JP4258577B2 - Process for producing poly-3-hydroxyalkanoic acid - Google Patents
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Description
【0001】
【発明の属する技術分野】
この出願は、ポリ−3−ヒドロキシアルカン酸の製造方法と、このポリ−3−ヒドロキシアルカン酸を大量に産生する遺伝子組換え生物に関するものである。さらに詳しくは、この出願は、代替プラスチック等として有用な高純度のポリ−3−ヒドロキシアルカン酸を簡便かつ大量に、しかも安価に製造する方法と、この方法に用いる新規生物に関するものである。
【0002】
【従来の技術】
ポリ−3−ヒドロキシアルカン酸(以下、「P(3HA)」と記載することがある)は、3−ヒドロキシアルカン酸の2以上がエステル結合等により重合した化合物の総称であり、例えば、ポリ−3−ヒドロキシブタン酸、ポリ−3−ヒドロキシヘキサン酸等がある。
【0003】
このP(3HA)は、近年、代替プラスチック等への利用が有望視されているが、化学合成による製造はコスト高となるため、バイオリアクター等による遺伝子工学的製造方法が検討されている。
この遺伝子工学的方法によるP(3HA)の製造では、P(3HA)を蓄積しない大腸菌等の宿主生物に他の生物由来のP(3HA)重合酵素の遺伝子を導入して宿主生物を形質転換し、この形質転換体をグルコース等の炭素源を含む培地で培養する方法が試みられてきた。大腸菌等のP(3HA)非蓄積生物は、その重合酵素を産生しないためにP(3HA)を蓄積しないと考えられるからである。
【0004】
しかしながら、P(3HA)非蓄積生物に重合酵素遺伝子を導入しただけではその形質転換体におけるP(3HA)蓄積能を増大させることはできないことから、大腸菌等におけるP(3HA)の非蓄積性は、その生物がP(3HA)重合酵素を産生しないことだけではなく、ポリ−3−ヒドロキシアルカン酸重合酵素の基質となる3−ヒドロキシアシルCoAの産生能が極めて低いことによるものであると推測されている。そこで、P(3HA)重合酵素遺伝子とともに、3−ヒドロキシアシルCoAの産生を促進するための脂肪酸合成酵素遺伝子を宿主生物に導入することが試みが報告されている(Williams 等:Protein Expr. Purif. 7:203-211, 1996)。この従来方法では、ラット由来の脂肪酸合成酵素の変異遺伝子と、Alcaligenes eutrophus由来のポリ−3−ヒドロキシアルカン酸重合酵素遺伝子とを昆虫(Spodoptera frugiperda)細胞に導入し、昆虫細胞用培地で3日間培養した結果、培地1リットル当たり600 mgの乾燥細胞、1mgのポリ−3−ヒドロキシアルカン酸を得ることに成功している。
【0005】
【発明が解決しようとする課題】
しかしながら、Williams 等の従来方法では、得られるP(3HA)は、乾燥細胞重量当たり0.17%と極めて少量であり、工業的規模での大量製造には適さない。また、宿主生物が昆虫細胞であるため、培養に特別な技術を必要とするといった問題点も存在した。
【0006】
この出願の発明は、以上のとおりの事情に鑑みてなされたものであって、従来方法の問題点を解消し、高純度のP(3HA)を簡便かつ大量に、しかも安価に製造することのできる新しいP(3HA)製造方法を提供することを課題としている。
またこの出願の発明は、この製造方法に用いる遺伝子組換え生物を提供することを課題としている。
【0007】
【課題を解決するための手段】
この出願は、前記の課題を解決する発明として、第1に、ポリ−3−ヒドロキシアルカン酸重合酵素遺伝子と、微生物由来の脂肪酸合成酵素遺伝子 fabH 、 fab D、 fab G、 acpP 、 fab Fのうちの1または2以上を大腸菌に導入して形質転換し、この形質転換大腸菌を炭素源存在下で増殖させ、この増殖した大腸菌からポリ−3−ヒドロキシアルカン酸を単離・精製することを特徴とするポリ−3−ヒドロキシアルカン酸の製造方法を、第2に、ポリ−3−ヒドロキシアルカン酸重合酵素遺伝子と、微生物由来の脂肪酸合成酵素遺伝子 fabH 、 fab D、 fab G、 acpP および fab Fを大腸菌に導入して形質転換し、この形質転換大腸菌を炭素源存在下で増殖させ、この増殖した大腸菌からポリ−3−ヒドロキシアルカン酸を単離・精製するポリ−3−ヒドロキシアルカン酸の製造方法を、第3に、微生物が大腸菌である前記第1または2の製造方法を提供する。
【0008】
またこの出願は、第4には、ポリ−3−ヒドロキシアルカン酸重合酵素遺伝子と、微生物由来の脂肪酸合成酵素遺伝子 fabH 、 fab D、 fab G、 acpP 、 fab Fのうちの1または2以上を大腸菌に導入することによって作出された形質転換大腸菌を、第5には、ポリ−3−ヒドロキシアルカン酸重合酵素遺伝子と、微生物由来の脂肪酸合成酵素遺伝子 fabH 、 fab D、 fab G、 acpP および fab Fを大腸菌に導入することによって作出された形質転換大腸菌を、第6には、微生物が大腸菌である前記第4または第5の形質転換大腸菌を提供する。
【0010】
【発明の実施の形態】
この発明の方法に使用するP(3HA)重合酵素遺伝子は、各種のP(3HA)蓄積生物に由来する遺伝子を用いることができる。そのような遺伝子としては例えば、Aeromonas caviae 由来のP(3HA)重合酵素遺伝子 phaCAC(Fukui et al., J. Bacteriol. 179:4821-4830, 1997 )、Alcaligenes eutrophus由来のP(3HA)重合酵素遺伝子 phbCAe (Peoples et al., J. Biol. Chem.262:15298-15303, 1989 )、Pseudomonas aeruginosa由来の重合酵素遺伝子 phaC1Pa (Timm et al., Eur. J. Biochem. 209:15-30, 1992 )等である。
【0011】
あるいは、これらの公知遺伝子をプローブとして、任意生物種のゲノムDNAから単離したP(3HA)重合酵素遺伝子を用いることもできる。
これらのP(3HA)重合酵素遺伝子は、微生物用の発現ベクターに組み込み、この組換えベクターを定法に従って大腸菌等の微生物に導入することによって形質転換微生物を作出することができる。発現ベクターは、微生物中で複製可能なオリジン、プロモーター、リボソーム結合部位、遺伝子クローニング部位、ターミネーター等を有する公知の微生物用発現ベクター(例えば、大腸菌用発現ベクターとしては、pUC系、pBluescript II、pET発現システム、pGEX発現システム)などを用いることができる。また、この出願の発明者らが新たに構築したプラスミドベクターpJRDTrc1(図1)を用いることもできる。このpJRDTrc1は、図1に示したように、市販のpTrc99AとpJRD215 とを組み合わせて構築した新規ベクターであり、そのマルチクローニングサイトに前記のP(3HA)重合酵素遺伝子 phaCAC等を確実に連結することができる。 この発明の方法に使用する脂肪酸合成酵素遺伝子は、真核生物や微生物由来の公知の遺伝子である。例えば、大腸菌Escherichia coli 由来の脂肪酸合成酵素遺伝子 fab(Battner et al., Science 277:1453-1474, 1997 )、Bacillus subtilis 由来の脂肪酸合成酵素遺伝子 fab(Kunst et al., Nature 390:249-256, 1997)等であり、これらを単独もしくは複数組み合わせて使用することができる。
【0012】
このような脂肪酸合成酵素遺伝子(群)は、前記P(3HA)重合酵素遺伝子と同様に、公知の微生物用発現ベクターに組み込んで宿主細胞に導入することができる。
以上のとおりに構築したP(3HA)重合酵素遺伝子発現ベクターおよび脂肪酸合成酵素発現ベクターは、電気穿孔法、リン酸カルシウム法、リポソーム法、DEAEデキストラン法など公知の方法により同一の宿主微生物に導入する。そして、発現ベクター中の耐性遺伝子による薬剤耐性等を用いて両遺伝子により形質転換した微生物を単離することができる。
【0013】
このようにして作出した形質転換微生物を、炭素源存在下で、必要に応じて遺伝子の発現誘導処置を施すなどして増殖させることにより、微生物体内にP(3HA)を蓄積させることができる。炭素源は、グルコースやフラクトース等の糖類、または脂肪酸類を制限なく用いることができる。
蓄積されたP(3HA)は公知の方法により単離・精製することができる。例えば、大腸菌の場合には、培養液から遠心分離等により菌体を集め、これを凍結乾燥し、乾燥菌体を酸−メタノール分解し、分解物からクロロホルム抽出によってP(3HA)を単離することができる。そして、各種クロマトグラフィー等により精製することができる。
【0014】
以下、実施例を示し、この発明についてさらに詳細かつ具体的に説明するが、この発明は以下の例に限定されるものではない。
【0015】
【実施例】
実施例1
P(3HA)重合酵素遺伝子(Aeromonas caviae FA440 株由来の phaCAC遺伝子)をpJRDTrc1に組み込み、P(3HA)重合酵素遺伝子発現ベクターを構築した(図1)。一方、Escherichia coli HB101 株由来の脂肪酸合成酵素遺伝子 fabH、fabD、fabG、acpPおよびfabF遺伝子群を連続してpUC118 にクローニングし、このクローンから図2に示したように、fabHを含む断片、fabDを含む断片、および全遺伝子群を含む断片を切り出し、各々をpBluescriptII KS(+) に組み込んで脂肪酸合成酵素遺伝子発現ベクター(それぞれ、pXbH1.0 、pEEv1.6、pXbSac5.0 )を構築した。
【0016】
P(3HA)重合酵素遺伝子発現ベクターと脂肪酸合成酵素遺伝子のいずれかを組み合わせてEscherichia coli HB101 株に同時に導入し、形質転換大腸菌を得た。
これらの形質転換菌をLB(Luria−Bertani)培地で30℃で12時間培養した後、遺伝子発現誘導剤としてIPTG(Isopropyl−β−D(-) −thiogalactopyranoside )を最終濃度1mMになるように添加して4時間培養した。次いで、グルコース(最終濃度10 g/リットル)を添加し、さらに24時間培養した。
【0017】
培養終了後、培養液を遠心分離して菌体を集め、凍結乾燥し、乾燥菌体を酸−エタノール分解し、クロロホルム抽出した後、ガスクロマトグラフィーでP(3HA)の収量およびその組成比を検出した。
なお、比較対照として、 phaCAC遺伝子のみを導入した遺伝子組換え大腸菌についても同様に培養し、P(3HA)の有無を調べた。
【0018】
結果は表1に示したとおりである。P(3HA)重合酵素遺伝子と脂肪酸合成酵素遺伝子群とを導入した形質転換菌からは、モノマーユニットがR−3−ヒドロキシブタン酸:100 %の3HBホモポリマーが得られたのに対し、比較対象として試験した phaCAC遺伝子のみを導入した形質転換菌からはポリ−3−ヒドロキシアルカン酸は検出されなかった。また、3HBの収率は、 fabH、fabD、fabG、acpPおよびfabF遺伝子群を全て導入した菌が乾燥菌体重量当たり10.3%と最も高く、次いで、fabH(6.3 %)、fabD(4.6 %)であった。
【0019】
【表1】
【0020】
【発明の効果】
以上詳しく説明したとおり、この出願によって、P(3HA)の遺伝子工学的手法による製造方法と、この製造方法に用いる遺伝子組換え生物が提供される。これらの発明によって、高純度のポリ−3−ヒドロキシアルカン酸を簡便かつ大量に、しかも安価に製造することが可能となる。
【図面の簡単な説明】
【図1】この発明に用いることのできるpJRDTrc1の構成を示した模式図である。
【図2】実施例で構築した脂肪酸合成酵素遺伝子発現ベクターの挿入遺伝子の関係を示した模式図である。[0001]
BACKGROUND OF THE INVENTION
This application relates to a method for producing poly-3-hydroxyalkanoic acid and a genetically modified organism that produces this poly-3-hydroxyalkanoic acid in large quantities. More specifically, this application relates to a method for producing high-purity poly-3-hydroxyalkanoic acid useful as an alternative plastic and the like in a simple and large amount at low cost, and a novel organism used in this method.
[0002]
[Prior art]
Poly-3-hydroxyalkanoic acid (hereinafter sometimes referred to as “P (3HA)”) is a general term for compounds in which two or more of 3-hydroxyalkanoic acids are polymerized by an ester bond or the like. Examples include 3-hydroxybutanoic acid and poly-3-hydroxyhexanoic acid.
[0003]
In recent years, P (3HA) has been promising for use in alternative plastics and the like. However, since production by chemical synthesis is costly, a genetic engineering production method using a bioreactor or the like is being studied.
In the production of P (3HA) by this genetic engineering method, the host organism is transformed by introducing a P (3HA) polymerase enzyme gene derived from another organism into a host organism such as E. coli that does not accumulate P (3HA). An attempt has been made to cultivate this transformant in a medium containing a carbon source such as glucose. This is because it is considered that P (3HA) non-accumulating organisms such as E. coli do not accumulate P (3HA) because they do not produce the polymerization enzyme.
[0004]
However, since the ability to accumulate P (3HA) in the transformant cannot be increased only by introducing a polymerization enzyme gene into a P (3HA) non-accumulating organism, the non-accumulation of P (3HA) in E. coli and the like is It is speculated that this is due not only to the fact that the organism does not produce P (3HA) polymerizing enzyme, but also because the ability to produce 3-hydroxyacyl CoA, which is a substrate for poly-3-hydroxyalkanoic acid polymerizing enzyme, is extremely low. ing. Thus, it has been reported that a fatty acid synthase gene for promoting the production of 3-hydroxyacyl CoA together with a P (3HA) polymerase enzyme gene is introduced into a host organism (Williams et al .: Protein Expr. Purif. 7: 203-211, 1996). In this conventional method, a mutant gene of fatty acid synthase derived from rat and a poly-3-hydroxyalkanoic acid polymerase enzyme gene derived from Alcaligenes eutrophus are introduced into insect (Spodoptera frugiperda) cells and cultured in insect cell culture medium for 3 days. As a result, 600 mg of dried cells and 1 mg of poly-3-hydroxyalkanoic acid were successfully obtained per liter of medium.
[0005]
[Problems to be solved by the invention]
However, in the conventional method such as Williams et al., The obtained P (3HA) is very small amount of 0.17% per dry cell weight and is not suitable for mass production on an industrial scale. In addition, since the host organism is an insect cell, there is a problem that a special technique is required for the culture.
[0006]
The invention of this application has been made in view of the circumstances as described above, and solves the problems of the conventional method, and can produce high-purity P (3HA) simply, in large quantities, and at low cost. It is an object of the present invention to provide a new P (3HA) production method.
Another object of the invention of this application is to provide a genetically modified organism used in this production method.
[0007]
[Means for Solving the Problems]
As an invention for solving the above-mentioned problems, this application firstly includes a poly-3-hydroxyalkanoic acid synthase gene and a microorganism-derived fatty acid synthase gene fabH , fab D, fab G, acpP , fab F. Characterized in that one or more of the above are introduced into E. coli and transformed, the transformed E. coli is grown in the presence of a carbon source, and poly-3-hydroxyalkanoic acid is isolated and purified from the grown E. coli. Secondly, a poly-3-hydroxyalkanoic acid synthase gene and a microorganism-derived fatty acid synthase gene fabH , fab D, fab G, acpP and fab F A poly-3-hydride which is transformed by introducing it into the E. coli, grown in the presence of a carbon source, and isolated and purified poly-3-hydroxyalkanoic acid from the grown E. coli The manufacturing method of Kishiarukan acid, the third, the microorganism to provide the first or second manufacturing method is Escherichia coli.
[0008]
Also this application, the fourth, E. coli poly-3 and hydroxyalkanoic acid synthase gene, derived from a microorganism of the fatty acid synthase gene fabH, fab D, fab G, acpP, one or more of the fab F Fifth, the transformed Escherichia coli produced by introduction into a poly-3-hydroxyalkanoic acid synthase gene and a fatty acid synthase gene fabH , fab D, fab G, acpP and fab F derived from microorganisms Sixth, the transformed E. coli produced by introduction into E. coli is provided as the fourth or fifth transformed E. coli wherein the microorganism is E. coli.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
As the P (3HA) polymerase enzyme gene used in the method of the present invention, genes derived from various P (3HA) accumulating organisms can be used. Such genes include, for example, the P (3HA) polymerase enzyme gene phaCAC (Fukui et al., J. Bacteriol. 179: 4821-4830, 1997) derived from Aeromonas caviae and the P (3HA) polymerase enzyme gene derived from Alcaligenes eutrophus. phbCAe (Peoples et al., J. Biol. Chem. 262: 15298-15303, 1989), Pseudomonas aeruginosa-derived polymerase enzyme gene phaC1Pa (Timm et al., Eur. J. Biochem. 209: 15-30, 1992) Etc.
[0011]
Alternatively, using these known genes as probes, a P (3HA) polymerase enzyme gene isolated from genomic DNA of an arbitrary species can also be used.
These P (3HA) polymerase enzyme genes can be incorporated into an expression vector for microorganisms, and a transformed microorganism can be produced by introducing the recombinant vector into a microorganism such as Escherichia coli according to a standard method. Expression vectors include known microorganism expression vectors having origins, promoters, ribosome binding sites, gene cloning sites, terminators, etc. that can be replicated in microorganisms (for example, pUC systems, pBluescript II, pET expression are used as expression vectors for E. coli). System, pGEX expression system) and the like. In addition, the plasmid vector pJRDDTrc1 (FIG. 1) newly constructed by the inventors of this application can also be used. As shown in FIG. 1, this pJRDTrc1 is a novel vector constructed by combining commercially available pTrc99A and pJRD215, and the P (3HA) polymerase gene phaCAC and the like are surely linked to the multicloning site. Can do. The fatty acid synthase gene used in the method of the present invention is a known gene derived from a eukaryote or a microorganism. For example, a fatty acid synthase gene fab (Battner et al., Science 277: 1453-1474, 1997) derived from Escherichia coli, a fatty acid synthase gene fab derived from Bacillus subtilis (Kunst et al., Nature 390: 249-256, 1997), etc., and these can be used alone or in combination.
[0012]
Such a fatty acid synthase gene (s) can be incorporated into a known microorganism expression vector and introduced into a host cell in the same manner as the P (3HA) polymerase enzyme gene.
The P (3HA) polymerase enzyme expression vector and the fatty acid synthase expression vector constructed as described above are introduced into the same host microorganism by known methods such as electroporation, calcium phosphate method, liposome method, DEAE dextran method. Then, a microorganism transformed with both genes can be isolated using drug resistance by the resistance gene in the expression vector.
[0013]
P (3HA) can be accumulated in the microorganism body by growing the transformed microorganism produced in this manner in the presence of a carbon source, for example, by performing gene expression induction treatment as necessary. As the carbon source, saccharides such as glucose and fructose, or fatty acids can be used without limitation.
The accumulated P (3HA) can be isolated and purified by a known method. For example, in the case of Escherichia coli, cells are collected from the culture solution by centrifugation or the like, lyophilized, the dried cells are acid-methanol decomposed, and P (3HA) is isolated from the decomposed product by chloroform extraction. be able to. And it can refine | purify by various chromatography etc.
[0014]
Examples Hereinafter, the present invention will be described in more detail and specifically, but the present invention is not limited to the following examples.
[0015]
【Example】
Example 1
A P (3HA) polymerase enzyme gene (phaCAC gene derived from Aeromonas caviae FA440 strain) was incorporated into pJRDDTrc1 to construct a P (3HA) polymerase enzyme expression vector (FIG. 1). On the other hand, the fatty acid synthase genes fabH, fabD, fabG, acpP, and fabF genes derived from Escherichia coli HB101 were successively cloned into pUC118. As shown in FIG. 2, a fragment containing fabH, fabD, was cloned from this clone. A fragment containing the entire gene group and a fragment containing the entire gene group were cut out and incorporated into pBluescriptII KS (+) to construct fatty acid synthase gene expression vectors (pXbH1.0, pEEv1.6 and pXbSac5.0, respectively).
[0016]
Either a P (3HA) polymerase enzyme expression vector and a fatty acid synthase gene were combined and introduced into Escherichia coli HB101 strain at the same time to obtain transformed Escherichia coli.
After culturing these transformed bacteria in LB (Luria-Bertani) medium at 30 ° C. for 12 hours, IPTG (Isopropyl-β-D (−)-thiogalactopyranoside) as a gene expression inducer was added to a final concentration of 1 mM. And cultured for 4 hours. Glucose (final concentration 10 g / liter) was then added and further cultured for 24 hours.
[0017]
After completion of the culture, the culture solution is centrifuged to collect the cells, freeze-dried, the dried cells are digested with acid-ethanol, extracted with chloroform, and then the yield of P (3HA) and its composition ratio are determined by gas chromatography. Detected.
As a comparative control, a recombinant E. coli into which only the phaCAC gene was introduced was also cultured in the same manner and examined for the presence of P (3HA).
[0018]
The results are as shown in Table 1. From the transformed bacterium introduced with P (3HA) polymerizing enzyme gene and fatty acid synthase gene group, 3HB homopolymer with a monomer unit of R-3-hydroxybutanoic acid: 100% was obtained. No poly-3-hydroxyalkanoic acid was detected from the transformed bacterium introduced with only the phaCAC gene. In addition, the yield of 3HB was the highest at 10.3% per dry cell weight with all of the fabH, fabD, fabG, acpP and fabF gene groups introduced, followed by fabH (6.3%) and fabD (4.6%). there were.
[0019]
[Table 1]
[0020]
【The invention's effect】
As described in detail above, this application provides a method for producing P (3HA) by genetic engineering techniques and a genetically modified organism used in this production method. These inventions make it possible to produce high-purity poly-3-hydroxyalkanoic acid simply, in large quantities, and at low cost.
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing the structure of pJRDDTrc1 that can be used in the present invention.
FIG. 2 is a schematic diagram showing the relationship of inserted genes of the fatty acid synthase gene expression vector constructed in Example.
Claims (6)
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26879198A JP4258577B2 (en) | 1998-09-22 | 1998-09-22 | Process for producing poly-3-hydroxyalkanoic acid |
| PCT/JP1999/005185 WO2000017340A1 (en) | 1998-09-22 | 1999-09-22 | Process for producing poly-3-hydroxyalkanoic acid |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26879198A JP4258577B2 (en) | 1998-09-22 | 1998-09-22 | Process for producing poly-3-hydroxyalkanoic acid |
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| JP2000135083A JP2000135083A (en) | 2000-05-16 |
| JP4258577B2 true JP4258577B2 (en) | 2009-04-30 |
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| JP26879198A Expired - Fee Related JP4258577B2 (en) | 1998-09-22 | 1998-09-22 | Process for producing poly-3-hydroxyalkanoic acid |
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| WO (1) | WO2000017340A1 (en) |
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| EP1785444B1 (en) | 2004-08-31 | 2015-02-25 | Riken | Method for producing a biopolyester with thermal stability |
| WO2006101176A1 (en) * | 2005-03-24 | 2006-09-28 | Kaneka Corporation | Microorganism capable of accumulating ultra high molecular weight polyester |
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| JPH0644875B2 (en) * | 1986-08-26 | 1994-06-15 | 日本化薬株式会社 | Method for producing recombinant gene product |
| JPH03272680A (en) * | 1990-03-20 | 1991-12-04 | Res Assoc Util Of Light Oil | Method for culturing genetic recombinant strain |
| US6600029B1 (en) * | 1995-12-19 | 2003-07-29 | Regents Of The University Of Minnesota | Metabolic engineering of polyhydroxyalkanoate monomer synthases |
| JPH11276180A (en) * | 1998-03-31 | 1999-10-12 | Rikagaku Kenkyusho | Plant having polyester synthetic ability and method for producing polyester |
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| WO2000017340A1 (en) | 2000-03-30 |
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