(12) United States Patent (10) Patent No.: US 6,610,863 B2 Arumugam Et Al
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USOO6610863B2 (12) United States Patent (10) Patent No.: US 6,610,863 B2 Arumugam et al. (45) Date of Patent: Aug. 26, 2003 (54) CONTINUOUS PROCESS FOR PRODUCING DE 199 04 821 C1, 7/2000 L-ASCORBIC ACID EP O554090 A2 4/1983 EP 1 048 663 A1 11/2000 (75) Inventors: Bhaskar Krishna Arumugam, SE 1. is : 3.3. Kingsport, TN (US); Nick Allen GB 2O34 315 * 6/1980 Collins, Fall Branch, TN (US); JP 73015931 5/1973 Transito Lynne Macias, Petal, MS WO WO 87/0O839 2/1987 (US); Steven Thomas Perri, Kingsport, WO WO 97/13761 4/1997 TN (US); Jeffrey Earl Grant Powell, WO WO 99/07691 2/1999 Blountville, TN (US); Chester Wayne WO WOOO46216 8/2000 Sink, Kingsport, TN (US); Michael Roy Cushman, Punta Gorda, FL (US) OTHER PUBLICATIONS Anderson, S. et al., Production of 2-Keto-L-Gulonate, an (73) Assignee: Eastman Chemical Company, Intermediate in L-AScorbate Synthesis, by a Genetically Kingsport, TN (US) Modified Erwinia herbicola, Science, 230, pp. 144-149, 1985. (*) Notice: Subject to any disclaimer, the term of this Regna, P.P. et al., Kinetics of Transformation of 2-Keto patent is extended or adjusted under 35 polyhydroxy Acids, J. Am. Chem. Soc., 66, pp. 246-250, U.S.C. 154(b) by 0 days. 1944. Reichstein, T. et al., Eine ergiebige Synthese der 1-AScorb (21) Appl. No.: 10/037,126 ins?ure (C-Vitamine)) Helv. Chim. Acta, 17, pp. 311-328, 1934 * See Information Disclosure Statement for Descrip (22) Filed: Dec. 21, 2001 tion. (65) Prior Publication Data Saito, Y., Direct Fermentation of 2-Keto-L-Gulonic Acid in Recombinant Gluconobacter Oxydans, Biotechnol. Bioeng., US 2002/0151726 A1 Oct. 17, 2002 58 (2 & 3), pp. 309-315, 1998. Related U.S. Application Data Wankat, Rate-Controlled Separations, chapter 10.4, (60) Provisional application No. 60/257,991, filed on Dec. 22, Elsevier Applied Science, p. 524–541, Simulated Moving 2000, Bed Fractionation, 1990. (51) Int. Cl............................................... C07D 307/62 * cited by examiner (52) U.S. Cl. ....................................................... 549/315 Primary Examiner Joseph K. McKane (58) Field of Search .......................................... 549/315 Assistant Examiner Ebenezer Sackey (74) Attorney, Agent, or Firm-Eric D. Middlemas; (56) References Cited Bernard J. Graves, Jr. U.S. PATENT DOCUMENTS (57) ABSTRACT 2,265,121 A 12/1941 Reichstein 2.462,251 A 2/1949 Bassford et al. The present invention provides methods and an apparatus 2,491,065 A 12/1949 Van Eekelen et al. for the manufacture of an L-ascorbic acid product in high 4,111,958 A 9/1978 Crawford yield by direct conversion of an aqueous Solution containing 4,767,870 A 8/1988 Fujiwara et al. 2-keto-L-gulonic acid by contact with an acid catalyst or 5,128,487 A 7/1992 Tomislav et al. under thermal Self-catalyzed conditions at a conversion level 5,391,770 A 2/1995 Le Fur et al. that maximizes the formation of L-ascorbic acid and mini 5,637,734. A * 6/1997 Honda et al. ............... 549/315 mizes decomposition of the L-ascorbic acid thus formed. 5,744,618 A 4/1998 Fechtel et al. 5,817.238 A * 10/1998 Makino et al. ............... 21/635 The Separation process for L-ascorbic acid and KLG is 5.998,634. A 12/1999 Murphy et al. operated in Such a way that an efficient Separation process 6,004,445 A 12/1999 Genders et al. allows the majority of the KLG to be recycled for further 6,197.977 B1 3/2001 Böttcher et al. conversion. The product Stream from the Separation process is then Subjected to a recovery Step to obtain crystalline FOREIGN PATENT DOCUMENTS L-ascorbic acid product. DE 384.3389 6/1990 DE 19734086 C1 11/1996 36 Claims, 14 Drawing Sheets U.S. Patent Aug. 26, 2003 Sheet 3 of 14 US 6,610,863 B2 \/SV/|||ENOZ||NE8HOSEC] U.S. Patent Aug. 26, 2003 Sheet 4 of 14 US 6,610,863 B2 WSWIS)y %‘AuOOSÐTx{ssed-3||6u?S pea-ux>]©TX%09@pea-,GINS 00|09070Z0 O O O 09 CN V %)WWSW JO Soy U.S. Patent Aug. 26, 2003 Sheet S of 14 US 6,610,863 B2 | uueufieldwol-iuo?oesuo?oeax, blue1313Koeae 921. U.S. Patent Aug. 26, 2003 Sheet 6 of 14 US 6,610,863 B2 -0-KLG -- ASCOrbic Acid Figure 6 U.S. Patent Aug. 26, 2003 Sheet 7 of 14 US 6,610,863 B2 s Figure 7 U.S. Patent Aug. 26, 2003 Sheet 8 of 14 US 6,610,863 B2 100 90 80 70 30 20 10 % eOA U.S. Patent Aug. 26, 2003 Sheet 9 of 14 US 6,610,863 B2 3000 2800 2600 2400 2200 2000 1800 1600 1400 : 1200 1000 800 > 5 600 5 9 (2 5 O 400 M O 200 s R s % oN U.S. Patent Aug. 26, 2003 Sheet 10 of 14 US 6,610,863 B2 4400 4200 4000 3800 3600 3400 3200 3000 2800 2600 2400. 2200 2000 1800 1600 1400 1200 1000 > . 5 5> g2 800 2 S O 600 (M. O 400 200 s s 2 e % ooA U.S. Patent Aug. 26, 2003 Sheet 11 of 14 US 6,610,863 B2 1700 1650 1600 1550 1500 1450 1400 1350 1300 1250 1200 1150 1100 1050 1000 950 900 850 800 750 700 650 600 S50 500 450 O 400 2 ' H 350 rid d O > 300 CD S. CD O 250 CM) O 200 150 100 50 s Sr & s SE s R s O % 00A U.S. Patent Aug. 26, 2003 Sheet 12 of 14 US 6,610,863 B2 i g s s s SN Sp CO O V N O % W U.S. Patent Aug. 26, 2003 Sheet 13 of 14 US 6,610,863 B2 s s s s s s s s s s s s U.S. Patent Aug. 26, 2003 Sheet 14 of 14 US 6,610,863 B2 8SQ3 3g33 S. 3 O O O O O ve O OO N O O %iou"AlmoeleS WSW US 6,610,863 B2 1 2 CONTINUOUS PROCESS FOR PRODUCING cyclization process without the use of copious amounts of L-ASCORBIC ACID acid catalysts (T. Reichstein, Helv. Chim. Acta 17, 1934, pp. 311-328 and BP 428,815). Although aqueous cyclization This application claims priority to U.S. Provisional does not require the extensive purification StepS associated Application Serial No. 60/257,991, filed Dec. 22, 2000, the with acid catalysis, non-acid catalyzed intramolecular disclosure of which is hereby incorporated herein by refer cyclization is associated with relatively low yields. For CCC. example, 2-keto-L-gulonic acid may be heated in water This invention was made with United States Government saturated with carbon dioxide with 50% yield after fractional Support under Cooperative Research Agreement No. crystallization (U.S. Pat. No. 2,265,121). Also, 2-keto-L- 70NANB5H1138 awarded by the Advanced Technology gulonic acid or derivatives of 2-keto-L-gulonic acid may be Program of the National Institute of Standards and Technol heated to 130-140 C. in water to generate ascorbic acid ogy. The United States Government has certain rights in the with yields approximating 50% (U.S. Pat. No. 2,491,065). invention. Numerous attempts at direct cyclization processes for keto-L-gulonic acid (KLG) and derivatives thereof have FIELD OF THE INVENTION 15 been proposed in which the final product is isolated from the The present invention relates to a process for producing cyclization stream by removal of the solvent. Purification of L-ascorbic acid. More particularly, the present invention the L-ascorbic acid product is hampered, however, due to the relates to a continuous process for producing L-ascorbic acid instability of L-ascorbic acid product in aqueous or acid that minimizes decomposition of the L-ascorbic acid product reaction solutions (e.g. P. P. Regna and B. P. Caldwell, J. Am. formed and allows for unreacted Starting material to be Chem. Soc., 66, pp. 246-250, 1944), especially when the recycled back into the reaction mix. reaction is operated Such that conversion of the 2-keto-L- gulonic acid Starting material is nearly complete. Thus, there BACKGROUND OF THE INVENTION exists a need for a process that operates at leSS than complete L-AScorbic acid (vitamin C) is produced commercially by conversion, but allows for efficient use of the 2-keto-L- combined chemical and fermentation processes Starting 25 gulonic acid Starting material and produces purified from glucose or Sorbose. A common intermediate generated L-ascorbic acid in high yield. Accordingly, it is to the in the commercial process is 2-keto-L-gulonic acid (KLG), provision of Such processes that the present invention is or its protected form, diacetone-2-keto-L-gulonic acid. The directed. conversion of 2-keto-L-gulonic acid to L-ascorbic acid may be carried out by esterification with methanol, followed by SUMMARY OF THE INVENTION cyclization using Stoichiometric amounts of a base, in a The present invention relates to a proceSS for producing methodology derived from the original Reichstein proceSS L-ascorbic acid which comprises the Steps of Subjecting an (T. Reichstein, A. Grussner, Helv. Chim. Acta 17, p. aqueous Solution of 2-keto-L-gulonic acid (KLG) or deriva 311-328, 1934). Alternatively, diacetone-2-keto-L-gulonic tives of 2-keto-L-gulonic acid to an acid-catalyzed, or Self acid may be cyclized directly, with a loSS of acetone fol 35 catalyzed cyclization, followed by Separation of the product lowed by consecutive lactonization and enolization, to form L-ascorbic acid and any unreacted 2-keto-L-gulonic acid ascorbic acid.