GB2058107A - Heteropolysaccharide S-130 - Google Patents
Heteropolysaccharide S-130 Download PDFInfo
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- GB2058107A GB2058107A GB8028286A GB8028286A GB2058107A GB 2058107 A GB2058107 A GB 2058107A GB 8028286 A GB8028286 A GB 8028286A GB 8028286 A GB8028286 A GB 8028286A GB 2058107 A GB2058107 A GB 2058107A
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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
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
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Abstract
A new heteropolysaccharide S-130 is prepared by fermentation of an unnamed Alcaligenes species, ATCC 31555. The polysaccharide has valuable properties as a thickening, suspending and stabilizing agent in aqueous systems e.g. food preparations and drilling muds. Its chemical composition is within the following weight ranges of sugars: 10-20% glucuronic acid; 10-25% mannose; 20-40% glucose; 30-60% rhamnose; the polymer also contains 3-5% acetyl groups.
Description
SPECIFICATION
Heteropolysaccharide S-130 BACKGROUND OF THE INVENTION
Compound S-130 may be prepared by fermentation of a suitable nutrient medium with a hitherto undescribed organism, based on extensive taxonomic studies, which is an unnamed Alcaligens species. An unrestricted permanent deposit of this organism employed in making our heteropolysaccharide was made with the American Type Culture Collection on August 1979 under Accession No. ATCC 31555.
The following considerations make the assignment of a new Alcaligenes species justified and necessary.
DESCRIPTION OF THE STRAIN
A. Characteristics of Colonial Morphology
On nutrient agar, small yellow colonies appear in one day at 30"C within the diameter reaching about 1.5 mm after 5 days' incubation. The colonies are round, smooth, convex, mucoid, and opaque. The yellow color becomes more deep and the texture of colonies becomes hard after prolonged incubation.
On YM agar, small mucoid yellow colonies appear in one day and the diameter reaches about 3 mm after 5 days' incubation. The colonies are round, smooth, convex, and opaque, but the top of the colonies are flat.
No embraneous hard texture is observed.
B. Characteristics of Cell Morphology
Strain S-130 is a gram-negative rod-shaped bacterium. On nutrient agarthe average size of the cell is about 0.5-0.6 by 1.2-1.6 ttm; ends of the cells are tapered and curvature was often seen. The size and shape of the cells do not change significantly after prolonged incubation.
On YM agar the average cell size is 0.6-0.8 by 1.6-2.0 ttm, but the cell becomes longer (3-4 ttm); accumulation of PHB is significant. Motility is positive. Flagella stains (modified silver nitrate method) show that the strain has mixed flagellation, i.e., polar and lateral flagella, as well as peritrichous flagella.
C. Physiological and Biochemical Characteristics
The following are results of tests employed:
Cytochrome oxidase is weak or negative; catalase positive.
Organism is capable of growth at 37 and 41"C, but notat43 C.
Tolerance to 3.0% NaCI, but not to 6.5% NaCI.
Growth at pH between 5 and 12.
Aerobic acid but not gas was produced from various carbohydrates, such as:
D-xylose lactose
L-arabinose maltose
D-glucose melibiose
fructose sucrose
galactose trehalose
mannose raffinose
Litmus milk was reduced, but not peptonized.
ADH was positive, but not LDC, ODC, and PDA.
MR positive, but negative for VP, indole, and urease.
Esculin gelatin (weak) and Tween 80 (weak) were hydrolyzed, but not casein, starch, cellulose, pectin.
No phosphatase, and haemolysis negative.
0.1% triphenyltetrazolium chloride was not inhibitory.
Survival at 60"C for 30 minutes.
Organisms grow on EMB agar and Tellurite Blood, but not on SS and MacConkey agar.
D. Antibiotic Susceptibility Test
The strain S-130 is susceptible to the following antibiotics: Kanamycin 30 g Neomycin ........................................ 30 Flg Chlortetrcycline ........................................ 5 g Novobiocin ........................................ 30 lig Erythromycin 15 frog Tetracycline t 30 ug Gentamicin ........................................ 10 9 Carbenicillin ........................................ .50 9 and not susceptible to::
Penicillin ........................................ 10 units
Streptomycin ...................................... 10 g
Colistin .......................................... 10 g
Polymyxin B ........................................ 300 units
E Nutritional Characteristics
Organic growth factors are not required and ammonium salts serve as the sole nitrogen source. A total of 30 organic compounds are utilized as sole source of carbon and energy. Most carbohydrates are utilized.
F. G+C Content ofthe DNA
No DNA analysis was performed.
G. Identification byAPlSystem The strain could not be identified by this system.
H. Identification
The strain S-130 is a gram-negative aerobic rod-shaped organism. The mode of flagellation of the organism is mixed; polar and peritrichous flagella (possibly degenerate flagella) are seen. According to
Bergey's Manual (8th Edition), such organisms belong as a member of the genusAlcaligenes.
TABLE 1
Biochemical and Other Miscellaneous Tests Employed for the Strain S-130
Oxidase: Kovac's + (weak) Hydrolysis of:
Pathotech + (weak) Gelatin + (weak)
Casein
Catalase + Starch
OF medium: Oxidative + Tween 80 + (weak)
Fermentative Pectin
Gas from glucose - Alginate NT
H2S production:TSI - Cellulose
from cystine + Chitin
Ammonium from peptone NT DNA NT ,8-Galactosidase (ONPG) + Esculin +
Arginine dihydrolase +
Lysine decarboxylase - Growth on various media:
Ornithine decarboxylase - EMB agar +
Tryptophan deaminase NT MacConkey agar
Phenylalanine deaminase - SS agar
Urease - Mannitol salt agar
Indole - TCBSagar MR test + Tinsdaletellurite VP test - blood agar +
Nitrate reduction - Pseudosel agar NT
Nitrite reduction
Denitrification NT Pigment production:
N2-fixation:King A medium
Growth in Burk's medium + King B medium
Nitrogenase activity NT Maionate (oxidation) - Dye reaction:
Phosphatase - Congo red
Haemolysis (sheep blood)
Litmus milk: acid, reduction only 3-ketolactose production
Survival at 60"C for 30 min. +
TSI: Slant Acid
Butt No growth
Gas
Egg Yolk Reaction + = positive
- = negative
NT = not tested
FERMENTATION CONDITIONS
Heteropolysaccharide S-130 is produced during the aerobic fermentation of suitable aqueous nutrient media under controlled conditions via inoculation with the organism of the unnamed Alcaligenes species.
The media are usual media, containing source of carbon, nitrogen and inorganic salts.
In general, carbohydrates (for example, glucose, fructose, maltose, sucrose, xylose, mannitol and the like) can be used either alone or in combination as sources of assimilable carbon in the nutrient medium. The exact quantity of the carbohydrate source or sources utilized in the medium depend in part upon the other ingredients of the medium but, in general, the amount of carbohydrate usually varies between about 2% and 4% by weight of the medium. Preferably 3% glucose is used. These carbon sources can be used individually, or several such carbon sources may be combined in the medium. In general, many proteinaceous materials may be used as nitrogen sources in the fermentation process. Suitable nitrogen sources include, for example, yeast hydrolysates, primary yeast, soybean meal, cottonseed flour, hydrolysates of casein, corn steep liquor, distiller's solubles or tomato paste and the like. The sources of nitrogen, either alone or in combination, are used in amounts ranging from about 0.05% to 0.4% by weight of the aqueous medium.
Among the nutrient inorganic salts which can be incorporated in the culture media are the customary salts capable of yielding sodium, potassium, ammonium, calcium, phosphate, sulfate, chloride, carbonate, and the like ions. Also included are trace metals such as cobalt, manganese, iron and magnesium.
It should be noted that the media described in the examples are merely illustrative of the wide variety of media which may be employed, and are not intended to be limitative.
One important media characteristic is that when strain S-130 is grown under low Ca++ conditions, i.e., in deionized water, or an aqueous system having less than 200 ppm Ca++ ions, the resultant gum has improved solution properties.
The fermentation is carried out at temperatures ranging from about 25"C to 35"C; however, for optimum results it is preferable to conduct the fermentation at temperatures of from about 28'C. to 32'C. The pH of the nutrient media for growing the Alcaligenes culture and producing the polysaccharide S-130 can vary from about 6 to 8, preferably 6.5 to 7.5.
Although the polysaccharide S-130 is produced by both surface and submerged culture, it is preferred to carry out the fermentation in the submerged state.
A small scale fermentation is conveniently carried out by inoculating a suitable nutrient medium with the culture, and after transfer to a production medium permitting the fermentation to proceed at a constant temperature of about 30"C on a shaker for several days.
The fermentation is initated in a sterilized flask of medium via one or more stages of seed development.
The nutrient medium for the seed stage may be any suitable combination of carbon and nitrogen sources.
The seed flask is shaken in a constant temperature chamber at about 30"C for 1-2 days, or until growth is satisfactory, and some of the resulting growth is used to inoculate either a second stage seed or the production medium. Intermediate stage seed flasks, when used, are developed in essentially the same manner; that is, part of the contents of the flask from the last seed stage are used to inoculate the production medium. The inoculated flasks are shaken at a constant temperature for several days, and at the end of the incubation period the contents of the flasks are recovered by precipitation with a suitable alcohol such as isopropanol.
For large scale work, it is preferable to conduct the fermentation in suitable tanks provided with an agitator and a means of aerating the fermentation medium. According to this method, the nutrient medium is made up in the tank and sterilized by heating at temperatures of up to about 121 C. Upon cooling, the sterilized medium is inoculated with a previously grown seed of the producing culture, and the fermentation is permitted to proceed for a period of time as, for example, from 2 to 4 days while agitating and/or aerating the nutrient medium and maintaining the temperature at about 30"C. This method of producing the S-130 is particularly suited for the preparation of large quantities.
The product is recovered from the fermentation medium by precipitation with a suitable alcohol, such as isopropanol.
HETEROPOLYSACCHARIDE S-130
The heteropolysaccharide produced by an unnamed Alcaligenes species is composed principally of carbohydrate with 3-5% acetyl groups as the O-glycosidically linked ester.
The carbohydrate portion of the S-130 polysaccharide contains 10-20% glucuronic acid; 10-25% mannose; 20-40% glucose; and 30-60% rhamnose.
The acetyl content of 5-10% was determined by treating a 0.2% aqueous solution of S-130 gum with an alkaline, hydroxylamine reagent followed by treatment with an acidic ferric chloride reagent [S.Hestrin (1949) J. Biol. Chem. 180 pp.249-261].
The neutral sugars of polysaccharide S-130 were determined by dissolving ten mg. of the product in 2 ml 2N H2SO4, and the mixture is heated at 1 00'C for 4 hours. The resulting solution is cooled, neutralized with barium hydroxide and the pH is brought to 5-6 with solid carbon dioxide. The resulting precipitate of barium sulfide is removed by centrifugation and the supernatent is concentrated to a syrup under reduced pressure.
The sugars in the hydrolysate are tentatively identified by gas-liquid chromatography of their aldononitrile acetate derivatives on a Hewlett-Packard Model 5750 chromatograph using 3% by weight OV-225 on 80/100 mesh Gas Carom Q at 210 C. The sugars are identified and quantitated by comparison with authentic standards [J.K. Baird, M.J. Holroyde, and D.C. Ellwood (1973) Carbohydr. Res. 27 pp 464-467].
The various neutral sugars of the polysaccharides were also characterized by use of descending paper chromatography on Whatman No. 1 chromatography paper using as the solvent the upper layer of pyridine:ethyl acetate:water (2:5:5). Chromatograms were stained using silver nitrate dip and acid analine phthalate spray reagent. Component sugars were identified by co-chromatorgraphy with sugar standards and by the specific-color reaction with the analine phthalate reagent.
The glucuronic acid content of the polysaccharide was determined by two separate methods. In one method the sample was decarboxylated with 19% hydrochloric acid and the liberated carbon dioxide was trapped in standard sodium hydroxide and determined by back titration [B.L. Browning (1967) Methods of
Wood Chemistry lI, pp. 632-633] and by the carbazole colorimetric method [T.Bitter and H.M. Muir (1962)
Anal. Biochem. 4pp. 330-334].
Paper electrophoresis was used for the separation and tentative identification of the glucuronic acid present in the neutralized acid hydrolysate described above. Aliquots of this and known glucuronic acid standards were applied to Camag electrophoresis paper No. 68-011 and electrophoresis was carried out for 2.0 hours in a pH 2.7 buffer using a Camag Model HVE electrophoresis apparatus. Chromatograms were air dried and stained with silver nitrate dip reagent to locate the glucuronic acids being separated.
The polysaccharide S-130 imparts viscosity to an aqueous medium when dissolved in water in low concentrations. Because of this, its sensitivity to shear and overall rheology, it is useful as a thickening, suspending emulsifying, stabilizing, lubricating, film-forming, or binding agent, especially in aqueous systems.In particular, it has uses in the following applications or products: adhesives, wall-joint cements, water-retentive grouts and mortars, spackling compounds, can sealing, boiler compounds, latex creaming, welding-rod fluxes, brazing pastes, ceramic glazes and extrusions, cleaners and polishes, toys, emulsions (latex, asphalt, silicont), silver recovery, seed coatings, spray control for pesticides or herbicides, emulsifiable concentrated and flowable pesticides and herbicides, tobacco binders, water-based inks lithographic fountain solutions, leather finishes, hydro-mulching and hydro-seeding, textile printing and finishing, wet-end paper additives, wet-end paper retention and formation aid, anti-stick compounds, mold-release agents, liquid resins, slurry and packaged explosives, petroleum and water-well drilling muds, petroleum workover and completion fluids, petroleum stimulation fluids, cosmetics, pharmaceutical suspensions and emulsions.
Also this gum has utility in food systems such as jellies and other high sugar systems, beverages including citric acid based drinks, dairy products including ice cream and yoghurt, salad dressings, dry mixes, icings, and glazes, syrups, puddings, farinaceous fods, canned and retorted foods, and bakery fillings.
A particularly valuable utility is in the field of petroleum and water-well drilling muds. More detailed examples illustrating this preferred use are found, infra.
Although S-130 gum possesses a general viscosity-imparting property, its particular profile of solution properties is a distinctive characteristic which enables it to be distinguished over other heteropolysaccharides.
Briefly, the gum is high viscosity in the presence of 0.1% KCI (1650 cPs) and Dl water (1470 cPs). It shows excellent acetic acid heat stability (+36%) and heat stability (-1%). A gel is formed in the presence of heat and 1% NaOH. This gum is KCI-reactive showing a greater than 16% viscosity increase in the presence of 0.1% and 2.5% KCI. A brittle, low tensile strength film is formed.
The gum's properties of good viscosity in brine (KCI and NaCI), and seawater, good acid and heat stability, a constant viscosity over pH ranges 1.5 to 12.1, and good shear stability, make it especially suitable for industrial applications such as drilling and petroleum applications fluids. Specifically, S-130 gum has excellent heat stability, and no viscosity loss occurs upon autoclaving at 121"C and 15 psi for 15-20 minutes.
1 Viscosity and Shear
A. Brookfield DI H2O Dl H2O + 0.1% KCI
1. 1.0%@ 60 rpm 1470 cPs 1650 cPs @ 6 rpm 10,400 cPs
Spindle No. 3
2. 0.1% (UL adapter)a 45 cPs 30 cPs
3. 0.5% Wells
Brookfield @9.6sec-1 680 cPs 1180 cPs
B.Shearb
1. n & ommat;19.2sec- 10,110 cPs
2. n @ 9.6 sec- 2200 cPs 3. n # 76.8 sec-1 nCCt76.8sec1 320 sec- 320 cPs
4. n # 384 sec- nCa384sec1 384 sec- 60 cPs
5. n Qa 384 sec- 60 cPs
6. n @ 9.6sec-1 1800 cPs C. 40'FStorage: 2050 cPs @ 60 rpm, with spindle No. 4, very chunky flow, increase of 39% viscosity over ambient
temperature viscosity.
2. Acid, Base, HeatStability
A. Stability
1. Acetic acid plus heat
initialn: 2500 cPs
finaln: 3600 cPs
% change: +36
2. 1% HC1 plus heat
initialn: 1230 cPs
finaln: total loss
% change: total loss
3. 1% NaOH plus heat initial: 1380 cPs
finaln: Gel
% change: Gel
4. Heat only
initialn: 2130 cPs
finaln: 2100 cPs
%change: -1
B. pHEffect
1. 5% acetic acid 2.71 pH 2560 cPsC
2. 5%NH40H 11.09 pH 2070 cPsC 3. SaltandDye Compatibllfty A. Salt
1.CaCI2 (saturated) compatible
2. Am m. polyphosphate precipitate
3. 60% NH4NO3 compatible
4. 1% Al2(S04)3.18H2O compatible
5. 1% CaC12.2H20 compatible
6. 1% KCI compatible
7. 0.1%KCI 2560 cPsC 8. 2.5%KCI 2560 cPsC B. Dyes
1. Milling Green compatible
2. Methylene Blue precipitate 4. TexturelFlowProperties High viscosity gum, chunky flow, no gelation, gummy to the touch.
5. Synergism and Enzymes: 0 hr 2 hr n 1% n of mixture of mixture
A. Guar 2320 cPs 2560 cPs 2560 cPs
B. H.P. Guar 1960 cPs 1950 cPs 2560 cPs
C. CMC 870 cPs 1310 cPs 970cPs D. HEC 440 cPs 870 cPs 1180 cPs
E. SMS47-6 2130 cPs
Expected
viscosity Synergism
A. Guar 2230 cPs +15% B. H.P. Guar 2050 cPs +25%
C. CMC 1360 cPs None%
D. HEC 970 cPs +22% 6. MilkReactivity
A. Dispersion: Excellent
B. Whey off: 1 st day C. Other observations: 7. FilmFormation Uneven pull down; film formed, not plastic, very brittle, low tensile strength.
a Viscosity measured on a Brookfield Model LVF at 6 rpm with the No. 1 spindle and a UL adapter.
b All measurements made on a Wells-Brookfield micro-viscometer Model RVT-c/p. -1 CViscosity measured on a Wells-Brookfield micro-viscometer Model RVT-c/p at 9.6 sec EXAMPLE 1
Fermentation Procedure for Producing Heteropoly-saccharide S- 130 A. Culture Maintenance
The unnamed Alcaligenes organism, ATCC 31555, grows quite well on NA agar, with good colonial morphology. The incubation temperature is 30 C. The organism produces a yellow pigment.
B. Seed Preparation
Flask seeds are prepared in YM broth incubated at 30 C for 24 hours, then used to inoculate seed medium which is the same as final fermentor medium. A 5% inoculum is used for a 14Lfermentor.
C. Final FermentorMedium The following medium gives acceptable results in the 14L fermentor and can be used for larger scale 20L and 70Lfermentors: Glucose 3.0% K2HPO4 0.05%
Promosoy 0.05%
NH4NO3 0.09% MgSO4.7H2O 0.01 % Fe++ ........................................ 1 ppm
HoLe salts ........................................ 1 ml/L
The pH is controlled between 6.5 and 7.5. At 0 hours, pH is 7.3 and residual carbon source was measured to be 3.07%. After 25.5 hours, pH was 7.0 and beer viscosity measured 2350. After 63.5 hours, pH was 6.3 and beer viscosity 3950, and the reaction is terminated by adding 4% isopropanol.
HoLe salts are a trace element solution containing tartrate, magnesium molybdate, CoCI3, ZnCI2, CuCl2, boric acid, manganese chloride and ferrous sulfate.
The initial agitation and aeration rates were 400 rpm and 3L/M, respectively. The aeration remained constant throughout the fermentation. The agitation was increased as necessary during the fermentation to ensure good mixing. Maximum agitation was 1600 rpm.
When a low calcium product is desired, the medium above is used with deionized water.
D. Recovery
Fermentation beer is pasteurized at 167 F for 10-15 minutes. Good fibers are produced under precipitation conditions giving 58-60% spent IPA.
E. Drying
Product is recovered after drying at 50-55"C for about one hour in a forced-air tray dryer.
The product prepared in this example shows a 1% viscosity of 1490 in deionized water, and 2400 at 1% in DI water containing 1% added KCI. It analyzed 12% glucuronic acid; 28% glucose; 13% mannose; 59% rhamnose; 3.5% acetyl, and no pyruvate.
Measurements of this gum is 2% KCI show excellent viscosity development, with excellent NaCI stability and maintenance of viscosity up to at least 300 F; slight gelation of gum is observed in 2% KCI.
EXAMPLE 2
Sea WaterMud Composition
S-130 has utility in muds used for oil well drilling. A formula and data for a sea water mud are as follows:
S-130...................................1.0lb
Sea water...............................1.0 bbl
Fann viscosity data:
Speed (rpm) 3 6 100 200 300 600
Dial Reading 3.4 3.8 8.5 11.0 13.2 17.2
p = 7.1
EXAMPLE 3
Hydraulic Fracturing Fluid Composition
Hydraulic fracturing fluid example - for high temperatures (over 200 F):
per 1000 gallons:
H20 5% Methanol or 500 ppm sodium sulfite 2% KCI . 1651b
Ammonium persulfate . .. lOIb S-130 . . .. 40 lb Viscosity of the above fluid:
Fann 35 rpm 600 300 200 100 6 -3
Viscosity, cP 15.0 24.2 33.4 53.3 450 813
Claims (4)
1. Heteropolysaccharide S-130, which contains 10-20% glucuronic acid; 10-25% mannose, 20-40% glucose 30-60% rhamnose; and 3-5% acetyl groups, prepared by fermentation under controlled conditions of culture ATCC 31555, an Alcaligenes species.
2. The compound of claim 1, containing less than 200 ppm Ca ++ ions.
3. The compound claimed in claim 1 or 2, for use as a thickening, suspending, emulsifying, stabilizing, lubricating, film-forming, or binding agent in an aqueous system.
4. A composition containing a compound as claimed in claim 1, substantially as hereinbefore described in Example 2 or 3.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US7357379A | 1979-09-07 | 1979-09-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2058107A true GB2058107A (en) | 1981-04-08 |
GB2058107B GB2058107B (en) | 1983-05-11 |
Family
ID=22114516
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8028286A Expired GB2058107B (en) | 1979-09-07 | 1980-09-02 | Heteropolysaccharide s-130 |
Country Status (6)
Country | Link |
---|---|
JP (1) | JPS5645901A (en) |
FR (1) | FR2465000A1 (en) |
GB (1) | GB2058107B (en) |
HK (1) | HK83885A (en) |
KE (1) | KE3562A (en) |
SG (1) | SG67685G (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0064354A1 (en) * | 1981-04-23 | 1982-11-10 | Merck & Co. Inc. | Heteropolysaccharide S-198 |
JPS57206382A (en) * | 1981-04-23 | 1982-12-17 | Merck & Co Inc | Heteropolysaccharide s-198 |
EP0077680A2 (en) * | 1981-10-21 | 1983-04-27 | Merck & Co. Inc. | Heteropolysaccharide S-194, a process for producing it, and compositions containing it |
US4575551A (en) * | 1983-05-02 | 1986-03-11 | Nakano Vinegar Co., Ltd. | Acidic heteropolysaccharide AM-2 |
US4749565A (en) * | 1984-09-21 | 1988-06-07 | L'oreal | Cosmetic compositions based on cationic silicone, water-soluble heteropolysaccharide and electrolyte |
US4818817A (en) * | 1983-11-30 | 1989-04-04 | Petroleum Fermentations N.V. | Enzymatic degradation of lipopolysaccharide bioemulsifiers |
US5175279A (en) * | 1989-01-19 | 1992-12-29 | Hakuto Co., Ltd. | Polysaccharide, and water absorbent, moisture absorbent or humectant and thickening agent chiefly made of the polysaccharide |
US5378832A (en) * | 1991-11-29 | 1995-01-03 | Agency Of Industrial Science And Technology | Polysaccharide and a method of producing it |
EP0735049A2 (en) * | 1995-03-27 | 1996-10-02 | Tayca Corporation | Humectant, antistatic agent, dispersant and film-forming agent having polysaccharide as active principle, preparation process of polysaccharides, and Klebsiella strain |
US5702690A (en) * | 1991-07-25 | 1997-12-30 | L'oreal | Composition for washing and antidandruff treatment of hair and the scalp, based on selenium sulphide and nonionic surfactant of the polyglycerolated or alkylpolyglycoside type |
US5786310A (en) * | 1991-02-19 | 1998-07-28 | L'oreal | Synthetic oil-based washing compositions and method of use |
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JP2008188514A (en) * | 2007-02-02 | 2008-08-21 | Sasakura Engineering Co Ltd | Compressor for steam in reduced pressure type evaporator |
CN108347981A (en) * | 2015-09-02 | 2018-07-31 | 三荣源有限公司 | The method of the physical property of improvement or holding substance |
JP7082457B2 (en) * | 2016-03-03 | 2022-06-08 | 三栄源エフ・エフ・アイ株式会社 | High-sweetness sweetener taste improving agent and taste improving method |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3856626A (en) * | 1972-06-09 | 1974-12-24 | Exxon Research Engineering Co | Fermentation process for the simultaneous production of protein and bio polymers |
-
1980
- 1980-09-02 GB GB8028286A patent/GB2058107B/en not_active Expired
- 1980-09-05 FR FR8019244A patent/FR2465000A1/en active Granted
- 1980-09-06 JP JP12296680A patent/JPS5645901A/en active Granted
-
1985
- 1985-09-14 SG SG67685A patent/SG67685G/en unknown
- 1985-09-19 KE KE356285A patent/KE3562A/en unknown
- 1985-10-31 HK HK83885A patent/HK83885A/en not_active IP Right Cessation
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0064354A1 (en) * | 1981-04-23 | 1982-11-10 | Merck & Co. Inc. | Heteropolysaccharide S-198 |
JPS57206382A (en) * | 1981-04-23 | 1982-12-17 | Merck & Co Inc | Heteropolysaccharide s-198 |
JPH046721B2 (en) * | 1981-04-23 | 1992-02-06 | Merck & Co Inc | |
US4401760A (en) * | 1981-10-21 | 1983-08-30 | Merck & Co., Inc. | Heteropolysaccharide S-194 |
EP0077680A3 (en) * | 1981-10-21 | 1983-06-29 | Merck & Co. Inc. | Heteropolysaccharide s-194, a process and culture for producing it, and compositions containing it |
EP0077680A2 (en) * | 1981-10-21 | 1983-04-27 | Merck & Co. Inc. | Heteropolysaccharide S-194, a process for producing it, and compositions containing it |
US4575551A (en) * | 1983-05-02 | 1986-03-11 | Nakano Vinegar Co., Ltd. | Acidic heteropolysaccharide AM-2 |
US4818817A (en) * | 1983-11-30 | 1989-04-04 | Petroleum Fermentations N.V. | Enzymatic degradation of lipopolysaccharide bioemulsifiers |
US4749565A (en) * | 1984-09-21 | 1988-06-07 | L'oreal | Cosmetic compositions based on cationic silicone, water-soluble heteropolysaccharide and electrolyte |
US5175279A (en) * | 1989-01-19 | 1992-12-29 | Hakuto Co., Ltd. | Polysaccharide, and water absorbent, moisture absorbent or humectant and thickening agent chiefly made of the polysaccharide |
US5955406A (en) * | 1991-02-19 | 1999-09-21 | L'oreal | Synthetic oil-based washing composition and method of use |
US5786310A (en) * | 1991-02-19 | 1998-07-28 | L'oreal | Synthetic oil-based washing compositions and method of use |
US5702690A (en) * | 1991-07-25 | 1997-12-30 | L'oreal | Composition for washing and antidandruff treatment of hair and the scalp, based on selenium sulphide and nonionic surfactant of the polyglycerolated or alkylpolyglycoside type |
US5378832A (en) * | 1991-11-29 | 1995-01-03 | Agency Of Industrial Science And Technology | Polysaccharide and a method of producing it |
EP0735049A3 (en) * | 1995-03-27 | 1997-06-18 | Tayca Corp | Humectant, antistatic agent, dispersant and film-forming agent having polysaccharide as active principle, preparation process of polysaccharides, and Klebsiella strain |
EP0735049A2 (en) * | 1995-03-27 | 1996-10-02 | Tayca Corporation | Humectant, antistatic agent, dispersant and film-forming agent having polysaccharide as active principle, preparation process of polysaccharides, and Klebsiella strain |
US5989874A (en) * | 1995-03-27 | 1999-11-23 | Tayca Corporation | Humectant, antistatic agent, dispersant and film-forming agent having polysaccharide as active principle, preparation process of polysaccharides, and Kliebsiella ocytoca TNM-3 strain |
Also Published As
Publication number | Publication date |
---|---|
KE3562A (en) | 1985-11-01 |
JPH0239521B2 (en) | 1990-09-06 |
GB2058107B (en) | 1983-05-11 |
JPS5645901A (en) | 1981-04-25 |
FR2465000B1 (en) | 1982-07-16 |
FR2465000A1 (en) | 1981-03-20 |
HK83885A (en) | 1985-11-08 |
SG67685G (en) | 1986-06-13 |
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