CA1105860A - Process for the production of coenzyme q - Google Patents

Process for the production of coenzyme q

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Publication number
CA1105860A
CA1105860A CA310,399A CA310399A CA1105860A CA 1105860 A CA1105860 A CA 1105860A CA 310399 A CA310399 A CA 310399A CA 1105860 A CA1105860 A CA 1105860A
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Prior art keywords
coenzyme
grams
pseudomonas
atcc
acetate
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CA310,399A
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French (fr)
Inventor
Ko Aida
Kinya Uchida
Izumi Kawada
Hideichi Itoh
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Individual
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Individual
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Priority claimed from JP10593977A external-priority patent/JPS5455787A/en
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/66Preparation of oxygen-containing organic compounds containing the quinoid structure

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  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

ABSTRACT OF THE DISCLOSURE

A process for producing Coenzyme Q which comprises cultivating a microorganism belonging to genus Pseudomonas in a culture medium to which at least one member selected from the group consisting of isopentenyl alcohol (3-methyl-3-butene-1-ol), dimethyl allyl alcohol (3-methyl-2-butene-1-ol), geraniol, isopentenyl acetate, dimethyl allyl acetate, geranyl acetate and .beta.-methyl crotonic acid is added, and obtaining thus formed Coenzyme Q.

Description

~1~5~60 1 BACKGRO~ND OF THE INVENTION
... .
1. Field of the Invention -The present invention relates to a process for the production of Coenzyme Q. More particularly, it is concerned with a process for the production of Coenzyme Q which comprises cultivating a microorganism belonging to genus Pseudomonas in a culture medium to which at least one member selected from the group consisting of isopentenyl alcohol, dimethyl allyl alcohol, geraniol, isopentenyl acetate, dimethyl allyl acetate, geranyl acetate and ~ -methyl crotonic acid is added to form Coenzyme Q
and obtaining it.
The temm "Coenzyme Q" used in the present invention is generally meant 2,3-dimethoxy-5-methyl-1,4-benzoquinones con-taining an isoprene side chain in the 6-position of the quinone nucleus represented by the general formula, O
H3CO~ CH3 H3COJ~CH2-CH= lC - CH ~tnH

The present invention is intended to provide Coenzyme Q repre-sented by the above formula in which n=8,9 and 10, respectively;
that is Coenzyme Q8' Coenzyme Qg and Coenzyme Q1o.
Coenzyme Q is widely distributed in animals, plants and microorganisms etc., and it plays an important role as a con-stitutive element of the terminal electron transfer system.
2. Explanation of the Prior Art Recently it has been clarified that Coenzyme Q exhibits excellent medical and physiological activities to various diseases. In particular, Coenzyme 21o is considered most valuable ''~s s~
as a medicine since Coenzyme Q of human being is Coenzyme Qlo.
It can be considered that the way of obtaining Coenzyme Q is to extract from the animal and plant tissue, or microorgan-isms, and to synthesize chemically. It is, however, difficult to produce Coenzyme Q by extracting from the animal or plant tissue on a large scale. Also, it is difficult to produce Coenzyme Q by organic synthesis because of a disadvantage in yields. Thus these procedures are not satisfactory for industrial ones. On the other hand, the procedure to extract from micro-organisms has the possibility of being employed economically according to the yields of the cells and Coenzyme Q.
It is known that microorganisms belonging to genus Pseudomonas produce Coenzyme Q8' Qg and Qlo Thus we searched the compounds that were able to marked-ly increase the content of Coenzyme Q per unit cell when they were added to the culture medium in comparison with the case that they were not added. P-hydroxy benzoic acid, and acetic acid and its salts are known to be able to increase the content of Coenzyme Q
per unit cell when added to the culture medium (Japanese Patent Publication No. 20396/72). It is known that the isoprene side chain of Coenzyme Q lS produced through geranyl- and farnesyl ~;~ pyrophosphate by the biosynthesis in which the condensation of isopentenyl- and dimethyl allyl pyrophosphate is repeated. However, since these precursors are difficult to permeate through the cell membrane, no attempt to make increase the content o Coenzyme Q
by adding such precursors to the culture medium has been reported~
SUMMARY OF THE INVENTION
The present invention provides a process for producing Coenzyme Q which comprises cultivating microorganisms belonging to genus Pseudomonas in a culture medium to which at least one .~

5~

1 member selec~ed from the group consisting of isopentenyl alcohol, dimethyl allyl alcohol, geraniol, isopentenyl acetate, dimethyl allyl acetate, geranyl acetate and ~ -methyl crotonic acid is added, to produce Coenzyme Q and obtaining it.
In the present invention, the term "Coenzyme Q" means Coenzyme Q8' Qg and Qlo, which are thought to be important from the industrial standpoint.
DETAILED DESCRIPTION OF THE INVENTION
We found that isopentenyl alcohol, dimethyl allyl alcohol, geraniol, isopentenyl acetate, dimethyl allyl acetate, geranyl acetate, and ~-methyl crotonic acid were easily utiliæed by the microorganisms belonging to genus Pseudomonas when added to the culture medium and that they were able to markedly increase the content of Coenzyme Q per unit cell.
Any of microorganisms belonging to genus Pseudomonas and capable of producing Coenzyme Q, can be employed in the present invention. For example, these microorganisms capable of producing Coenzyme Qlo include Pseudomonas diminuta ATCC 11568 (IAM-1513), etc., those capable of producing Coenz~me ~9 include 20 Pseudomonas schuylkilliensis ATCC 31419 (IAM-1126), Pseudomonas denitrificans ATCC 13867 (I~-12023), Pseudomonas olevorans ATCC 8062 (IAM-150~), Pseudomonas putrefaciens ATCC 8071 (IAM-1509) etc., and those capable of producing Coenzyme Q8 include Pseudomonas rubescens ATCC 12099 (IAM-1510), Pseudomonas fulva ATCC 31418 (IAM-1529), Pseudomonas putida ATCC 4359 (IAM-1506) etc.
In the culture medium used in practice of the present invention, sugars such as glucose, molasses, etc., and any other carbon sources with which these microorganisms are able to utilize, can be used as carbon sources. Inorganic nitrogen compounds such
-3-v ~
. .

., , ;

s~
1 as ammonium su~fate, ammonium chloride and the like, organic nitrogen compounds such as corn steep liquor, e~tracts of fish meat, peptone, yeast extract, and the like, etc., can be usea as nitrogen sources. In addition, as inorganic salts, potassium salts, sodium salts, magnesium salts, salts of phosphoric acid and sulfuric acid and the like, are employed.
The cultivation is usually carried out by agitation with air under the condition of pH 4 to 8, temperature 25 to 35C and period 10 to 50 hours.

The addition of isopentenyl alcohol, dimethyl allyl alcohol) geraniol, isopentenyl acetate, dimethyl allyl acetate, geranyl acetate and ~ -methyl crotonic acid according to the present invention can be carried out by a desired procedure and desired time. For example, all amounts of the additive are added at the start Or at a desired growth stage during the cultivation, or it is added little by little according to the state of ferment--~ ation. Further, the additive can be used singly or in combination with the other additives. The amount of the additive being added is usually 1 x 10 5 ~o 5 x 10 3 mole/liter (as a final concentra-tion~, preferably 5 x 10 5 to 5 x 10 4 mole/liter.
After the cultivation, Coenzyme Q formed is extracted from the cells and separated from other materials. For example, the wet cells obtained by centrifugation are extracted with hydrophilic solvent such as acetone and the like; Coenzyme Q-containing fraction is then transferred into a solvent such as petroleum ether and the like; and the Coenzyme Q-containing fraction is subjected to fractional purification by use of alumina column, etc., whereby Coenzyme Q can be isolated.
In the present invention, the identlfication of Coenzyme Q is conducted by comparing the product of this invention with ~s~

1 a standard sample by means of W spectrum, measurement of melting point and reversed phase thin layer chromatography in which a mixture of acetone:water (9~:5) is used as a solvent, and others.
The following examples are given to explain the present invention in more detail, but the present invention is not limited by them.
Example 1 In a 30 liter-jar fermentor was placed 15 liters of a culture medium (pH 7.0) containing 0.05~ of KH2P04, 0.15% of Na2HP04, 0.05% of MgSO4 7H20, 1% of glucose, 1% of peptone and 0.2~ of yeast extract. After sterilized with steam, 645 milli-grams of isopentenyl alcohol dissolved in 10 milliliters of ethanol was added. Pseudomonas schuylkilliensis ATCC 31419 (IAM-1126), which had been previously cultured in 500 milliliters of the culture medium havin~ the same composition as described above for 2~ hours, was inoculated in the above culture medium and cultured ~or 24 hours with aeration of 15 liter/minute at 27C.
After the cultivation, the culture broth was centrifuged whereby 418 grams of wet cells (87 grams as dry cells) were obtained.
To the wet cells was added 2 liters of acetone, and the extraction was made with stirring. Then the cells were separated by centrifugation. This procedure was repeated two times more.
The acetone extracts were combined together and condensed under reduced pressure to distill away the acetone. Thereafter the remaining solution was extracted three times with each 1 liter of petroleum ether respectively and the resulting petroleum ether layers were combined. The combined petroleum ether layer was washed with water, dried over and condensed under reduced pressure.
; 3~ The residual oil was dissolved in a small amount of petroleum ,~
-5- ~

~$~
1 ether and subjected to alumina ~olumn chromatography by eluting with a mixture of petroleum ether and ethyl ether. The solvent was dis~illed away from the above obtained eluate containing Coenzyme Q. The residual oil was dissolved in a small amount of ethanol and allowed to stand in a refrigerator whereby crystals of Coenzyme Qg were appeared. These crystals were recrystalyzed from ethanol three times and 142.6 milligrams of crystals of Coenzyme Qg were obtained.
On the other hand, the same cultivation as above was conducted by use of 15 liters of a culture medium to which no isopentenyl alcohol was added. In the same manner as above, 359 grams of wet cells (69 grams as dry cells) were obtained. Further the same procedure as above was applied whereby 81.42 milligrams of crystals of Coenzyme Qg were obtained.
Based upon the above data, the effect of isopentenyl alcohol on the production of Coenzyme Qg was calculated. The addition of isopentenyl alcohol to the culture broth increased the yield of Coenzyme Qg per liter of the broth by 75%, and by 39% per gram of dry cells. Thus it was clearly confirmed that the addition of isopentenyl alcohol was effective to increase the yield of Coenzyme Qg.
Example 2 The procedure o~ Example 1 was followed except that 1.16 grams of geraniol was used in place of isopentenyl alcohol, and 390 milligrams of wet cells (68 grams as dry cells) were obtained.
The wet cells were subjected to the same procedure as described in Example 1, and 104.7 milligrams of crystals of Coenzyme Qg were obtained.
On the other hand, the same microorganism was cultivated by use of the culture medium to which no geraniol was added, and ~5~
1 327 grams of wet cells (63 grams as dry cells) were obtained.
From th~ cells 74.3 milligrams of crystals of Coenzyme Q9 were obtained.
Based upon thè above data, the effèct of geraniol on the production of Coenzyme Qg was compared. The addition of geraniol to the culture medium increased the yield of Coenzyme Qg per liter of the culture broth by 41% and by 30% per gram of the dry cells.
Example 3 Pseudomonas rubescens ATCC 12099 (IAM-1510) was cultivated in the same culture medium and in the same manner as described in Example ~, and 410 grams of wet cells (73 grams as dry cells) were obtained. These were treated in the same manner as describe~ in Example 1 and 58.4 milligrams of Coenzyme Q8 were obtained.

On the other hand, the same microorganism was cultivated in the same culture medium as above except that no geraniol was added, and 390 grams of wet cells (74 grams as dry cells) were obtained. From the cells, 44.4 milligrams of Coenzyme Q8 were obtained.

Based upon the above data, the same comparison as in Example 1 was made. The addition of geraniol to a culture medium increasecl the yield of Coenzyme Q8 per liter of the culture broth by 32~ and 33% per gram of dry cells.
Example 4 Pseudomonas diminuta ATCC 11568 (IAM~1513) was culti-....
vated by the same procedure as in Example 1 except that sodiumacetate was used in place of glucose in the composition of the medium and three 300 milligrams fractions of isopentenyl alcohol were added separately (total amount 900 milligrams). Thus 380 grams o wet cells ~69 grams as dry cells) were obtained, which were then subjected to the same treatment as in Example 1, where-by 30.5 milllgrams of crystals of Coenzyme Qlo were obtained.
On the other hand, the same microorganism was cultivated in the culture medium to which no isopentenyl alcohol was added, and 320 grams of wet cells (61 grams as dry cells) were obtained, from which 19.8 milligrams of crystals of Coenzyme Qlo were obtained.
Based upon the above data, the same comparison as Example 1 was made. The addition of isopen~enyl alcohol increased the yield of Coenzyme Qlo per liter of the culture broth by 54%
and 38% per gram of dry cells.
Example 5 The procedure of Example 1 was followed except that Pseudomonas denitrificans ATCC 13867 (IAM-12023) was used as ~ . . .
microorganism and that two 1 gram portions of geraniol were added separately to the culture medium (total 2 grams) at different times of cultivation. Thus 395 grams of wet cells (76 grams as dry cells) were obtained, which was then subjected to the same treatment as in Example 1, whereby 63.1 milligrams of crystals of Coenzyme Qg were obtained.
On the other hand, the same microorganism was culti-vated in the culture medium to which no geraniol was added, and 328 grams of wet cells (63 grams as dry cells) were obtained, from which 37.2 milligrams of crystals of Coenzyme Q9 were obtained.
Based upon the above data, the same comparison as in Example 1 was made. The addition of geraniol increased the yield of Coenzyme Qg per liter of the culture broth by 69% and by 41% per gram of dry cells.

30~

~S~ ~
1 Exam21e 6 The procedure of Example 1 was followed except that Pseudomonas fulva ATCC 31~18 (IAM-1529) was used as microorganism :
and that three portions of isopentenyl alcohol (total 3 grams) were separately added at different times of cultivation. Thus 390 grams of wet cells (73 grams as dry cells) were obtained, which were then subjected to the same treatment as in Example 1, whereby 86.4 milligrams of crystals of Coenzyme Q8 were obtained.
On the other hand, the same microorganism was cultivated in the culture medium to which no isopentenyl alcohol was added and 350 grams of wet cells (67 grams as dry cells) were obtained, from which 60.S milligrams crystals of Coenzyme Q8 were obtained.
Based upon the above data, the same comparison as in Example 1 was made. The addition of isopentenyl alcohol increased the yield of Coenzyme Q8 per liter of the culture broth by 43%
and by 31% per gram of dry cells.
Example 7 The procedure of Example 1 was followed except that Pseudomonas ru~escens ATCC 12099 (IAM-1510) was used as micro-organism and that 645 milligrams of dimethyl allyl alcohol was added. Thus 430 grams of wet cells (80 grams as dry cells) were obtained, which were subjected to the same treatment as Example 1, whereby 86 milligrams of crystals of Coenzyme Q8 were obtained.
On the other hand, the same microorganism was culti-vated in the culture medium to which no dimethyl allyl alcohol was added and 390 grams of wet cells (76 grams as dry cells) were obtained, from which 68 milligrams of crystals of Coenzyme Q8 were obtained.
- Based upon the above data, the same comparison as Example 1 was made. By the addition of dimethyl allyl alcohol ~s~
1 the yield of Coenzyme Q8 per liter of the culture broth was increased by 26~ and by 20~ per gram of dry cells.
Exam~le 8 The procedure of Example 1 was followed except that Pseudomonas fulva ATCC 31418 (IAM-1529) was used as microorganism and that 750 milligrams of ~ -methyl crotonic acid was added.
Thus 540 grams of wet cells (105 grams as dry cells) were obtained, which were subjected to the same treatment as Example 1, whereby 102 milligrams of crystals of Coenzyme Q8 were obtained.

On the other hand, the same microorganism was culti-vated in the culture medium to which no ~ ~methyl crotonic acid is added and 525 grams of wet sells (103 grams as dry cells) were obtained, from which 79 milligrams of crystals of Coe~zyme Q8 were obtained.
Based upon the above data, the same comparison as in Example 1 was made. The addition of ~-methyl crotonic acid increased the yield of Coenzyme Q8 per liter of the culture broth by 28~ and by 26% per gram of dry cells.
Example 9 The procedure of Example 1 was followed except that Pseudomonas olevorans ATCC 8062 (IAM-1508) was used as microorgan~
ism and that 960 milligrams of dimethyl allyl acetate was added.
Thus 490 grams of wet cells (94 grams as dry cells) were obtained, which were subjected to the same treatment as Example 1, whereby 96 milligrams of crystals of Coenzyme Qg were obtained.
Gn the other hand, the same microorganism was cultivated i in the culture medium to which no dimethyl allyl acetate was added ; and 470 grams of wet cells t90 grams as dry cells) were obtained, from which 68 milligrams of crystals of Coenzyme Qg were obtained.
Based upon the above data, the same comparison as Example ~580 1 1 was made. The addition of dimethyl allyl acetate increased the yield of Coenzyme Qg per liter of the culture broth by 42~ and by 34% per gram of dry cells.
Example 10 The procedure of Example 1 was followed except that Pseudomonas schuylkilliensis ATCC 31419 ~IAM-1126) was used as _ . .
the microorganism and that 1.47 grams of geranyl acetate was added. Thus, 530 grams of wet cells (93 grams as dry cells) were obtained, which were subjected to the same treatment as Example 1, whereby 120 milligrams of crystals of Coenzyme Qg were obtained.
On the other hand, the same microorganism was cultivated in the culture medium to which no geranyl acetate was added and 525 grams of wet cells (90 grams as dry cells) were ~btained, from which 98 grams of crystals of Coenzyme Qg were obtained.
Based upon the above data, the same comparison as Example 1 was made. The addition of geranyl acetate increased the yield of Coenzyme Qg per liter of culture broth by 23% and by 19~ per gram of dry cells.
Example 11 The procedure of Example 1 was followed except that `~
Pseudomonas denitrificans ATCC 13867 (IAM~12~23) was used as microorganism and that the mixture of 960 milligrams of isopen-tenyl acetate and l.47 grams of geranyl acetate was added. Thus 480 grams of wet cells (96 grams as dry cells) were obtained, which were subjected to the same treatment as Example 1, whereby 115 milligrams of crystals of Coenzyme ~ wer~ obtained.
On the other hand, the same microorganism was cultivated in the culture medium to which the mixture was not added and 490 gxams of wet cells (98 grams as dry cells) were obtained, from which 76 milligrams of crystals of Coenzyme Qg were obtained.
-~51~

1 ~ased upon the above data, the same comparison as Example 1 was made. The addition of isopentenyl acetate and geranyl acetate increased the yield of Coenzyme Q~ per liter of the culture broth by 51% and by 54% per gram of dry cells.
Example 12 Pseudomonas diminuta ATCC 11568 (IAM-1513) was culti-.
vated by the same procedure as in Example 4 except that the mixture of 960 milligrams of isopentenyl acetate and 960 milli-grams of dimethyl allyl acetate was added. Thus 495 grams of wet cells (98 grams as dry cells) were obtained, which were subjected to the same treatment as Example 1, whereby 53 milligrams of crystals of Coenzyme Qlo were obtained.

On the other hand, the same microorganism was cultivated in the culture medium to which the mixture was not added. Thus 480 grams of wet cells (94 grams as dry cells) were obtained, from which 39 milligrams of crystals of Coenzyme Qlo were obtained.
Based upon the above data, the same comparison as Example 1 was made. The addition of isopentenyl acetate and dimethyl allyl acetate increased the yield of Coenzyme Qlo per liter of culture broth by 36~ and by 32% per gram of dry cells.

.

Claims (4)

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
1. A process for producing Coenzyme Q which comprises cultivating a microorganism belonging to genus Pseudomonas, capable of producing Coenzyme Q, in a culture medium to which at least one member selected from the group consisting of isopentenyl alcohol, dimethyl allyl alcohol, geraniol, isopentenyl acetate, dimethyl allyl acetate, geranyl acetate and .beta.-methyl crotonic acid is added and thereby obtaining Coenzyme Q produced.
2. A process for producing Coenzyme Q as in claim 1, wherein the microorganism is Pseudomonas diminuta ATCC 11568, and Coenzyme Q produced is Coenzyme Q10.
3. A process for producing Coenzyme Q as in claim 1, wherein the microorganism is Pseudomonas schuylkilliensis ATCC 31419, Pseudomonas dentrificans ATCC 13867 or Pseudomonas olevorans ATCC 8062, and Coenzyme Q produced is Coenzyme Q9.
4. A process for producing Coenzyme Q as in claim 1, wherein the microorganism is Pseudomonas rubescens ATCC 12099 or Pseudomonas fulva ATCC 31418, and Coenzyme Q produced is Coenzyme Q8.
CA310,399A 1977-09-05 1978-08-31 Process for the production of coenzyme q Expired CA1105860A (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP105939/1977 1977-09-05
JP10593977A JPS5455787A (en) 1977-09-05 1977-09-05 Production of coenzyme q
JP40812/1978 1978-04-08
JP4081278 1978-04-08

Publications (1)

Publication Number Publication Date
CA1105860A true CA1105860A (en) 1981-07-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
CA310,399A Expired CA1105860A (en) 1977-09-05 1978-08-31 Process for the production of coenzyme q

Country Status (9)

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CA (1) CA1105860A (en)
CH (1) CH645607A5 (en)
DE (1) DE2838252C3 (en)
DK (1) DK147602C (en)
ES (1) ES473041A1 (en)
FR (1) FR2401993A1 (en)
GB (1) GB2005662B (en)
IT (1) IT1157168B (en)
NL (1) NL7808778A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1223794B (en) * 1958-12-29 1966-09-01 Merck & Co Inc Process for obtaining coenzyme Q-10 from microorganisms

Also Published As

Publication number Publication date
GB2005662B (en) 1982-03-17
DE2838252B2 (en) 1980-07-17
FR2401993B1 (en) 1981-09-04
DK389078A (en) 1979-03-06
IT1157168B (en) 1987-02-11
DE2838252C3 (en) 1981-09-24
GB2005662A (en) 1979-04-25
DK147602B (en) 1984-10-15
DK147602C (en) 1985-04-22
FR2401993A1 (en) 1979-03-30
DE2838252A1 (en) 1979-03-15
ES473041A1 (en) 1979-04-01
IT7850934A0 (en) 1978-09-01
CH645607A5 (en) 1984-10-15
NL7808778A (en) 1979-03-07

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