PRECIPITATION OF XANTHAN GUM

Abstract: Xanthan gum is precipitated from the aqueous so­ lution by adding to said solution an effective amount of a precipitating agent which comprises a subprecipitant amount of divalent cations and a subprecipitant amount of an organic solvent.

Description: Precipitation of xanthan gum The present invention relates to the recovery of xanthan gum by precipitation. Xanthan gum is an anionic exocellular polysaccharide produced during fermentation of carbohydrates by Xanthomonas campestris and other bacteria of the genus Xanthomonas. The gum is manufactured on an industrial scale, and is used, for example, as a thickener in foods and as a viscosity control agent during secondary recovery of oil. Fermentation of a xanthan-producing micro-organism on a continuous or batch basis gives a viscous broth or beer containing the desired gum. Various techniques are available for recovering the xanthan gum from the broth, with precipitation being by far the commonest technique. The methods for precipitating xanthan gum from aqueous solution include: precipitation using an organic solvent which is a nonsolvent for xanthan gum, for example by addition of acetone, methanol or isopropanol; precipitation at alkaline pH of a calcium or other divalent metal salt of the polymer; precipitation at acid pH of an aluminium salt of the polymer; or precipitation as a quaternary ammonium salt of the polymer. The most favoured method for the recovery of xanthan gum is precipitation using about 45 to 60% by weight of azeotropic isopropanol added to the broth. This then gives xanthan gum as a salt of the cations already present in the broth. Thus, the typical xanthan gum product is predominantly a mixed salt with potassium and sodium. In order to reduce the amount of isopropanol required to bring about precipitation, it has been proposed to add potassium or sodium chloride along with the isopropanol. However, this proposal does not seem to have been adopted, possibly since chloride ion is corrosive when used in conventional stainless steel equipment, and azeotropic isopropanol without added electrolyte has continued to be the precipitating agent of choice. According to the present invention, there is now provided a process for recovery of xanthan gum, wherein a salt of a divalent cation and an organic solvent are added to xanthan gum solution to precipitate the gum. In the present process, divalent cations are added in an amount that of itself is insufficient to cause precipitation of the gum at the prevailing pH, temperature and other conditions. Equally, the organic solvent, a nonsolvent for xanthan gum, is added in an amount that of itself is insufficient to cause precipitation of all the gum under the nrevail ing conditions. However, acting together, the divalent cations and organic solvent can cause precipitation of substantially all the gum as a manageable hard precipitate. Thus, the present invention is based on the discovery that an effective precipitating agent for precipitating xanthan gum can comprise a sub-precipitant amount of divalent cations together with a sub-precipitant amount of organic solvent. The preferred divalent cations are of an alkaline earth metal, especially calcium, though other divalent cations can be used, for example zinc. Xanthan gum broth typically contains 1 to 3X gum and has a pH of 6 to 8; a suitable sub-precRpftant amount of divalent cations will usually then be from 0.005 to 1, preferably 0.01 to 0.1 g equivalents/litre(N). More generally, for any xanthan gum solution, a suitable amount of divalent cations can be found by experimentation, for instance as described in the Examples below. The preferred organic solvent for the present process is isopropanol, i.e. propan-2-ol, often referred to as IPA. A suitable sub-precipitant amount of IPA is typically less than two volumes of IPA for each volume of solution, with from 0.8 to 1.8 volumes per volume being preferred. These ratios are quoted on the basis that the IPA is an industrial grade of aqueous IPA containing about 82 w/w IPA. Other grades of IPA, including 100% IPA can be used, with due allowance being made in the volume per volume figures given. The diluent organic solvent need not be IPA. For example, the present process can employ methanol or other alkanols, or acetone or other ketones. These solvents can now be employed in sub-precipitant amounts for the present purposes, with the solvent: broth ratio typically being 2:1 or less. In practice the bivalent cations will usually be added to the xanthan gum solution before the isopropanol. Preferably, the solution contains 1 to 3% of the gum, with the solution typically taking the form of a fermented broth. If desired, the solution may be subjected to a heat treatment before, during or after the steps constituting a recovery process embodying the present invention. Heat treatments in general improve the xanthan gum product, but heat treatment before or during the recovery process of the invention can offer the additional benefit of a further reduction in the amount of organic solvent which is required. Suitable heat treatments include, for example, holding the solution at 100 to 130 C for 1 to 15 minutes say at about 125 C for about 2 minutes. The gum precipitated by the present process can be separated in a conventional manner e.g. by decantation, and further treated as desired e.g. to remove excess solvent from the gum and/or to inprove the granularity of the gum. Techniques for these and other treatments are known per se and further details are unnecessary. By adoption of the present process it is possible to achfeve an efficient recovery of xanthan gum using less organic solvent than would be required without addition of the divalent cations to the solution. Furthermore, less organic solvent is employed than would be required with addition of sodium or potassium chloride or other source of monovalent cations. The present invention is illustrated by the following non-I imiting examples: For the Examples the following experimental procedure was employed. 2.5 to 3X xanthan gum broths from laboratory fermentattons using Medium A or B of Table 1 were used either before heat-treatment (NHT) or after heat treatment (HT) at 125- C for 2 minutes. Table 1 - Media Composition MEDIUM A MEDIUM B Ion (low phosphate) (low citrate) equivs/l equivs/l H+ 1.131 x 10-2 5.710 x 10-3 NH 4+ 2.906 x 10-2 2.906 x 10-2 K+ 5.601 x 10-4 1.117 x 10-2 Mg2+ 3.481 x 10-3 3.266 x 10-3 Ca2+ 7.006 x 10-4 7.006 x 10-4 OH- 4.181 x 10-3 3.408 x SO42- 5.601 x 10-4 5.582 x 10-4 HPO42- 2.906 x 10-2 4.023 x 10-2 citrate 3- 1.131 x 10-2 5.710 x 10-3 Increasing volumes of 1 M solutions of various salts, (Ca(NO3)2, MgSO4, Na2SO4, Al(N03)3), were added and well mixed with a high-speed stirrer into a series of 50 g al iquots of broth in 250 ml beakers. Each broth sample was then titrated and well mixed with 99% w/w isopropanol from a 250 ml burette up to the point where a hard precipitate was formed. Where indicated, the titration data were plotted in the form of graphs of the per cent by weight of IPA in the water versus the logarithm of the normal ity of the added cation in the broth before alcohol addition. The calculated 82% IPA : broth (V/v) ratios are included on a separate scale (where the broth volume does not include the volume of the added salt solutfon). Examples 1 and 2 Figure 1 shows the curves for: (El) NHT broth (Medium A) + Ca(N03)2 (E2) NHT broth (Medium B) + Ca(N03)2 The results show that the quantity of IPA required to precipitate both NHT broths decreases very sharply over a concentration range of Ca(N03)2 introduced to the broth extending from 2 x 102 to 2 101 N (f.e. 2.36 to 23.6 gel 1 Ca(N03)2.4H20 or 1.64 to 16.4 gel 1 anhydrous Ca(N03)2). To put this in perspective, the normality of the polyanion was calculated based on a polymer concentration of 25 to 30 gull1 a degree of pyruvylatfon x of 0.66, and an equivalent weight of the polyanion taken from the equation, E.W. of the polyanion = 865 + 69x 1 1 x The calculated normal ity falls in the range 4.5 to 5.5 x 10-2 N which occurs in the centre of the linearly declining @ section of the graph. The curves seem to plateau at high concentration of added Ca(N03)2(above 2 x 10-1N) indicating a constant minimum level of IPA to precipitate the gum irrespective of further salt addition. Examples 3 to 5 and Comparison Example 1 Figure 2 shows the curves for: (E3) NHT broth (Medium A) + Ca (NO3)2 (E4) NHT broth (Medium A) +MgS04 (ES) HT broth (MediumA ) + Ca(NO3)2 (CE1) HT broth (MediumA ) + NaO4 where 'E' and 'CE' stand for 'Example' and 'Comparative Example' respectively. The main features of interest from Fig. 2 are as follow: (a) xanthan broth requires less IPA for precipitation after heat treatment (b) Comparison of the two heat treated broths (E5) and (CE1) shows the exceptional improvement obtained using a divalent metal ion, calcium a in comparison with a monovalent metal ion, sodium. For example, at 0.3N, the calcium requires about 0.7 volumes of IPA, whereas the sodium requires about 1.05 volumes of IPA. (c) Ca(NO3)2 is more effective in reducing the IPA requirement for precipitation than Na2S04 or MgSO4. This is not only so in terms of the reduction of IPA per unit concentration of added salt but also the maximum possible saving in IPA use is greater when Ca(N03)2 is used. The latter observation may be due to the fact that Na 2S04 exceeds its solubility limit in IPA water mixtures before a sufficient concentration can be reached where the maximum IPA reduction is attained. The optimum level of Ca(N03)2 addition for heat-treated broth is 1;82 x 10 1 N which is somewhere between 3.3 and 4 times the normal ity of the polyan ion. (d) The effect of MgSO4 appears to be intermediate between that of Ca(N 3)2 and No 004. Example 6 NHT broth (Medium A) was made 10-3 N in Ca(NO3)2 and then heat-treated. The IPA required to precipitate this broth as a function of the total added Ca(N03)2 (before and after heat treatment) is shown in fig. 3 in comparison with the corresponding data obtained for HT broth + Ca(N03)2. The results establish that the addition of a small quantity of Ca(NO3)2 prior to heat treatment of broth has no special effect in enhancing the ion-binding affinity of Ca2+ ions. The IPA added salt concentration profile remains essentially the same as that obtained for addition of all the salt after heat-treatment. Comparison Example 2 Al (NO3)3 addition was investigated with NHT (Medium B) broth at 0.143 N Al3+ This created a very viscous and sticky mixture even before alcohol was introduced. When the alcohol concentration reached as little as 33.5% W/W in water clear rather glassy floccules were produced but these failed to harden into a manageable precipitate on addition of further IPA. Examples 7 to 9 and Comparison Examples 3 to 5 In a similar manner to the preceding figures, Figure 4 shows the curves for (E7) HT broth + 3N Ca(OAc)2 (E8) HT broth + 5N Ca(NO3)2.4H20 (E9) HT broth + 5N MgSO4e 7H20 (CE3) HT broth + 1Nx K2S04 (CE4) HT broth + 2N Na2SO4 (CE5) HT broth + 5N A12(S04)3.16H20 Among other features it will be seen that: (a) The calcium salts give the best reduction in IPA, with the nitrate being better than the acetate. (b) The potassium and sodium salts are intermediate between the divalent and trivalent salts in efficacy. (c) All but the calcium salts lead to non-fibrous precipitates. (d) Magnesium gives the most reduction in IPA at lower concentrations before the curves fall away. (e) The curves for Ca(N03)2 and Ca(OAc)2 both start dropping steeply at a relatively high concentration compared with other metal cations. Consequently, MgS04 is a good choice if only a small reduction in IPA is required.

Claims: CLAIMS 1. In a process for precipitating xanthan gum from aqueous solution, the improvement which comprises adding to said solution an effective amount of a precipitating agent which comprises a subprecipitant amount of divalent cations and a subprecipitant amount of an organic solvent. 2, The process of Claim 1, wherein the divalent cations are of zinc. 3. The process of Claim 1, wherein the aqueous solution is xanthan gum beer, the divalent cations are of an alkaline earth metal, and the organic solvent is an alkanol or ketone. 4. The process of Claim 3, wherein the solvent is isopropanol, methanol, or acetone. 5. The process of Claim 3, wherein the alkaline earth metal cations is of calcium or magnesium. 6. The process of Claim 3, wherein the beer contains 1 to 3% xanthan gum and has a pH of 6 to 8, the organic solvent is isopropanol, and the divalent cations are present in the amount d.005 to 1 (preferably, 0.01 to 0.1) g equivalents/litre. 7. The process of Claim 3, wherein the volume:volume ratio of solvent:beer is 0.8-1.8:1 when the solvent is 82 w/w% IPA and less than 2:1 when the solvent is methanol or acetone. 8. The process of Claim 1 further comprising heat treating said solution. 9. The process of Claim 8, wherein the heat treatment occurs before or during the addition of said precipitation agent and comprises holding said solution at 100 to 130eC for 1-15 minutes, preferably 125eC for 2 minutes.

Inventors: SMITH, IAN HUMPHREY
Applicants: KELCO BIOSPECIALTIES LIMITED
Application year: 1982
Main classification: C12P19
IPC codes: C12P19, C08B37, C12R1