PRODUCTION OF XANTHAN HAVING A LOW PYRUVATE CONTENT

Abstract: Low pyruvate xanthan gum comprising 0.1-1% by weight pyruvate (FCC Method) has useful properties for secondary oil recovery. It is produced by aerobically fermenting an organism of the genus Xanthomonas in a broth comprising: 1) a chemically defined simple salts medium com­ prising sources of nitrogen, sulphur, potassium, phosphorus, magnesium, calcium, and (optionally) iron, said simple salts medium being substantially free of cobalt, copper, manganese, zinc and boron; 2) an assimilable carbon source, and 3) a complex organic material which is a nitrogen source.

Description: PRODUCTION OF XANTHAN HAVING A LOW PYRUYATE CONTENT This invention relates to a process for the production of xanthan, the biopolymer obtained from various species of the genus-Xanthomonas,having a low pyruvate content. The structure of xanthan, specifically the gum produced by Xanthomonas campestris strains, was proposed by Jansson et al (Carbohydrate Research 45, 275-282 (1975)) to consist of a ss (1-4) - linked glucose backbone, alternative residues of which are substituted with a trisaceharide side chain composed of mannose and glucuronic acid in the ratio 2:1. These side chains terminate in D-mannose residue, a proportlon of which are substituted with pyruvic acid to form 4,6-0-(1-carboxyethylidene)-D-mannose. Some other Xanthomonas species have been shown to produce exopolysaccharides composed of glucose, mannose and glucuronic acid containing substituent pyruvic acid at a level greater than 1% by weight (Qrentas et al, Can. J. Microbiol. 9,427,430, (1963)). It is recognized that the proportion of the D;mannosyl residue substituted with pyruvic acid in xanthan generally can vary and it is usual for the level to be in the range 2.5-5.0 a by weight. In a comprehensive study, Cadmus et al (Biotachnol. Bioeng. 20, 1003-1014, 1978) found that the culture medium composition, the strain of X.campestris and the cuttivation temperature all influence the pyruvic acid content of the polymer. A pyruvic acid content of 1.3 was the minimum obtained. U.K. Patent Application No.GB 2 008 60Q A, in the name of Pfizer Inc., describes the production of xanthan gums which are pyruvate-free. These gums are produced by a new strain of Xanthomonas, namely Xanthomonas campestris ATCC 31313. One use for which xanthan is of considerable interest, is as a water additive for use in the displacement of oil from partially depleted oil fields. In this technique, oil which is still in the pores of the oil-bearing rock after the initial pressurized oil has been recovered, is displaced by flooding the rock formation with water. This water is rendered more viscous by the addition of a polymeric water-soluble material such as a polyacrylamide or xanthan inorder to improve its displacement characteristics. According to GB 2 008 600A, completely pyruvate-free xanthan is advantageous in water flooding processes since it is less prone to precipitation causing blockage of the pores of the oil-bearing rock. However the pyruvate-free xanthan of GB 2 008 600A exhibits a sharp decrease in apparent viscosity at 700C. As explained above, ordinary strains of Xanthomonas produce, under the usual cultivation condition, a xanthan having a pyruvate content bf over 1%. Indeed, for food use, xanthan is required to have a pyruvate content of at least 1.5, and thus industrial xanthan-producing processes concentrate on producing xanthan having a relatively high pyruvate content. We have found that by cultivating X.campestris under certain conditions in continuous culture, a xanthan gum can be produced having a pyruvate content of below 1 %. In some instances a pyruvate content of about 0.1 %, i.e. near 0, can be obtained by this method. We have found that the control of the pyruvate content is related to a number of factors, all of which must be right for low pyruvate product to be obtained. According to the present invention we provide a process for the preparation of xanthan having a pyruvate content of less than 1.0 % by weight, comprising continuous culture of a xanthanproducing strain of genus Xanthomonas in a medium containing only sources of nitrogen sulphur, carbon, potassium, phosphorus, magnesium, calcium and? optionally, iron, the medium being substantially free from cobalt, copper, manganese, zinc and boron and being a chemically defined simple salts medium which additionally contains a complex organic material; at a concentration of total precipitable matter (TPM) of at least 15 g 1 1 (i.e.- greater than 44% conversion efficiency) and a xanthan to cell ratio by weight of at least 4:1; and isolating from the culture medium the xanthan produced. As stated, the medium used for the continuous fermentation should be defined, simple salts, medium, that is to say a medium containing only inorganic. salts of known formula as sources of N, N, P, K, Ca, Fe and Mg and a carbohydrate of known formula as the carbon source. In this basic medium is includedva complex organic material which may act as a nitrogen source. The complex nitrogen source may comprise, for example, a yeast extract or a leguminous product such as soy flour. Yeast extract is preferred. The complex nitrogen source is to be added, at a level of 0.01 to 0.05 g available N per litre in the culture medium preferably about 0.02 g/1. With a low-salts yeast extract, 0.02 g available N per litre corresponds to a level of about 0.2 g yeast extract per litre. The complex nitrogen source is an essential feature of the present invention, together with the absence of trace elements from the medium. If a normal, simple salts, chemically defined medium is modified to contain no trace elements, we find that the cell growth is considerably suppressed'and the polysaccharide produced has a rather low pyruvate content. The use of such a medium is obviously not commercially useful, as the yield of xanthan would be too low. However, we have found that if trace elements (with the possible exception of iron) are excluded but the medium is enriched with a complex source such as yeast extract, the product can be a very low pyruvate material and can be produced in good yield. Thus, for example, Low Salt Yeast Extract, sold by Distillers Company Limited, contains Zn 60 p.p.m; Cu 10 p.p.m.; Mn 15 p.p.m.; Co 5 p.p.m.; Fe 100 p.p.m. At a concentration of 200 p.p.m in the medium, the yeast extract thus supplies no more than 0.012p.p.m of Zn, Mn, Co and Cu and only 0.02 p.p.m. of Fe. I.s contrast a normal medium might contain from *0.05 to 0.5 p.p.m of n, Mn Co and Cu and from 5 to 10 p.p.m. of Fe. The carbohydrate source is conveniently a monosaccharide which may be in the form of a syrup which may also contain higher saccharides, for example a glucose syrup derived from acid and/or enzymic degradation of starch. All of these requirements are essential and if departed from in any way tend to lead to the production of xanthan containing a higher pyruvate content than required, unless a special strain of X.campestris, such as ATCC 31313, is used. The pyruvate level referred to generally throughout this specification is measured by the F.C.C. Food Chemicals Codex Second Edition, National Academy of Sciences, Washington DC 1971, page 856 method which is the method used in nearly all the existing xanthan art up to now. Typically, a broth or xanthan solution containing 0.20.4% w/v polysaccharide is hydrolysed in 1 N HCl for 3 hours. A 2 ml aliquot is removed and is mixed with 1 ml of a 2,4-dinitrophenylhydrazine reagent (0.5t w/v in 2N HCl.) for 5 minutes. The reaction mixture is extracted with 5 ml of ethyl acetate and the aqueous layer is discarded. The ethyl acetate extract is extracted with three 5 ml portions of 10X w/v aqueous sodium carbonate and then the combined extracts are diluted to 25 ml with additional 102 w/v aqueous sodium carbonate. The optical density of this solution is then measured at 375 nm and the pyruvate content determined against a previously known standard. Using this method, the product of the process of the present invention has a pyruvate level of less than 1t, typically from 0.25 to 0.655. However, there is an alternative assay for pyruvate, described in U.S.D.A. ARS-NC-51 November 1976. This assay is believed to be more reliable and more accurate, but gives lower figures than the FCC test. Typically, the product of the present prccess is found to contain from 0.08 to about 0.25 pyruvate by this enzymic assay. Using the conditions according to the invention, a low-pyruvate xanthan is obtained, possessing viscosity characteristics which make it useful in the same applications as that obtained from X. camDestris ATCC 31313 by the process of Application 2 008 600A. The lcw-pyruvate xanthan obtained according to the present invention can be isolated from the culture medium in any conventional manner. Usually, the polysaccharide will be precipitated by addition of an organic solvent such as isopropanol. If desired, the polysaccharid can then be further purified and clarified, e.g. by treatment with acid or alkali and/or with an enzyme. The requirement that the T.P.M.concentration should be at least 15 gl-1 with a polymer to cell ratio of at least 4:1 can be achieved by methods well known in this art, namely by ensuring that the nutrient c'oncentration is sufficiently high (although the exact level will depend on the type of nutrient used). As a typical example, in a nitrogen-limited fermentation, a nitrogen level of at least 0.2 g is required. Preferably, a T.P.,m', level is achieved which gives an actual xanthan level of at least 15 gl The rate of continuous fermentation will, under steady state conditions, inevitably be limited by the concentration of one of the nutrients in the medium. This limiting nutrient may, for example, be nitrogen or sulphur,.or may be one of the trace elements missing from the medium. A preferred medium contains, for example, from 40-70 g/l -of glucose (as a syrup); 2 to 4 g/l of an ammonium salt, e.g. ammonium sulphate or diammonium hydrogen phosphate; about 0.02 to 0.1 g/l of magnesium compounds; about 0.25 to 0.75 g/l of potassium salts, up to 0.05 g/l of iron salts and 0.1 to 0.5 g/l low-salts yeast extract; in deionised water. The oxygenation should also be sufficiently plentiful e.g. by providing good aeration coupled with efficient stirringof the fermenter tank. The following examples illustrate the invention further. Example 1 Xanthomonas camoestris (laboratory stock derived from ATCC 13951) was grown continuously in a 5 litre capacity, stirred tank fermenter. Fermentation parameters were;.- pH, 7.0; temperature, 30"C; impeller speed, 1000 rev.min-1; impeller diameter, 8.4 cm (curved-bladed impellers with blades swept from direction of rotation); air flow, 1.47 1. min¯1. The composition of the culture medium is given in Table 1. The glucose (in one-fifth total volume) was sterilised separately from the salts components (in four-fifths total volume) at 121"C and a pressure of 1 bar for 15 mins and when cooled the solutions were mixed to give the complete medium at pH 6.8. The working volume was set at 2 litres by means of a weir. Stirring was achieved using tao curved-bladed impellers 6.0 cm apart. The lowest impeller was positioned at the lowest point on the impeller shaft. Air was introduced below the lowest impeller. Mixing was aided by four baffles, positioned longitudinally, around the circumference of the culture vessel. The fermenter was fitted with automatic pH control for metering in 1M NaOH to maintain the pH at 7.0. The fermenter and addition lines were sterilised in the usual way prior to addition of the medium. To the medium in the culture vessel was added 100ml of a culture grown in MYGP broth (g/l:-malt extract, 3.0; yeast extract, 3.0; glucose, 10.0; peptone, 5.0; pH not adjusted) in shake flasks. The culture was grown in batch mode for 36h under the described conditions. A continuous medium feed was then supplied at a dilution rate of 0,05h'l (100 ml/h). The culture was monitored for (a) pH; (b) measurement of 02 uptake and C02 evolution using an oxygen analyser and an infra-red carbon dioxide analyser; (c) total isopropanol precipitable matter (TPM) -( precipitate from broth: isopropanol mixture (1:2 w/v) collected by filtration and dried under an infra-red lamp); (d) optical measurement of cell density at 540 nm. The culture was allowed to reach a "steady-state". A sample of the total precipitable matter (xanthan gum) was analysed for pyruvate content by the enzymic method described in the U.S. Department of Agriculture publication ARS-NC-51, November 1976. The viscosities of a 1 solution.of the xanthan gum in distilled water and in a 1 % solution of sodium chloride were measured on a Contraves Rheomat 30 cone and plate viscometer. A xanthan gum with a pyruvate content of 0.6 Z was obtained as indicated in Table 2. Example 2 Xanthomonas camDestris (strain of Example 1) was continuously cultured under the conditions described fn.Example 1 except that the air flow rate was 2.0 litres mien 1, and the impeller speed was 550 rev. mien 1, the two coaxial impellers being 13 cm diameter and 10 cm apart, each having 6 curved blades. The culture medium used, which was sulphur limited with nitrogen supplied as ammonium, is given in Table 1. The characteristics of the product obtained are summarised in Table 2. Examole 3 Xanthomonas campestris (strain of Example 1) was continuously cultured as described in Example 2 except that-working volume was 2.5 , air flow rate was 4.0 1 rnn1, impeller speed was 650 rev. mien 1 and dilution rate was 0.046h 1. The medium used was designed to be nitrogen.limited (Table 1), but a small amount of nitrogen was detected in the broth removed, indicating that the limiting factor was possibly a trace element rather than nitrogen. Steady state conditions were achieved for about 230 hours. The pyruvate content of xanthan gum obtained under these steady-state conditions was 0.09 + 0.02 (w/w) (Enzyme). Example 4 Xanthomonas campestris (strain of Example 1) was continuously cultured as described in Example 1. Air flow rate was 1.75 1 mien¯1, impeller speed was 1200 rev. mien 1, dilution rate was 0.055 h 1. The culture medium (Tabte 1) was similar to that of Example 3. The pyruvate content of xanthan gum obtained under steady-state conditions was 0.3 X (w/w). Comparative Examples 1-4 Xanthomonas campestris (strain of Example 1) was continuously cultured in a similar way to that described in Example 1. The culture media, as given in Table 1, contained no trace elements nor yeast extract (comp.Example 1); trace elements but no yeast extract (Comp.Examples 2 and 4); or trace elements and yeast extract (Comp.Example 3). In Comp. Example 2, the trace element level was reduced 50% compared with that of Comp. Example 4. The results are summarised in Table 2. Comparison of product obtained according to the invention with a higher pyruvate product shows that both possess similar viscosities. A striking feature of the low pyruvate material prepared according to the present invention, however, is its apparent stability to elevated temperatures. A solution can be refluxed for several hours without the viscosity being markedly lowered. This property is significant when it is remembered that the temperatures encountered in oil-bearing reservoirs can often be greater than 10OOC. Figure 1 shows a comparison of viscosities after various reflux times for the product of Example 4, the product of Comparative Example 4 and two commercially available xanthan gums, Rhodopol (T.M) (Rhone Poulenc) and Keltrol (T.M) (Kelco Div.of Merck & Co., Inc.). In order to show that the stability is not merely due to the absence of trace elements in the solution, a curve for a solution containing the product plus trace elements equivalent to normal medium if all entered into product is included. Heat treatment of the product in curve (5) was at 1"COP for 2 minutes. TABLE 1 Culture media used in the Examples EMI12.1 Component <SEP> Example <SEP> Comparative <SEP> Example <tb> gl-1 <SEP> 1 <SEP> 2 <SEP> 3 <SEP> 4 <SEP> 1 <SEP> 2 <SEP> 3 <SEP> 4 <tb> Glusose <SEP> 43Ú <SEP> 43Ú <SEP> 56Ú <SEP> 67Ú <SEP> 62ê <SEP> 62Ú <SEP> 60Ú <SEP> 62Ú <tb> Acetic <SEP> acid <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0.45 <SEP> 0.45 <SEP> 0.45 <tb> Citric <SEP> acid <SEP> 1.0 <SEP> 1.0 <SEP> 0.6 <SEP> 0.6 <SEP> 1.0 <SEP> 1.0 <SEP> 1.0 <SEP> 1.0 <tb> Mg(OH)2 <SEP> 0.034 <SEP> 0.034 <SEP> 0 <SEP> 0 <SEP> 0.048 <SEP> 0.078 <SEP> 0.07 <SEP> 0.078 <tb> Ca(OH)2 <SEP> 0.025 <SEP> 0.025 <SEP> 0.025 <SEP> 0.025 <SEP> 0 <SEP> 0.05 <SEP> 0.05 <SEP> 0.05 <tb> MgSO4#7H2O <SEP> 0.062 <SEP> 0.062 <SEP> 0.02 <SEP> 0.02 <SEP> 0 <SEP> 0.06 <SEP> 0.09 <SEP> 0.06 <tb> K2HPO4 <SEP> 0 <SEP> 0.5 <SEP> 0 <SEP> 0 <SEP> 0.78 <SEP> 1.0 <SEP> 1.0 <SEP> 1.0 <tb> KH2PO4 <SEP> 0.5 <SEP> 0 <SEP> 0.5 <SEP> 0.5 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <tb> (NH4)2HPO4 <SEP> 3.77 <SEP> 3.77 <SEP> 2.7 <SEP> 2.7 <SEP> 3.02 <SEP> 2.62 <SEP> 2.38 <SEP> 3.0 <tb> Yeast <SEP> Extract <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0 <SEP> 0 <SEP> 0.2 <SEP> 0 <tb> Mgl-1 <SEP> (p.p.m) <tb> MnSO4#4H2O <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0.55 <SEP> 1.1 <SEP> 1.1 <tb> ZnSO4#7H2O <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0.71 <SEP> 0.71 <SEP> 1.42 <tb> CuSO4#5H2O <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0.125 <SEP> 0.25 <SEP> 0.25 <tb> CoSo4#7H2O <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0.14 <SEP> 0.28 <SEP> 0.28 <tb> H3BO4 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0 <SEP> 0.553 <SEP> 0.03 <SEP> 0.06 <SEP> 0.06 <tb> F2SO4#7H2O <SEP> 35 <SEP> 0 <SEP> 36 <SEP> 36 <SEP> 0.014 <SEP> 17.8 <SEP> 3.56 <SEP> 35.6 <tb> 1 glucose = Dexyme 081 from Tunnel Refineries Limited, Tunnel Avenue, Greenwich, London SE10 2 glucose = Meritose Grade AR, from Fisons Scientific Apparatus Ltd, Meadow Road, Loughborough, Leicestershire TABLE 2 Dilution rate, h-1 Cell concentration E540, gl-1 Cell dry weight Polymer: cell ratio Broth rheology(K(n)), cp Oxygen uptake, mmol l-1 h-1 Pyruvate, % (FCC) Product Data* EMI13.1 K <SEP> and <SEP> (n) <SEP> 1% <tb> at <SEP> stated <SEP> solution <SEP> 0.3% <tb> pencentager <SEP> 0.1% <tb> EMI13.2 Example <tb> 1 <SEP> 2 <SEP> 3 <SEP> 4 <tb> 0.053 <SEP> 0.052 <SEP> 0.051 <SEP> 0.05 <tb> 5.2 <SEP> 5.2 <SEP> 5.36 <SEP> 5.6 <tb> 24.4 <SEP> 22.6 <SEP> 32.21 <SEP> 30 <tb> 4.82 <SEP> 3.4 <SEP> 5.37 <SEP> 4.95 <tb> 4:1 <SEP> 5.65:1 <SEP> 5:1 <SEP> 5: :1 <tb> 42099 <SEP> 431330 <SEP> 41310 <SEP> # <SEP> 5393 <SEP> 51200 <tb> <SEP> (0.13) <tb> 21.0 <SEP> 22.2 <SEP> 20.2 <SEP> 24.3 <tb> 0.6 <SEP> 0.6 <SEP> 0.3 <SEP> 0.3 <tb> 9691(0.17) <SEP> 17102(.09) <SEP> 13234(0.08) <SEP> 12077(0.19) <tb> 1320(0.26) <SEP> 1384(0.24) <SEP> 736(0.35) <SEP> 646(0.37) <tb> 63(0.55) <SEP> 100(0.5) <SEP> 67.9(0.56) <SEP> 68 <tb> *K = consistency index (in m Pasn); n=flow behaviour index. TABLE 2 Continued. Dilution rate, h-1 Cell concentration E540, gl-1 Cell dry weight Polymer: cell ratio Broth rheology(K(n)), cp Oxygen uptake, mmol l-1 h-1 Pyruvate, % (FCC) Product Data* EMI14.1 K <SEP> and <SEP> (n) <SEP> 1% <tb> at <SEP> stated <SEP> solution <SEP> 0.3% <tb> percentage <SEP> 0.1% <tb> EMI14.2 Example <tb> 1 <SEP> 2 <SEP> 3 <SEP> 4 <tb> 0.043 <SEP> 0.042 <SEP> 0.044 <SEP> 0.04 <tb> 3.88 <SEP> 4.6 <SEP> 5.34 <SEP> 3.8 <tb> 19.70 <SEP> 26.8 <SEP> 27.6 <SEP> 24.02 <tb> 2.25 <SEP> 3.0 <SEP> 3.6 <SEP> 2.6 <tb> 7.76:1 <SEP> 7.6:1 <SEP> 6.9: :1 <SEP> 8.2 <tb> 24139 <SEP> 35124 <SEP> 28796 <SEP> 34526 <tb> (0.14) <SEP> (0.2) <SEP> (0.22) <SEP> (0.17) <tb> 16.75 <SEP> 10.7 <SEP> 15.84 <SEP> 18.4 <tb> 3.4 <SEP> 7.0 <SEP> 5.4 <SEP> 6.2 <tb> 8567(0.18) <SEP> 11204(0.14) <SEP> 10450(0.14) <SEP> 11208 <tb> <SEP> (0.15) <tb> <SEP> 459(0.41) <SEP> 621(0.35) <SEP> 691(0.35) <SEP> 692 <tb> <SEP> (0.36) <tb> 43(0.60) <SEP> 46(0.60) <SEP> 63(0.55) <SEP> 62 <tb> <SEP> (0.55) <tb> *K = consistency index (in m Pasn); n= flow behaviour index.

Claims: 7. A process of claim 6 wherein the complex organic material supplies no more than 0.012 ppm ZN, MN, CO, and CU and no more than 0.02 ppm FE to the medium. 8. A process of claim 4 wherein the organism is X. campestris. 9. A process of claim 8 wherein the organism has the identifying characteristics of X. Campestris ATCC 13951. 10. A process of claim 4 further comprising isolation of the low pyruvate xanthan gum followed by purification and clarification of said gum by treatment with acid or alkali and/or with an enzyme. 11. A process for the recovery of crude oil from an oil-bearing subterranean formation comprising injecting into said formation through one or more injection wells a mobility control solution comprising an effective amount of low pyruvate xanthan gum. CLAIMS; l. Low pyruvate xanthan gum which comprises 0.1 to lç by weight pyruvate (FCC method). 2. A xanthan gum of claim 1 which comprises 0.3 to a.62 by weight pyruvate. 3. A xanthan gum of claim 1 which comprises about 0.1 by weight pyruvate. 4. A process for preparing low pyruvate xanthan gum which comprises aerobically fermenting an organism of the genus Xanthomonas in a broth comprising: 1) a chemically defined simple salts medium comprising sources of nitrogen, sulphur, potassium, phosphorus, magnesium, calcium, and (optionally) iron, said simple salts medium being substantially free of cobalt, copper, manganese, zinc, and boron; 2) an assimilable carbon source, and 3) a complex organic material which is a nitrogen source. 5. A process of claim 4 which is a continuous process, has a conversion efficiency of greater than 44%, and produces a broth with a xanthan gum: cell ratio by weight of at least 4:1. 6. A process of claim 5 wherein the complex organic material is a yeast extract or a leguminous product

Inventors: JARMAN, TREVOR RODNEY, PACE, GARY WILLIAM
Applicants: KELCO BIOSPECIALTIES LIMITED
Application year: 1982
Main classification: C12P19
IPC codes: E21B43, C08B37, C09K8, C12P19, C12R1