LT3050B - Process for the preparing of coloureless polyhydroxyalkanoate - Google Patents
Process for the preparing of coloureless polyhydroxyalkanoate Download PDFInfo
- Publication number
- LT3050B LT3050B LTIP543A LTIP543A LT3050B LT 3050 B LT3050 B LT 3050B LT IP543 A LTIP543 A LT IP543A LT IP543 A LTIP543 A LT IP543A LT 3050 B LT3050 B LT 3050B
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- LT
- Lithuania
- Prior art keywords
- extraction
- polyhydroxyalkanoate
- pha
- biomass
- preparing
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/62—Carboxylic acid esters
- C12P7/625—Polyesters of hydroxy carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/88—Post-polymerisation treatment
- C08G63/90—Purification; Drying
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- Organic Chemistry (AREA)
- Wood Science & Technology (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Zoology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Polymers & Plastics (AREA)
- General Chemical & Material Sciences (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Medicinal Chemistry (AREA)
- Microbiology (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polyesters Or Polycarbonates (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Biological Depolymerization Polymers (AREA)
- Medicinal Preparation (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Materials For Medical Uses (AREA)
Abstract
Description
Išradime pateikiamas (PHA) gavimo būdas. PHA susintetinamas auginant tam tikrose sąlygose bakterijų biomasę jų ląstelėse kaip kaupimo medžiagą.The present invention provides a method of obtaining (PHA). PHA is synthesized by growing bacterial biomass in their cells as a storage medium under certain conditions.
Tam tikrose fermentacijos sąlygose įvairūs mikroorganizmai susintetina polimerus - hidroksialkanato rūgštis, pavyzdžiui polihidrosviesto rūgštį (PHS) arba kopolimerą polihidroksivalerijono rūgštį, taip pat ir kitas polihidroanglies rūgštis. Greta to, ląstelėse visada atsiranda lipidai ir spalvinės medžiagos, kurios, kaip tepliosios medžiagos, trukdo tolesniam gauto PHA apdirbimui. Yra žinomas būdas, kuriuo lipidai ir spalvinės medžiagos pašalinamos alkoholiu arba acetonu (EP 15 123, EP 58 480, EP 124 3Q9) . Tačiau naudoj antis šiuo būdu kai kurios spalvinės medžiagos įgyj a .nepageidaujamą atspalvį, t.y. gaunamas baltasUnder certain fermentation conditions, various microorganisms synthesize polymers such as hydroxyalkanoic acids, such as polyhydric butyric acid (PHS) or copolymer polyhydroxy valeric acid, as well as other polyhydro carbonic acids. In addition, cells always contain lipids and dyes that, like lubricants, interfere with the subsequent processing of the resulting PHA. There is a known method for removing lipids and coloring agents with alcohol or acetone (EP 15 123, EP 58 480, EP 124 309). However, when using ducks in this way, some of the colored materials acquire an undesirable hue, i.e. resulting in white
Kita galimybė bespalviam polimerui gauti yra paveikti :;0/:j/į///:::|HA/0//ti;rpikl;ių/ (DD .27 6 304)’. Tai išsprendžiama, , auginant bakterijų biomasę. Iš kitos pusės didelio //:/ kiekio ir įvairių''ŽŪirpikįių/'/ĘąhaddpjrmąB/Bąpšųnkįhąt/i^fiA gavimą. Galimas didelis tirpiklių ir nusodintojų kiekisAnother option for obtaining a colorless polymer is affected by:; 0 /: j / to /// ::: | HA / 0 // ti; rpikl ; s / (DD .27 6 304) '. This is solved by growing bacterial biomass. On the other hand, the receipt of large quantities of //: / and various''Ž ir p p /' / h h h ad d d pj / / / / h h h A / / / / ^. Large amounts of solvents and precipitators are possible
PHA.PHA.
Išradimo uždavinys yra pašalinti iš PHA spalvines medžiagas, atsiradusias mikroorganizmų auginimo ir PHA akumuliacijos procese ląstelėse.SUMMARY OF THE INVENTION It is an object of the invention to remove from PHA dyes that result from the cultivation of microorganisms and PHA in cells.
Pagal išradimą bespalvio PHA gavimas iš bakterijų biomasių, atliekant palaipsnį drėgnos bakterijų biomasės džiovinimą, PHA ekstrakciją acto rūgštimi ir PHA nusodinimą, yra numatytas taip, kad išdžiovinta bakterijų biomasė prieš ekstrakciją yra apdorojama termiškai .· Tam išdžiovinta 0 bakterijų :? biomasė laikotarpyje nuo 10 iki 120 min. kaitinamą temperatūroje nuo ,80°C iki apatinės polihidroksialkanoato lydymosi temperatūros ribos. Šio temperatūros poveikio rezultate bakterijų biomasėje esanti spalvinė medžiaga · įgyja tokią formą, kuri nebedaro . įtakos tolesniam polimero apdirbimui. Toliau atliekama ekstrakcija acto rūgštimi, pridedant nuo 1 iki 10 % nuo bendro ekstrakcijos medžiagos tūrio alifatinės karboninės rūgšties derinių. Šie alifatiniai anglies rūgšties dariniai gali būti, pavyzdžiui, acto rūgšties anhidridas arba β - butirolaktonas..According to the invention, the production of colorless PHA from bacterial biomass by stepwise drying of wet bacterial biomass, extraction of PHA with acetic acid, and precipitation of PHA is contemplated such that the dried bacterial biomass is subjected to heat treatment prior to extraction. biomass in the period from 10 to 120 min. heated at a temperature from, 80 ° C to a lower melting point of polyhydroxyalkanoate. As a result of this temperature effect, the coloring material in the bacterial biomass · acquires a form that no longer does. influence the further processing of the polymer. Acetic acid extraction followed by addition of 1 to 10% by volume of aliphatic carbonic acid combinations. These aliphatic carbonic acid derivatives may be, for example, acetic anhydride or β-butyrolactone.
Ekstrakcija atliekama žinomose sąlygose. Taip, ekstrakcijos priemonių pagalba, prisilaikant atitinkamų, išradime nurodytų, sąlygų, išskiriamas šviesus PHA.Extraction is carried out under known conditions. Yes, the extraction means release the light PHA under the appropriate conditions of the invention.
15? . Alifatinės karboninės rūgšties dariniai ir spalvinė medžiaga lieka ekstrakcijos preparate.15? . Aliphatic carbonic acid derivatives and coloring matter remain in the extraction preparation.
Labiausiai stebina tai, kad atlikus PHA ekstrakciją išradime 'pasiūlytu mišiniu, susidedančiu iš acto rūgšties · ir iš acto rūgšties anhidrido, gaunamas šviesesnis PHA, negu atliekant ekstrakciją tik su acto rūgštimi arba tik · su acto rūgšties ' anhidridu. Buvo netikėta, kad kartu su acto rūgštimi panaudojus ir l-s-10 % nuo bendro ekstrakcijos preparato tūrio acto rūgšties anhidrido, šitaip smarkiai sumažėjo spalvinės medžiagos 2 kiekis PHA, palyginus su e kstrakeij a, naudoj ant tik acto rūgšties anhidridą.Most surprisingly, the extraction of PHA with a mixture of acetic acid and acetic anhydride of the invention provides a lighter PHA than with extraction with acetic acid or only with acetic anhydride. It was unexpected that the use of acetic anhydride in an amount of 1 to 10% of the total volume of the extraction preparation resulted in a significant decrease in the amount of coloring agent 2 in the PHA compared to the extract, using only acetic anhydride.
3030th
Būdo, pateikto šiame išradime, privalumas yra tas, kad nebereikia naudoti papildomų tirpiklių išdžiovintos bakterijų biomasės priešekstrakcijai, kuri atliekama spalvinei medžiagai pašalinti prieš ekstrakciją, kaip kad yra daroma, gaunant žymiai didesnės grandinės ilgio po-1 imerus, panaudo j ant 7 pakopinį PHA nusodinimą. Išradimas paaiškinamas/.sekančiais pavyzdžiais. / ' ' 3 -'7.An advantage of the process of the present invention is that no additional solvents are required for pre-extraction of the dried bacterial biomass, which is performed to remove the color material prior to extraction, as is done with 7-step PHA precipitation for substantially higher chain length po-1. . The invention is illustrated by the following examples. / '' 3 -'7.
Pavyzdys palyginimuiExample for comparison
Iki blizgesio išdžiovinta bakterijųbiomasė (šviesumas pagal HUNTER Lab=64,5) virimo temperatūroje ekstra5 huojama acto rūgštimi santykiu 1:10 ir apdorojama žinomais būdais. Gautas polihidrosviesto rūgšties (PHB) šviesumas būtų L=75,3.The bacterial biomass (luminosity according to HUNTER Lab = 64.5) dried to shine is extracted with acetic acid in a ratio of 1:10 at boiling point and treated in known manner. The resulting luminance of polyhydricbutyric acid (PHB) would be L = 75.3.
I-asis pavyzdysExample I
Iki blizgesio išdžiovinta bakterijų biomasė prieš ekstrakciją buvo apdorota termiškai džiovinimo.spinto j e. . Žemiausia polihidroksisviesto rūgšties lydymosi temperatūra buvo 160cČ. .Po to sekė apdorotos bakterijų .15 biomasės ekstrakcija acto rūgštimi santykiu 1:10, pridedant acto rūgšties anhidrido: vienu a'tveju 1 % nuo bendro ekstrakcijos preparatų tūrio, kitu atveju 10 %,/· j nuo bendro tūrio . Gavosi .?··: sekančio;; šviesumo , (pagal HUNTER) PHB: ' // /--/-.:777 //7į'.7' 77/'7777'<77/77 Bacterial biomass dried to shine prior to extraction was subjected to heat drying.spinto j e. . Lower polyhydroxy butyric acid, a melting point was 160 cc. This was followed by the extraction of the treated bacterial .15 biomass with acetic acid in a ratio of 1:10 by the addition of acetic anhydride: one at a time of 1% of the total volume of the extraction preparations, otherwise at 10%, of the total volume. Received.? ·· : next ;; brightness (based HUNTER) PHB: '// // - .: 777 //7į'.7' 7 7 / '7 777'<7 7/77
-:2.0 '-: 2.0 '
Acto rūgšties anhidridas, //i·į/:';///'..’-;· % nuo bendro ekstrakcijos '/,>'· 777:77/ preparatų tūrio ·.·/ ‘ .·,.//--:.Acetic anhydride, //i··/:';///'..'-;·% of total extraction '/,>' · 777 : 77 / volume of preparations ·. · / '. ·,. // -:.
////./ /.'/-į.'... 7/7,./į-į;;-·/'.·77'·';·'·'7·'/./'/'' ----/ 7'////./ /.'/- to .'... 7 / 7,./ .- ;;;-·/'.· 77 '·'; · '·' 7 · '/./' / '' ---- / 7 '
II-asis pavyzdys įExample II to
Atitinkamai I-ajam pavyzdžiui, iki blizgesio išdžiovinta bakterijų biomasė prieš ekstrakciją apdorota termiškai.i Ekstrakcijos preparatui . acto .--:.// rūgščiai priedu paimtas β - butirolaktonas: vienu atveju paimtas 1 %, o kitu atveju 10 % nuo bendro ekstrakcijos preparato kiekio. Gavosi sekančio šviesumo L (pagal HUNTER) PHB: β - butirolaktonas, .% bendram-ekstrakcijos preparato kiekiuiAccording to Example I, the bacterial biomass dried to shine was heat treated prior to extraction. acetic .--: .// acid-treated β-butyrolactone: in one case 1% and in another 10% of the total extract. The following luminosity L (by HUNTER) PHB was obtained: β - butyrolactone,% for total extraction preparation
Claims (3)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19924215862 DE4215862A1 (en) | 1992-05-14 | 1992-05-14 | Dye-free poly-hydroxy-alkanoate prodn. - comprises drying moist bacterial biomass and heating followed by extn. with acetic acid |
DE4215860A DE4215860A1 (en) | 1992-05-14 | 1992-05-14 | Dye-free poly:hydroxy:alkanoate prodn. - comprises drying moist bacterial biomass and extracting using acetic acid contg. beta-butyrolactone |
DE19924215861 DE4215861C2 (en) | 1992-05-14 | 1992-05-14 | Process for the production of dye-free polyhydroxyalkanoates |
Publications (2)
Publication Number | Publication Date |
---|---|
LTIP543A LTIP543A (en) | 1994-04-25 |
LT3050B true LT3050B (en) | 1994-10-25 |
Family
ID=27203739
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
LTIP543A LT3050B (en) | 1992-05-14 | 1993-05-12 | Process for the preparing of coloureless polyhydroxyalkanoate |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP0641387B1 (en) |
AT (1) | ATE167702T1 (en) |
CZ (1) | CZ282634B6 (en) |
DK (1) | DK0641387T3 (en) |
EE (1) | EE03060B1 (en) |
ES (1) | ES2118957T3 (en) |
LT (1) | LT3050B (en) |
LV (1) | LV10656B (en) |
RU (1) | RU2123048C1 (en) |
SK (1) | SK279080B6 (en) |
WO (1) | WO1993023554A1 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5942597A (en) * | 1995-08-21 | 1999-08-24 | The Procter & Gamble Company | Solvent extraction of polyhydroxyalkanoates from biomass |
DE19623778A1 (en) * | 1995-09-09 | 1997-12-18 | Buna Sow Leuna Olefinverb Gmbh | Extractant for polyhydroxyalkanoic acids |
ATE364708T1 (en) | 1997-04-15 | 2007-07-15 | Metabolix Inc | HIGH TEMPERATURE PHA EXTRACTION WITH POOR-SOLVING SOLVENTS FOR PHA |
US6043063A (en) * | 1997-04-15 | 2000-03-28 | Monsanto Company | Methods of PHA extraction and recovery using non-halogenated solvents |
DE69840594D1 (en) | 1997-07-22 | 2009-04-09 | Metabolix Inc | POLYHYDROXYALKANOATE MOLDING |
US7455999B2 (en) | 1998-01-22 | 2008-11-25 | Metabolix, Inc. | Transgenic systems for the manufacture of poly (3-hydroxy-butyrate-co-3-hydroxyhexanoate) |
WO2002016284A2 (en) | 2000-08-23 | 2002-02-28 | Metabolix, Inc. | Low molecular weight polyhydroxyalkanoate molding compositions |
WO2006025375A1 (en) | 2004-08-31 | 2006-03-09 | Riken | Biopolyester with thermal stability |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0015123A1 (en) | 1979-02-21 | 1980-09-03 | Imperial Chemical Industries Plc | A process for the extraction of poly-3-hydroxy-butyric acid from microbial cells |
EP0058480A1 (en) | 1981-02-12 | 1982-08-25 | Imperial Chemical Industries Plc | Extraction of poly(beta-hydroxybutyric acid) |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1720325A1 (en) * | 1967-11-28 | 1971-06-16 | Battelle Development Corp | Process for stabilizing polytetramethylglycolide against thermal depolymerization |
DD229428A1 (en) * | 1984-11-28 | 1985-11-06 | Akad Wissenschaften Ddr | PROCESS FOR EXTRACTION OF POLY-SS HYDROXYBUTTERIC ACID FROM BACTERIA BIOMASS |
AT390068B (en) * | 1988-07-07 | 1990-03-12 | Danubia Petrochemie | EXTRACTION AGENT FOR POLY-D (-) - 3-HYDROXYBUTTERIC ACID |
-
1993
- 1993-04-28 RU RU94046071A patent/RU2123048C1/en active
- 1993-04-28 CZ CZ942664A patent/CZ282634B6/en not_active IP Right Cessation
- 1993-04-28 ES ES93911727T patent/ES2118957T3/en not_active Expired - Lifetime
- 1993-04-28 AT AT93911727T patent/ATE167702T1/en not_active IP Right Cessation
- 1993-04-28 WO PCT/DE1993/000372 patent/WO1993023554A1/en active IP Right Grant
- 1993-04-28 DK DK93911727T patent/DK0641387T3/en active
- 1993-04-28 EP EP93911727A patent/EP0641387B1/en not_active Expired - Lifetime
- 1993-04-28 SK SK1313-94A patent/SK279080B6/en unknown
- 1993-05-12 LT LTIP543A patent/LT3050B/en not_active IP Right Cessation
- 1993-05-13 LV LVP-93-334A patent/LV10656B/en unknown
-
1994
- 1994-09-29 EE EE9400076A patent/EE03060B1/en unknown
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0015123A1 (en) | 1979-02-21 | 1980-09-03 | Imperial Chemical Industries Plc | A process for the extraction of poly-3-hydroxy-butyric acid from microbial cells |
EP0058480A1 (en) | 1981-02-12 | 1982-08-25 | Imperial Chemical Industries Plc | Extraction of poly(beta-hydroxybutyric acid) |
Also Published As
Publication number | Publication date |
---|---|
LV10656A (en) | 1995-04-20 |
ATE167702T1 (en) | 1998-07-15 |
RU2123048C1 (en) | 1998-12-10 |
SK131394A3 (en) | 1995-11-08 |
SK279080B6 (en) | 1998-06-03 |
EE03060B1 (en) | 1997-12-15 |
DK0641387T3 (en) | 1999-04-06 |
CZ266494A3 (en) | 1995-03-15 |
WO1993023554A1 (en) | 1993-11-25 |
EP0641387A1 (en) | 1995-03-08 |
LV10656B (en) | 1996-02-20 |
CZ282634B6 (en) | 1997-08-13 |
ES2118957T3 (en) | 1998-10-01 |
EP0641387B1 (en) | 1998-06-24 |
LTIP543A (en) | 1994-04-25 |
RU94046071A (en) | 1997-03-10 |
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