OF ORGANIC CHEMISTRY ; METALLURGY ; MICROBIOLOGY ; MUTATION OR GENETIC ENGINEERING ; ORGANIC CHEMISTRY ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; SPIRITS ; THEIR RELEVANT APPARATUS ; TRANSPORTING ; VINEGAR ; WINE</subject><creationdate>2004</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20040630&DB=EPODOC&CC=CN&NR=1155554C$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,778,883,25551,76304</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20040630&DB=EPODOC&CC=CN&NR=1155554C$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>TOMISLAV KEGLEVIC</creatorcontrib><creatorcontrib>RALF DUMPELMANN</creatorcontrib><title>Process for isolation of 2-keto-L-gulonic acid from fermented meat soup and use thereof</title><description>本发明公开了一种使存在于发酵水溶液中的2-酮基-L-古洛糖酸钠盐转变成其游离酸的醇溶液并且,如果需要,转变成该酸的烷基酯的方法。
Conversion of the sodium salt of 2-keto-L-gulonic acid, present in an aqueous fermentation solution, into an alcoholic solution of the free acid and optionally into an alkyl ester of the acid, comprises: (a) recovering sodium 2-keto-L- gulonate-monohydrate by evaporation, cooling or displacement crystallisation and optionally comminuting the crystalline material by milling; (b1) suspending the recovered sodium 2-keto-L- gulonate-monohydrate from (a) in a low alcohol, allowing the crystals to swell and then adding an acid (I) with a low water content such that the measured pH is > 1.5; (b2) incorporating the recovered sodium -2-keto-L-gulonate-monohydrate from (a) together with a stoichiometric amount of an acid (I) with a low water content into a low alcohol using a wet milling procedure, the measured pH being > 1.5, or (b3) a combination of steps (b1) and (b2) with recycling of the materials streams; (c) separating the salt of the acid (I) formed in stage (b1),(b2) or (b3) to yield an alcoholic solution of the 2-keto-L-gulonic acid, and optionally (d) treating the alcoholic solution of the 2-keto-L-gulonic acid formed in (c) with a catalytic amount of an acid or an acid ion exchanger to esterify the 2-keto-L-gulonic acid with the alcohol to form the corresponding 2-keto-L-gulonic acid low alkyl ester. Stage (a) is preferably accomplished by continuous evaporative crystallisation. The low alcohol used in stage (b) is e.g. methanol, ethanol, propanol or glycol, especially methanol. The acid (I) is e.g. concentrated sulphuric acid, phosphoric acid, hydrochloric acid or nitric acid or gaseous HCl, and especially > 95 % H2SO4. The pH in stage (b) is 2.5-3.5. The temperature in stage (b) is 20-70 degrees C. The salt formed during stage (b) is removed e.g. by filtration and/or centrifuging, especially centrifuging.</description><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS</subject><subject>APPARATUS THEREFOR</subject><subject>BEER</subject><subject>BIOCHEMISTRY</subject><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><subject>CHEMISTRY</subject><subject>ENZYMOLOGY</subject><subject>FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIREDCHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERSFROM A RACEMIC MIXTURE</subject><subject>GENERAL METHODS OF ORGANIC CHEMISTRY</subject><subject>METALLURGY</subject><subject>MICROBIOLOGY</subject><subject>MUTATION OR GENETIC ENGINEERING</subject><subject>ORGANIC CHEMISTRY</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>SPIRITS</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><subject>VINEGAR</subject><subject>WINE</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2004</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNyr0NwjAUReE0FAjY4S7gIvxMYIEoEKJAoows-xosEj_Lz9kfCgbgNF9zlt3jVsVTFVEqksroWpIMidiaN5uYi3nOo-Tk4XwKiFUmRNaJuTFgomtQmQtcDpiVaC9WSlx3i-hG5ebnqsPpeLdnwyIDtTjPzDbYa98fvu2t3f2xfAB8XTjK</recordid><startdate>20040630</startdate><enddate>20040630</enddate><creator>TOMISLAV KEGLEVIC</creator><creator>RALF DUMPELMANN</creator><scope>EVB</scope></search><sort><creationdate>20040630</creationdate><title>Process for isolation of 2-keto-L-gulonic acid from fermented meat soup and use thereof</title><author>TOMISLAV KEGLEVIC ; RALF DUMPELMANN</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN1155554CC3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>chi ; eng</language><creationdate>2004</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><topic>APPARATUS THEREFOR</topic><topic>BEER</topic><topic>BIOCHEMISTRY</topic><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><topic>CHEMISTRY</topic><topic>ENZYMOLOGY</topic><topic>FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIREDCHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERSFROM A RACEMIC MIXTURE</topic><topic>GENERAL METHODS OF ORGANIC CHEMISTRY</topic><topic>METALLURGY</topic><topic>MICROBIOLOGY</topic><topic>MUTATION OR GENETIC ENGINEERING</topic><topic>ORGANIC CHEMISTRY</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>SPIRITS</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><topic>VINEGAR</topic><topic>WINE</topic><toplevel>online_resources</toplevel><creatorcontrib>TOMISLAV KEGLEVIC</creatorcontrib><creatorcontrib>RALF DUMPELMANN</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>TOMISLAV KEGLEVIC</au><au>RALF DUMPELMANN</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Process for isolation of 2-keto-L-gulonic acid from fermented meat soup and use thereof</title><date>2004-06-30</date><risdate>2004</risdate><abstract>本发明公开了一种使存在于发酵水溶液中的2-酮基-L-古洛糖酸钠盐转变成其游离酸的醇溶液并且,如果需要,转变成该酸的烷基酯的方法。
Conversion of the sodium salt of 2-keto-L-gulonic acid, present in an aqueous fermentation solution, into an alcoholic solution of the free acid and optionally into an alkyl ester of the acid, comprises: (a) recovering sodium 2-keto-L- gulonate-monohydrate by evaporation, cooling or displacement crystallisation and optionally comminuting the crystalline material by milling; (b1) suspending the recovered sodium 2-keto-L- gulonate-monohydrate from (a) in a low alcohol, allowing the crystals to swell and then adding an acid (I) with a low water content such that the measured pH is > 1.5; (b2) incorporating the recovered sodium -2-keto-L-gulonate-monohydrate from (a) together with a stoichiometric amount of an acid (I) with a low water content into a low alcohol using a wet milling procedure, the measured pH being > 1.5, or (b3) a combination of steps (b1) and (b2) with recycling of the materials streams; (c) separating the salt of the acid (I) formed in stage (b1),(b2) or (b3) to yield an alcoholic solution of the 2-keto-L-gulonic acid, and optionally (d) treating the alcoholic solution of the 2-keto-L-gulonic acid formed in (c) with a catalytic amount of an acid or an acid ion exchanger to esterify the 2-keto-L-gulonic acid with the alcohol to form the corresponding 2-keto-L-gulonic acid low alkyl ester. Stage (a) is preferably accomplished by continuous evaporative crystallisation. The low alcohol used in stage (b) is e.g. methanol, ethanol, propanol or glycol, especially methanol. The acid (I) is e.g. concentrated sulphuric acid, phosphoric acid, hydrochloric acid or nitric acid or gaseous HCl, and especially > 95 % H2SO4. The pH in stage (b) is 2.5-3.5. The temperature in stage (b) is 20-70 degrees C. The salt formed during stage (b) is removed e.g. by filtration and/or centrifuging, especially centrifuging.</abstract><edition>7</edition><oa>free_for_read</oa></addata></record> |
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subjects | ACYCLIC OR CARBOCYCLIC COMPOUNDS APPARATUS THEREFOR BEER BIOCHEMISTRY CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY ENZYMOLOGY FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIREDCHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERSFROM A RACEMIC MIXTURE GENERAL METHODS OF ORGANIC CHEMISTRY METALLURGY MICROBIOLOGY MUTATION OR GENETIC ENGINEERING ORGANIC CHEMISTRY PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL SPIRITS THEIR RELEVANT APPARATUS TRANSPORTING VINEGAR WINE |
title | Process for isolation of 2-keto-L-gulonic acid from fermented meat soup and use thereof |
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