GB2043100A - Improved process for the production of single cell protein - Google Patents

Abstract

A process for the production of prokaryotic, particularly bacterial, single cell protein includes a step in which whole and/or ruptured micro- organism cells are treated with an oxidising agent or are subjected to other oxidising means. The preferred oxidising agent is hydrogen peroxide. The product of the process has a number of advantages over known prokaryotic single cell protein, most important being that its use alleviates difficulties of reduced feed intake, reduced live weight gain, poor feed conversion ratios and liver damage experienced when single cell protein is fed to domestic fowls in high dietary inclusions.

Description

SPECIFICATION Improved process for the production of single cell protein This invention relates to an improved process for the production of single cell protein (SCP).

Proteinaceous materials are important dietary components for many animals. A wide variety of such materials are in use including for example fish meal, soya bean meal and materials derived from rape seeds and sunflower seeds. In the past twenty years considerable research effort has been devoted to the production of yeast and bacterial proteins for inclusion in animal diets.

Such proteins derived from micro-organisms are commonly referred to as single cell protein or SCP.

The inclusion of high proportions of some widely used proteinaceous materials in their diets can have adverse effects upon certain species. This is frequently ascribed to "toxic" constituents. The effect of these constituents has been recently reviewed (Toxic Constituents of Plant Foodstuffs, Ed. I.E. Liener, Academic Press, New York). Leiner (1969, pages 4-6) refers to toxic constituents as substances that produce deleterious effects when fed to men or animals. He distinguishes between chemical constituents that are lethal and those that produce an adverse physiological response. Processing, or "other means of preparation have proved to be effective in destroying many toxic constituents".Reference is also made to Altshul A.M., (1967, Science, 158, 221) that if it "were not for the fact that such oilseeds as soyabeans and cotton seed can be processed so as to inactivate their toxic constituents, these rich sources of plant protein would not occupy such a position of importance as they now command in the feeding of farm animals".

It is known that the feeding of single cell protein derived from prokaryotic micro-organisms, which include bacteria and blue-green algae, to certain animal species, particularly domestic fowls' in high dietary inclusions causes reduced feed intake (RFI), reduced live weight gain (LWG) and poor feed conversion ratios (FCR). In extreme instances this produces liver damagge with organ enlargement, focal necrosis with phogocytic and inflammatory cell infiltration being observable on histopathological examination. This effect has been produced with prokaryotic single cell protein derived from different micro-organisms, grown on different nutrient media and in different processes and has been reported by (i) D E Owen and S M A Doak (Fd. Cosmet.

Toxicol, 16, 633, 1978); (ii) L Farstad (Acta Agric. Scand., 27, 129, 1977) and (iii) C T Whittemore, D W Gilchrist-Shirlaw, D B McDonald and A G Taylor (British Poultry Science, 19, 283, 1978).

From experiments in which single single cell protein produced by the process described in our UK Specification No. 1 370892 was included as a proteinaceous material in normal commercial diets fed to domestic fowls, we have found progressive decreases in LWG and progressive decreases in food intake. Correlated with this is an increase in the incidence of observable liver damage as the percentage inclusion of prokaryotic single cell protein in the diets is increased.

The experiments were carried out with diets containing 0%. 2.5%. 5%, 7.5%, 10%, 15%, 20%, 25%, and 30% of prokaryotic single cell protein produced by the process of UK Specification No. 1 370892. With low inclusions of SCP (eg 2.5%), the incidence of liver damage did not differ significantly from the incidence with diets containing no SCP. However, with high inclusions of SCP significant differences in the incidence of liver damage between SCP containing diets and non-SCP diets were observed. For instance with broiler chick diets containing non-stressful levels of crude protein, say 25%, and also non-stressful levels of vitamins and minerals, the incidence of liver damage was between 10 and 40% usually 10%.

With laying hens, fed stressful levels (30%) of crude protein, contained in diets having a 30% SCP content the incidence of liver damage was between 30 and 70%, usually 50%. We have also found that the effect upon growth performance of domestic fowls resulting from the inclusion of SCP in their diets is not affected significantly by varying the microbial culture conditions or by varying the method whereby the micro-organisms are dried to produce a dietary ingredient, i.e. freeze-, flash- and spray-dried products give similar effects.

The effect of using prokaryotic SCP as a dietary ingredient upon certain species restricts the proportions in which the SCP can be included in the diets of these species and, in consequence, reduces the utility of prokaryotic SCP in relation to these species.

According to the present invention we provide a process for the production of single cell protein which comprises cultivating prokaryotic micro-organisms and subsequently treating the cultivated micro-organisms to produce a product comprising whole non-viable cells and/or ruptured cells wherein the micro-organisms are treated with an oxidising agent or are subjected to other oxidation means, the oxidising agent being added or the other means being applied during cultivation and/or during the subsequent treatment and/or to the product after the subsequent treatment, the oxidising agent being added in an amount between 3 and 300 ml moles per litre of a solids suspension containing the micro-organisms when it is added during cultivation or during subsequent treatment, or, when added to the product, being added in an amount between 3 and 300 m moles per litre of the product moisture content.

The prokaryotic micro-organisms generally used to date in processes for the production of single cell protein are bacteria. Thus the process of the present invention is mainly of interest insofar as it relates to bacteria and will hereafter be described as a process for the production of bacterial SCP. The present invention is applicable to any process for the production of bacterial SCP. Such a process is that described in our UK Specification No. 1 370892 in which the bacteria employed are strains of the species Pseudomonas methylotropha (now known as Methylophilus methylotrophus), Pseudomonas rosea, Hyphomicrobium variabile and Microcyclus polymorphum.A number of strains of these species have been deposited at the following culture collections: (a) National Collection of Industrial Bacteria (NCIB), Torrey Research Station, Aberdeen Scotland, UK; (b) US Department of Agriculture (NRRL), Peoria, Illinois, USA; (c) Fermentation Research Institute (FRI), Japan; and have been assigned the following accession numbers: NCIB Nos. 10508-10515; 10592-10596; 10516; 10517; 10597-10612.

NRRL Nos. B5352-B5359; B5360-B5364; B5381; B5382; B5365-B5380.

FRI Nos. 1215-1222; 1223-1227; 1228; 1229; 1230-1245.

The characteristics of the above four species and the particular strains listed are given in our UK Specification No. 1 370892. Of the species specifically mentioned above Pseudomonas methylotropha (Methylophilus methylotrophus) is especially preferred. Among the specific strains listed above this species is represented by strains NCIB Nos. 10508-10515 and 10592-10596.

The process of this invention may be a batch or a continuous process preferably it is a continuous process. In a continuous process a culture of micro-organisms is grown in a fermenter and an aqueous suspension containing microbial cells is continuously withdrawn and subjected to a series of treatment steps to concentrate the suspension before it passes to a drier.

In a typical process sequence the suspension leaving the fermenter is subjected to the following steps before passing to a drier: (i) a flocculation step, eg involving heating and acid treatment as described in our UK Specification No. 1 381 306; (ii) a separation step or steps to separate the bulk of the liquid from the microbial cells, separated liquid may be returned to the fermenter while a concentrated suspension often termed "drier feed cream passes to the drier.

The cells may be treated with the oxidising agent at any stage in the process. However in choosing the stage at which to perform treatment the following factors are relevant: 1. The oxidising agent employed may be toxic to living micro-organisms and thus have deieterious effects upon a growing culture; 2. Many oxidising agents are degraded and wholly or partially de-activated by enzymes such as peroxidases and catalase which are present in most bacteria; 3. The amount of oxidising agent required depends upon the volume of liquid associated with the cells and thus the invention is more economically applied by adding the oxidising agents to concentrated suspensions or to the product; 4.Treatment with oxidising agent is preferably carried out at temperatures between 10 and 140 C, especially between 50 and 80or, a temperature of 60"C being particularly preferred; 5. The pH at which treatment with oxidising agents is carried out is preferably in the range pH 7.0-9.0, particularly in the range 7.5-8.5 with pH values of 8.0 to 8.5 being most suitable. Lower pH values are acceptable but the oxidation conditions are altered. Equally higher pH values are also acceptable but in this instance decomposition of some oxidising agents tends to occur to an exhanced extent making treatment less effective.Additionally lysed and flocculated cells react in high pH conditions to produce a highly viscous fluid which is difficult to mix.

Taking account of the above considerations addition of the oxidising agent to a growing culture is not preferred because of problems caused by the action of the oxidising agent on a growing cell and by its degradation by catalase peroxidase. After cell lysis and suspension concentrated catalase degradation is minimal and the solids concentration is high. Thus, it is preferred to treat the cell suspension with the oxidising agent shortly before the suspension passes to the drier, ie to treat the drier feed cream. Alternatively the product from the drier may be treated with the oxidising agent. Although this product tends to be referred to loosely as dried cells, there is in fact a measurable proportion of water associated with the "dried" cells typically 10% (w/w). Thus if the oxidising agent is added in an amount of 3 to 300 m moles per litre of the product moisture content, this can be calculated as follows: Typical ' "dry" product contains 10% moisture = 100 mls water/kg.

Therefore add 3-300 m moles oxidising agent per 10 kg product.

When the product is treated with certain oxidising agents further process steps may be required in order to remove traces of the oxidising agents from the final product.

Suitably the oxidising agent is one which is pure, leave no toxic residues and does zero or minimal damage to the nutritional quality of the product. The preferred oxidising agent is hydrogen peroxide. Other suitable oxidising agents include organic peroxides, inorganic peroxides, ozone and permanganate. Other suitable oxidising means may include electrolytic processes.

The preferred amount of oxidizing agent to be added varies to some extent depending upon the pH at which addition takes place. However a preferred range of amounts effective at a variety of pH values is from 30 to 1 75 m moles, particularly 70 to 1 50 m moles, per litre of a solids suspension or per litre of the product moisture content. In the studies we have made we have found the greatest effect with minimal oxidation when adding the oxidising agent in an amount of 86 m moles per litre.

The duration of the treatment with the oxidising agent is suitably within the range of 1 to 300 minutes, 10 to 40 minutes and particularly 30 minutes being preferred.

Using the process of the invention a product is obtained which has a number of advantages over previously known prokaryotic SCP. Most importantly use of this product alleviates the difficuSties of reduced feed intake, reduced live weight gain and poor feed conversion ratics experienced with domestic fowls and reduces the incidence of liver damage when the product is fed at high dietary inclusions. In addition the product has improved colour and improved dispersion properties which are important when it is used for feeding young animals, eg veal calves. These advantages increase the utility of prokaryotic SCP generally.

Ths invention is illustrated by the following Examples: EXAMPLE 1 In a series of large-scale trials male and female chicks and laying hens were fed diets containing Methylophilus methylotrophus (Pseudomonas methylotropha) single cell protein in some instances untreated and in others treated with hydrogen peroxide by the process of the present invention.

During production of the treated single cell protein used, cell lysate (ie drier feed cream) having a solids content of 18% (w/v) was treated with quantities of concentrated hydrogen peroxide solution (12% w/v) such that the initial concentrated of hydrogen peroxide in the cream was between zero and 1 75 mM. After mixing the hydrogen peroxide with the cream, the treated cream was held at a temperature of 60"C and at pH 7.0 for 30 minutes prior to drying by flash drier.

Typical results, for birds fed diets containing treated and untreated single cell protein and for birds fed diets in which single cell protein was replaced by alternative proteinaceous materials, are given in Table 1. Fig. 1 is a graph of the occurrence of gross observable liver damage (per cent of the test population) against the concentration (mM)* of hydrogen peroxide in the drier feed cream for laying hens (plot A), female chicks (plot B) and male chicks (plot C). Plots A, B and C are linear regression analyses of all chick and laying hen data obtained in this series of trials. The incidence of lesions was highest with laying hens and least with male chicks. The graph indicates that the minimum concentration of hydrogen peroxide required to reduce liver damage in chicks and laying hens effectively to zero levels is 114 mM.In our tests on birds fed diets containing alternative proteinaceous materials a number of birds exhibited liver damage.

TABLE 1 liver damage in liver damage in liver damage in laying hens male chicks female chicks single incidence total incidence total incidence total cell mM H202" ie % of no. of ie % of no. of ie % of no. of protein in drier birds birds birds birds birds birds in diet feed developing in developing in developing in (% w/w) cream damage trial damage trial damage trial 0.0 0 1.3 78 0.7 1067 - 7.5 0 - - 5.2 408 - 10.0 0 8.3 60 - - - 25.0 0 - - 15.3 144 21.0 276 30.0 0 47.1 102 - - - 25.0 35.0 - - 5.9 187 16.5 284 25.0 175.0 - - 2.0 100 0.0 93 30.0 70.0 19 42 - - - 30.0 87.5 7.1 42 - - - "In the Table and in Fig. 1 the concentration of hydrogen peroxide in m moles per litre was calculated assuming the drier feed cream to have a density of 1.0 g/cm3.

EXAMPLE 2 In a further series of large-scale trials domestic fowls were fed diets containing Methylophilus methylotrophus (Pseudomonas methylotropha) SCP, in some instances untreated and in others treated with hydrogen peroxide according to the process of the present invention. The SCP was produced in a large pilot plant using the process of our UK Specification No. 1370892. In the process bacterial cells were cultivated in a methanol-containing medium in a fermenter of our UK Specification No. 1 353008. The cell suspension leaving the fermenter was treated using the method of our UK Specification No, 1 381 306 and was concentrated to produce a drier feed cream (DFC) which was subsequently fed to a drier.

In these trials samples of DFC at pH 4 and having a 12-15 MO solids content were taken from the plant and were subjected to the following treatment steps in a laboratory to produce hydrogen-peroxide-treated material (steps 2 to 4 being omitted to produce non-hydrogen peroxide treated control material):1. add KOH/NaOH (1.68:1.00 molar ratio) to give desired pH; 2. add H2O2-see note below; 3. maintain at 60"C for 30 minutes; 4.* re-neutralize to pH 7 with H2SO4; 5. spray dry; and 6. granulate feed sample.

*In trial No. APC021J this step was found to be unnecessary.

In step 3 an amount of 12% (40 vol) hydrogen peroxide was added to the DFC. The number of millilitres of hydrogen peroxide added to 100 g of DFC is hereinafter designated as the "percentage addition" of hydrogen peroxide, i.e. 2.5 mls added to 100 g DFC gives a "2.5%" hydrogen peroxide treatmentorrnsponding to the addition of 86 m moles per litre of hydrogen peroxide.

Samples of SCP obtained as described above were included in the diets of the following fowls: (a) Broiler chicks (Ross I) fed diets containing 25% of the test sample from approximately 8 to 22 days of age.

(b) Laying hens (Light White Hybrids over 40 weeks of age) fed diets containing 30% of the test sample for 6 days.

In each of a seriels of 6 trials SCP was treated with "2.5%" hydrogen peroxide at various pH values and was included in the diets of the above fowls (4 trials with chicks and 2 with laying hens). In each case a control diet containing untreated SCP was also used. The biological data generated from these trials are summarised in the graph shown in Fig. 2. In this the ordinate is the percentage incidence of !over damage, relative to that occurring with a control diet including untreated SCP in the same trial (taken as 100%), using diets containing SCP treated with "2.5%" hydrogen peroxide. The abscissa is the pH of hydrogen peroxide treatment for the treated SCP. The different symbols on the graph represent the different trials from which the values plotted were obtained.The percentage of fowls exhibiting liver damage amongst those fed to control diet containing untreated SCP in each trial is given in Table 2.

TABLE 2

Trial No. and % incidence of symbol on Fig. 2. liver damage in control Type of fowl BC 117 22.0% chicks APC003J 32.7% chicks OAPCO16J 27.0% chicks A APC021J 14.0% chicks [7 L 32 30.0% laying hens PL4 XXV 27.8% laying hens The percentages given in Table 2 were taken as the 100% values for the graph in Fig. 2 in respect of the individual trials.

These data clearly indicate a pH optimum for such hydrogen peroxide treatment in the region of pH 8-8.5. The average percentage incidences of liver damage represented by the broken line of the graph in Fig. 2 are: Untreated Control - 25.6% DFC/2.5% H2O2 . pH 7 - 11.7% pH 7.5 - 3.6% pH 8 - 1.4% pH 8.5 - 2.3% pH 9 - 10.2% In a further trial APC024J carried out in the manner described above the level of hydrogen peroxide addition and the pH of treatment with hydrogen peroxide were both varied. The liver damage data resulting from this trial are summarised in the graph shown in Fig. 3. In this graph the ordinate is the percentage liver damage incidence, relative to that occurring when an untreated control was used (taken as 100%), using feeds containing SCP treated with varying levels of hydrogen peroxide at varying pH values. The abscissa is the pH of hydrogen peroxide treatment. These data imply that an optimum treatment lies in the range "2%" H202 at pH 8 and "2.5%" H202 at pH 8.5.

Claims (20)

1. A process for the production of single cell protein which comprises cultivating prokaryotic micro-organisms and subsequently treating the cultivated micro-organisms to produce a product comprising whole non-viable cells and/or ruptured cells wherein the micro-organisms are treated with an oxidising agent or are subjected to other oxidation means, the oxidising agent being added or the other means being applied during cultivation and/or during subsequent treatment and/or to the product after the subsequent treatment, the oxidising agent being added in an amount between 3 and 300 m moles per litre of a solids suspension containing the microorganisms when it is added during cultivation or during subsequent treatment, or, when added to the product, being added in an amount between 3 and 300 m moles per litre of the product moisture content.

2. A process for the production of single cell protein which comprises cultivating prokaryotic micro-organisms and subsequently treating the cultivated micro-organisms to produce a product comprising whole non-viable cells and/or ruptured cells wherein the micro-organisms are treated with an oxidising agent, the oxidising agent being added during cultivation and/or during the subsequent treatment and/or to the product after the subsequent treatment, the oxidising agent being added in an amount betweeen 3 and 300 m moles per litre of a solids suspension containing the micro-organisms when it is added during cultivation or during subsequent treatment, or, when added to the product, being added in an amount between 3 and 300 m moles per litre of the product moisture content.

3. A process according to claim 1 or claim 2 wherein the prokaryotic micro-organism is a bacterium.

4. A process according to claim 3 wherein the bacterium is a strain of the species Methylophilus methylotrophus.

5. A process according to claim 4 wherein the bacterium is any one of strains NCIB Nos.

10508 to 10515 to 10592 or 10596.

6. A process according to any one of the preceding claims wherein, during production of the single cell protein, a concentrated suspension of micro-organism cells is prepared and is subjected to drying means, the oxidising agent being added to the concentrated suspension before said suspension is subjected to drying means.

7. A process according to any one of claims 1 to 5 wherein the oxidising agent is added during subsequent treatment.

8. A process according to any one of the preceding claims wherein the micro-organisms are treated with the oxidising agent at a temperature in the range 10 to 140"C.

9. A process according to claim 8 wherein treatment takes place at a temperature in the range 50 to 80"C.

1 0. A process according to any one of the preceding claims wherein the micro-organisms are treated with the oxidising agent at a pH in the range 7.0 to 9.0.

11. A process according to claim 10 wherein the pH is in the range 7.5 to 8.5.

12. A process according to any one of the preceding claims wherein the oxidising agent is added in an amount in the range 30 to 1 75 m moles per litre of the solids suspension or per litre of the product moisture content.

1 3. A process according to claim 1 2 wherein the oxidising agent is added in an amount in the range 70 to 1 50 m moles per litre.

14. A process according to any one of the preceding claims wherein the duration of the treatment with the oxidising agent is in the range 1 to 300 minutes.

15. A process according to claim 14 wherein the duration of the treatment is in the range 10 to 40 minutes.

1 6. A process according to any one of the preceding claims wherein the oxidising agent is an organic peroxide, an inorganic peroxide, ozone or permanganate.

1 7. A process according to claim 1 6 wherein the oxidising agent is hydrogen peroxide.

1 8. A process for the production of single cell protein wherein micro-organisms are treated with hydrogen peroxide substantially as described herein and as shown in either of the Examples.

1 9. Single cell protein whenever produced by a process according to any one of the preceding claims.

20. A feedstuff containing single cell protein as claimed in claim 1 9.