# Patent

## Title
Film depositing apparatus and a film depositing method

## Abstract

This is a continuation of application Ser. No. 813,188 filed July 5, 1977, now abandoned which in turn is a continuation of Ser. No. 584,451, filed June 6, 1975, now abandoned; which in turn is a Rule 60 continuation of Ser. No. 440,775, filed Feb. 8, 1974 (now U.S. Pat. No. 3,937,693).

## Background
This invention is for improvements in or relating to the production of edible protein containing substances.

It has particular reference to a process for reducing the nucleic acid content of microfungi.

British Pat. No. 1,210,356 describes and claims a process for the production of an edible protein-containing substance which comprises incubating and proliferating, under aerobic conditions, an organism which is a non-toxic strain of a microfungus of the class Fungi Imperfecti, in a culture medium containing essential growth-promoting nutrient substances, of which carbon in the form of assimilable carbohydrate constitutes the limiting substrate in proliferation, and separating from the assimilable carbohydrate exhausted medium the proliferated organism which constitutes the edible protein-containing substance.

British Pat. No. 1,331,471 describes and claims a process for the production of an edible protein-containing substance which comprises incubating and proliferating, under aerobic conditions, a non-toxic strain of Penicillium notatum or Penicillium chrysogenum or a variant or mutant thereof, in a culture medium containing essential growth-promoting nutrient substances, of which carbon in the form of assimilable carbohydrate constitutes the limiting substrate in proliferation, and separating from the assimilable carbohydrate exhausted medium the proliferated organism which constitutes the edible protein-containing substance.

British Pat. No. 1,331,472) describes and claims our specific novel strain of Penicillium notatum-chrysogenum IMI 138291 and variants and mutants thereof.

British Pat. No. 1,346,062) describes and claims a process for the production of an edible protein-containing substance which comprises incubating and proliferating, under aerobic conditions, a non-toxic strain of the genus Fusarium or a variant or mutant thereof, in a culture medium containing essential growth-promoting nutrient substances, of which carbon in the form of assimilable carbohydrate constitutes the limiting substrate in proliferation, and separating the proliferated organism comprising the edible protein-containing substance.

Our British specification No. 1,346,062 contains the following disclosure:

The present invention relates to a process for the production of edible protein-containing substances and has particular reference to the production of fungal protein by microbial action.

Our Specification No. 1,210,356 relates to a process for the production of an edible protein-containing substance which comprises incubating and proliferating, under aerobic conditions, an organism which is a non-toxic strain of a microfungus of the class Fungi Imperfecti, in a culture medium containing essential growth-promoting nutrient substances, of which carbon in the form of assimilable carbohydrate constitutes the limiting substrate in proliferation, and separating from an assimilable carbohydrate exhausted medium the proliferated organism which constitutes the edible protein-containing substance.

Our copending Application No. 8977/70, Ser. No. 1,331,471, claims an edible protein-containing substance comprising fungal mycelium possessing a high net protein utilization value on rat assays of at least 70 based on the .alpha.-amino nitrogen.

It is also an object of the present invention to provide an edible protein-containing substance comprising non-toxic fungal mycelium possessing a high net protein utilization value on rat assays of at least 65 preferably at least 70 based on the .alpha.-amino nitrogen and containing a non-toxic strain of the genus Fusarium or a variant or mutant thereof. The non-toxic mycelium possessing a high net protein utilization value of at least 70 based on the .alpha.-amino nitrogen may contain a non-toxic strain of the species Fusarium graminearum.

According to the present invention there is provided a process for the production of an edible protein-containing substance which comprises incubating and proliferating, under aerobic conditions, a non-toxic strain of the genus Fusarium or a variant or mutant thereof, in a culture medium containing essential growth-promoting nutrient substances, of which carbon in the form of assimilable carbohydrate constitutes the limiting substrate in proliferation, and separating the proliferated organism comprising the edible protein-containing substance.

The separated proliferated organism comprising the edible protein-containing substance may be incorporated into a foodstuff for human or animal consumption.

The substrate employed in the incubation stage may be of vegetable origin, for example starch, starch-containing materials or products of their hydrolysis, sucrose, sucrose-containing materials or hydrolysed sucrose i.e. invert sugar or mixtures thereof. Thus the substrate may comprise hydrolysed potato, molasses, glucose, maltose, hydrolysed bean starch or cassava. Alternatively substrate of animal origin comprising whey may be employed.

The non-toxic strain of Fusarium may be a strain of Fusarium graminearum.

The preferred non-toxic strain is our strain of Fusarium graminearum Schwabe, which is described and claimed together with variants and mutants thereof in copending United Kingdom Application No. 23452/70 (Ser. No. 1,346,061), has been deposited at the Commonwealth Mycological Institute, Kew, and assigned the number IMI 145425. It is non-pathogenic to wheat.

Our copending United Kingdom Application No. 23452/70 (Ser. No. 1,346,061) also describes and claims specifically five variants of our strain of Fusarium graminearum Schwabe IMI 145425 namely I-7, I-8, I-9, I-15 and I-16 deposited with the Commonwealth Mycological Institute and assigned the numbers IMI 154209, IMI 154211, IMI 154212, IMI 154213 and IMI 154210 respectively.

The temperature of incubation is in general between 25.degree. and 34.degree. C., preferably around 30.degree. C.

Inoculation resulting in commencement of the process is carried out by a pregerminated seed stage comprising for example from 2% to 10% of inoculum, usually in the range 5% to 10% of inoculum based on final fermented operating volume.

The pH of the substrate medium during incubation is preferably kept within a suitable range supporting maximum growth, for example, between 3.5 to 7.

The period of growth in batch culture under the abovementioned conditions is usually found to range from 20 to 48 hours. In both batch and continuous processes aeration and agitation should be carried out to provide a sufficient level of dissolved oxygen to overcome deficiency which can be a limiting growth factor.

As will be well understood by those skilled in the art sufficient quantities of essential growth nutrients such as nitrogen, sulphur, phosphorus and other trace elements are maintained in the substrate medium so that growth of the substrate is limited only by the carbohydrate available to the fungus.

In addition to the nutrients stated above the presence of one or more vitamins such as for example biotin may be desirable to maintain maximum growth rate.

It is also desirable to add a non-toxic anti-foaming agent to the substrate medium to control foaming during the fermentation.

The substance produced according to the present invention may be isolated in any suitable manner known in the art. Thus the resulting mycelium may be recovered by separation, washing, filtration and drying. In this connection, however, it has been found that if the moisture content of the substance is reduced below a critical level of about 50% (w/w) by filtration under pressure the subsequent drying methods employed are not subjected to such stringent temperature limitations which is an important factor in the economic processing of these materials. The method of drying must not cause damage to the nutritional value of the mycelium and may be drying in a current of air at 75.degree. C. or freeze drying.

The fungal mycelium produced by the process of the present invention shows very good water-binding capacity and may be useful as a thickening and gelling agent. Not being an isolate, it retains its vitamins as well as other nutritionally available materials such as lipids and some carbohydrates. Fungal mycelium has satisfactory baking characteristics which are of value in protein enriched breads, breakfast foods and food snacks. The fungal mycelium, because of its filamentous structure, can be baked, fried or puffed and presented to many communities as a food comparable in appearance and acceptability with conventional foods which they are accustomed to eating.

Following is a description by way of example of method of carrying the invention into effect.

Culture medium or medium percentages given are as weight per unit volume (w/v) or volume per unit volume (v/v) for solids and liquids respectively. ##EQU1## .mu.max. is the growth rate constant (the maximum value of .mu. at saturation levels of substrate).

Examples 1-4 are of batch culture.

10 Liters of the following culture medium were prepared and sterilized as described in a stirred fermenter vessel. Cane molasses to provide 6% w/v sugar Ammonium sulphate     1.2% NaH.sub.2 PO.sub.4    0.25% Sterilized 30 minutes 15 psig CaCO.sub.3            0.5% w/v Sterilized 3 hours    15 psig ______________________________________

The medium components were added aseptically and attemperated to 30.degree. C. An inoculum equivalent to 5-10% by volume of the culture medium and grown either on a glucose/corn steep liquor medium or other suitable materials in shake flasks was inoculated with a spore suspension of the organism comprising our strain of Fusarium graminearum Schwabe IMI 145425, for 18-24 hours at 30.degree. C. on a rotary shaker, and added aseptically to the fermenter.

The fermenter incubated at 30.degree. C. was then stirred at 800 rpm with a 6 bladed disc turbine (C.5D) in a full baffled vessel and 1 VVM of sterile air passed through. After 35 hours, the grown mycelium was removed from the fermenter, centrifuged, washed with water and dried in a warm air band drier, air temperature 75.degree. C.

The dried product had the following composition: Total Nitrogen 8.0% Ash            5.3% Liquid         2.7% NPUop.         52     based on Total Nitrogen ______________________________________

10 Liters of the following culture medium were prepared and sterilized as described, in a 14 liter New Brunswick, Microferm, fermenter. Final % ______________________________________ Solution 1 Glucose         pH 3.0  3.0 Solution 2 Ammonium sulphate       0.7 Solution 3 Potassium di-hydrogen pH 5.0  1.0 phosphate Solution 4 FeSO.sub.4 7H.sub.2 O pH 2.5  0.001 MnSO.sub.4 4H.sub.2 O   0.0005 CuSO.sub.4 5H.sub.2 O   0.0001 MgSO.sub.4 7H.sub.2 O   0.025 Solution 5 Na.sub.2 MoO.sub.4 2H.sub.2 O 0.0001 CoCl.sub.2 6H.sub.2 O   0.0015 Solution 6 NaOH                    0.1 ______________________________________

All the above solutions were sterilized by heat for 15 minutes at 15 psig.

Solution 7 Vitamins and/or amino acids as described below sterilized by filtration.

The solutions were added aseptically to the vessel.

An inoculum was grown and added as in Example 1 except tha the final concentration in the fermenter was adjusted so as to provide 0.5 gm/l dry wt. of mycelium.

The conditions of growth were temperature 30.degree. C.; aeration 1 VVM, stirrer speed was adjusted to maintain a level of dissolved oxygen above 25% of the saturation value in the culture medium, measured by a New Brunswick Inc. DO probe. Sterile antifoam, polypropylene glycol 2000, was added as required to suppress foam and pH was maintained between 6.0-6.3 by the addition of sterile potassium hydroxide solution. Growth rates (hr..sup.-1) ______________________________________ (i)   Omitting solution 7 (Minimal medium) very slow (ii)  Solution 7 such that the final con- 0.2 centration of Biotin in the culture medium was 50 .mu.g/l (iii) Solution 7 such that the final con- 0.25 centration of Biotin in the culture medium was 50 .mu.g/l; Choline chloride 30 mg/l and Methionine 300 mg/l ______________________________________

Medium and conditions were as in Example 2, but the glucose was replaced with maltose. (i)       Solution 7 as Example 2 (ii) 0.18 (ii)      Solution 7 as Example 2 (iii) 0.21 ______________________________________

100 Liters of the following culture medium were prepared and sterilized as described in a 130 l stainless steel fermenter. % Final concentration ______________________________________ Glucose             4.0 Corn steep liquor (50% Total Solids) 0.8 Ammonium sulphate   0.2 Potassium di-hydrogen phosphate 0.2 Mg SO.sub.4 7H.sub.2 O 0.025 Zn SO.sub.4 7H.sub.2 O 0.0005 Fe SO.sub.4 7H.sub.2 O 0.0005 Mn SO.sub.4 4H.sub.2 O 0.0001 ______________________________________

The medium was sterilized at pH 3.0 at 15 psig for 30 minutes and on cooling to 30.degree. C. adjusted to pH 5.0 by the sterile addition of ammonia.

Biotin sterilized by filtration to give 40 .mu.g/l final concentration, was added aseptically.

The vessel was inoculated with B 10 liters of culture grown in a sparged vessel, for 18 hours, at 30.degree. C., on a medium containing: Glucose 2%; tryptone ("Oxoid") 0.4%; yeast extract ("Oxoid") 0.1%; ammonium sulphate 0.15%; potassium di-hydrogen phosphate 1%; sodium hydroxide 0.1%; magnesium sulphate 0.025%; ferrous sulphate 0.001%; zinc sulphate 0.001%; manganese sulphate 0.0005%; copper sulphate 0.001%; anti-foam, polypropylene glycol 2000 0.05%, and sterilized for 45 minutes at 15 psig, inoculated with a spore suspension of our organism Fusarium graminearum Schwabe IMI 145425. The word "Oxoid" is a Registered Trade Mark.

The conditions for growth were temperature 30.degree. C., aeration adjusted to provide dissolved oxygen concentrations above 10% of the saturation value for the culture broth. Sterile antifoam, polypropylene glycol 2000, was added to suppress foaming, and the pH was maintained at 5.0 by means of sterile ammonia additions. Samples of the mycelium were taken at intervals over the period of batch culture, filtered, washed with water and dried. On dry weight basis analysis gave Total nitrogen 8.0-8.6%; .alpha.-Amino nitrogen 6.4-6.6%. The initial growth rate in this complex medium derived from both the batched culture medium and inoculum was approximately 0.3 hr..sup.-1.

The following examples 5 and 6 are of continuous culture.

Culture medium of the following composition was prepared: Final % ______________________________________ Solution 1 Glucose                  3.0 Ammonium sulphate        0.25 Potassium di-hydrogen phosphate 0.3 Magnesium sulphate       0.025 Anti-foam, polypropylene glycol 2000 0.01 Sterilized at pH 3.0 for 30 minutes at 15 psig Solution 2 MnSO.sub.4 4H.sub.2 O    0.0005 FeSO.sub.4 7H.sub.2 O    0.0005 ZnSO.sub.4 7H.sub.2 O    0.0005 CoCl.sub.2 6H.sub.2 O    0.0001 CuSO.sub.4 5H.sub.2 O    0.0001 Na.sub.2 MoO.sub.4 2H.sub.2 O 0.0001 Sterilized 15 minutes at 15 psig ______________________________________

Vitamins and/or amino acid as described below sterilized by filtration.

All solutions were added as necessary, aseptically. In 8.5 liter chemostat the conditions of growth were as follows:

Temperature 30.degree. C.; aeration IVVM; agitation 800 rpm; single 6 bladed disc turbine 0.5 D in fully baffled vessel. Organism, our strain of Fusarium graminearum Schwabe IMI 145425.  The pH maintained at 5.0 by automatic addition of sterile ammonia.

Samples were taken, filtered, washed with water and dried. .mu. Max. Yield Mycelium  NPU based NPU based hr..sup.-1 factor TN % AN % on TN on AN __________________________________________________________________________ (i) Solution 3 such that the final 0.17-0.19 0.5 7.2 to 7.9 6.3 to 6.8 54    65 concentrate of Biotin in the culture medium was 20 .mu.g/l (ii) Solution 3, such that the final 0.20-0.21 0.5 7.7 to 8.6 6.1 to 6.5 59    78 concentration of Biotin in the culture medium was 20 .mu.g/l and of methionine was 600 mg/l __________________________________________________________________________

Culture medium of the following composition was prepared: Bean starch (.alpha.-amylase treated) 3.0    carbohydrate Corn steep liquor      1.33 Ammonium sulphate      0.25 Potassium di-hydrogen phosphate 0.15 Magnesium sulphate     0.025 Antifoam polypropylene glycol 2000 (v/w) 0.025 Sterilized pH 4.0 for 30 minutes at 15 p.s.i.g. ______________________________________

The medium was fed to the 8.5 liter chemostat under the same conditions as in Example 5 except that the pH was varied between 3.5 and 6.0 and growth rate throughout 0.1 hr.sup.-1. Samples were taken, filtered, washed with water and dried. The following result was obtained: TN   AN     NPU based NPU based %    %      on TN     on AN ______________________________________ Product grown at pH 4.0 7.8    6.6    54      67 Product grown at pH 5.0 8.6    7.1    57      71 Product grown at pH 6.0 7.7    5.9    61      80 ______________________________________

The culture medium and conditions were as in Example 6 except that the pH was held at 5.0 throughout the run and the temperature was varied between 26.degree. and 34.degree. C. The optimum temperature was found to be 30.degree.-32.degree. C.

Examples 7 to 11 describe the fermentation of five variants or isolates of Fusarium graminearum Schwabe IMI 145425.

Duplicate shake flasks of 1-liter capacity were prepared containing 200 mls. of the following medium: Final concentration % ______________________________________ Solution 1 Glucose (sterilized 3.0 separately pH 3.0 10 p.s.i./10 min.) Solution 2 Ammonium sulphate 0.565 Potassium Dihydrogen 1.0 Phosphate MgSO.sub.4 :7H.sub.2 O 0.025 FeSO.sub.4 :(NH.sub.4).sub.2 SO.sub.4 :6H.sub.2 O 0.0005 MnSO.sub.4 :4H.sub.2 O 0.0005 CuSO.sub.4 :5H.sub.2 O 0.0001 CoCl.sub.2 :6H.sub.2 O 0.0001 CaCl.sub.2 :2H.sub.2 O 0.0015 Na.sub.2 MoO.sub.4 2H.sub.2 O 0.00001 NaOH             0.2 ______________________________________

Salts sterilized at 15 p.s.i.g./15 min. Final pH 6.0

Solution 3 Vitamins as described below were sterilized by filtration.

The solutions were added aseptically to give a final volume of 200 ml. then the flasks were inoculated with washed spores of our strain of Fusarium graminearum I-7 IMI 154209 to give a concentration of 8.times.10.sup.3 /ml.

The conditions of growth were temperature 30.degree. C., 140 r.p.m. on orbital shaker with 2" throw.

At hourly intervals the growth was measured by measuring the Optical Density of a sample at 600 m.mu.. From the results obtained the following growth rates were established. Growth rate h.sup.-1 ______________________________________ (i)  Solution 3 omitted (minimum medium) very slow (ii) Solution 3 such that the final con- 0.22 centration of Biotin in the culture medium was 50 .mu.g/l (iii) Solution 3 such that the final 0.27 concentration of Biotin in the culture medium was 50 g/l and Choline chloride 50 .mu. mg/l. ______________________________________

The procedure of Example 7 was repeated but the strain I-7 was replaced by our strain of Fusarium graminearum Schwabe I-8. The following growth rates were established: Growth rate h.sup.-1 ______________________________________ (i)         As 7 (i) very slow (ii)        As 7 (ii) 0.22 (iii)       As 7 (iii) 0.27 ______________________________________

The procedure of Example 7 was repeated but the strain I-7 was replaced by our strain of Fusarium graminearum Schwabe I-9. The following growth rates were established: Growth rate h.sup.-1 ______________________________________ (i)         As 7 (i) very slow (ii)        As 7 (ii) 0.21 (iii)       As 7 (iii) 0.27 ______________________________________

The procedure of Example 7 was repeated but the strain I-7 was replaced by our strain of Fusarium graminearum Schwabe I-15. The following growth rates were established: Growth rate h.sup.-1 ______________________________________ (i)         As 7 (i) very slow (ii)        As 7 (ii) 0.21 (iii)       As 7 (iii) 0.27 ______________________________________

The procedure of Example 7 was repeated but the strain I-7 was replaced by our strain of Fusarium graminearum Schwabe I-16. The following growth rates were established: Growth rate.sup.-1 ______________________________________ (i)         As 7 (i) very slow (ii)        As 7 (ii) 0.21 (iii)       As 7 (iii) 0.27 ______________________________________

The procedure of Example 7 was repeated but the strain I-7 was replaced by the parent strain Fusarium graminearum Schwabe IMI 145425. The following growth rates were established. Growth rate.sup.-1 ______________________________________ (i)         As 7 (i) very slow (ii)        As 7 (ii) 0.22 (iii)       As 7 (iii) 0.27 ______________________________________

Examples 13 and 14 describe fermentation using strains of Fusaria other than Fusarium graminearum.

A spore suspension of Fusarium solani strain A7-16 (IMI 154217) was inoculated into a seed fermenter of 80 liter volume containing a glucose, corn steep liquor medium. After growing up the seed fermenter to 10-20 gms per liter, it was split in two, 40 liters to each 400 liter vessel. The seed was inoculated into a medium of the following composition: % ______________________________________ Starch            6.0 KH.sub.2 PO.sub.4 0.20 (NH.sub.4).sub.2 SO.sub.4 0.25 Corn Steep Liquor 0.50 50% Total Solids) ______________________________________

pH was 5.5 maintained by addition of sterile ammonia; Temperature 30.degree. C. Pressure 30 p.s.i.g. Air rate 1.0 v.v.m. The revolutions of the stirrer were increased steadily from 92 to 184 r.p.m. to maintain dissolved oxygen in the vessel. The agitator consisted of two turbines 0.4D. When the carbohydrate had been utilized the grown mycelium was removed from the fermenter, filtered, washed with water, centrifuged, and dried in a warm air band drier at 75.degree. C. The dried product had the following composition: Total nitrogen 9.1% Ash       8.3% ______________________________________

When fed to rats this material gave an NPUop of 41 based on Total Nitrogen.

Fusarium oxysporum strain A9-23 (IMI 154214) was grown exactly as in the previous example except the starch was replaced by cane molasses at a concentration that produced 6.0% sugars.

The dried product had the following composition: Total nitrogen 9.9% Ash            10.8% NPUop          47.0    based on Total Nitrogen ______________________________________

Methods of analysis for Total Nitrogen (TN) Automatic Kjeldahl digestor (Technicon). A. Ferrari, Ann. N.Y. Sci. 87, 792 (1960).

Amino nitrogen (AN) 2:4:6-Tri-nitro benzene sulphuric acid (modified). M. A. Pinnegar, Technicon Symposium 1965, p. 80.

British Pat. No. 1,346,061 describes and claims our specific novel strain of Fusarium graminearum Schwabe IMI 145425 and variants and mutants thereof. This strain has also been deposited with the American Type Culture Collection and assigned the number A.T.C.C. 20334.

The separated proliferated organism comprising the edible protein-containing substance obtained by the fermentation processes of our British Pat. Nos. 1,331,471 and 1,346,062 may be incorporated into a foodstuff for human or animal consumption.

The processes of our British Pat. Nos. 1,331,471 and 1,346,062 are capable of producing an edible protein-containing substance comprising fungal mycelium which possesses a high net protein utilisation value on rat assays of at least 70 based on the .alpha.-amino nitrogen.

If single-cell protein is to be used as a primary protein source for human consumption the World Health Organization has advised that the nucleic acid content should be reduced to a level which would allow a maximum intake in the range of 2 grams of nucleic acid per day.

For a processing method to be acceptable, it must not only decrease the nucleic acid level to the required degree, but it also must be inexpensive and must not contaminate the food product with undesirable chemicals.

It is an object of the present invention to provide a process for the reduction of levels of nucleic acid in particular ribonucleic acid (RNA) in proliferated microorganisms combined with the minimum loss of protein to render them more acceptable as human food.

We have developed a process for treating cells of grown non-toxic microfungus of the class Fungi Imperfecti which can meet the above requirements of the World Health Organisation.

The invention provides fungal mycelium possessing a reduced level of RNA of below 4%.

Thus the invention provides fungal mycelium containing Fusarium graminearum Schwabe IMI 145425 possessing a reduced level of RNA of below 3% by weight, preferably below 2% by weight.

The invention also provides fungal mycelium containing Penicillium notatum-chrysogenum IMI 138291 possessing a reduced level of RNA of below 4%

According to the present invention there is provided a process for reducing the nucleic acid content in the production of an edible protein-containing substance comprising contacting a grown non-toxic microfungus of the class Fungi Imperfecti with a solvent comprising between 40% and 100% (by volume) of a lower alkanol containing up to three carbon atoms and thereafter incubating at a pH betweeen 5 and 9.5 and at a temperature between 30.degree. C. and 80.degree. C. for a time of at least 90 seconds.

The process may be applied to a grown non-toxic strain of Fusarium, Penicillium notatum or Ponicillium chrysogenum, Penicillium funiculosum or Aspergillus niger.

The strain of Fuscarium may be a strain of Fusarium graminearum Schwabe in particular IMI 145425, Fusarium oxysporum or Fusarium nolani as described and claimed in British Pat. Nos. 1,346,061 and 1,346,062.

The strain of Penicilium notatum or Penicillium chrysogenus may be a strain of Penicillim notatum -chrysogenum, for example IMI 138291, as described and claimed in British Pat. Nos. 1,331,471 and 1,331,742.

The lower alkanol containing up to three carbon atoms may be methyl alcohol, ethyl alcohol, propyl alcohol or isopropyl alcohol. Ethyl alcohol and isopropyl alcohol are solvents permitted by the Solvents in Food Regulations, 1967. The preferred solvent in the process of the present invention is isopropyl alcohol (IPA). Instead of pure isopropyl alcohol aqueous solutions containing between 40 or 50% by volume and up to 100% I.P.A. may be employed.

The incubation may conveniently be carried out at a temperature between 45.degree. C. and 60.degree. C. for a time of between 1.5 minutes and 40 minutes.

The incubation step may conveniently be carried out in the presence of a buffer solution for example NH.sub.4 Cl/NH.sub.4 OH or NH.sub.4 Cl/HCl.

The post fermentation process of the present invention for reducing the nucleic acid content of microorganisms is essentially a two stage process.

The grown microbial protein or fungal mycelium obtained for example by the fermentation process described and claimed in British Pat. Nos. 1,331,471 and 1,346,062 may be harvested, filtered to remove growth medium and washed, if desired. It may then be suspended in the alkanol solvent for example 1 minute at 20.degree. C. or contacted with an alkanol solvent water mixture. The majority or all of the alkanol solvent may be removed by such methods as vacuum filtration, filter pressing or centrifugation. The duration of contact with the alkanol solvent may be varied but is generally in the range between 15 seconds and 15 minutes. The temperature may vary between 0.degree. C. and 60.degree. C.

The cells may then be brought into intimate contact with aqueous buffer solutions in the pH range 5 to 9.5. Thus the solvent treated cells may then be resuspended and incubated in aqueous buffer solution at pH 8.6 and temperature 45.degree. C. An example of a suitable buffer solution is 0.1M ammonium chloride solution with ammonium hydroxide added to adjust the pH to 8.6.

The resulting treated cells may then be harvested again for example by filtration and washing with water and thereafter formulated into foods or dried by various methods.

When the process is carried out in the pilot-plant the pH is adjusted to 5 after RNA removal. The purpose of this acidification is twofold (a) the material becomes "whiter" and (b) the texture change and this enables harvesting by vacuum filtration to be carried out easier.

The resulting solvent treated microbial protein or fungal mycelium may have a RNA content of 1-4% compared to 7 to 10% of the untreated proliferated organism.

The cells may be analysed to determine their chemical composition and to evaluate the efficiency of the nucleic acid reduction process.

Following is a description by way of example of methods of carrying the invention into effect.

References to "Biomass Loss" denote weight lost during processing.

Ribonucleic acid (RNA) content was determined by a modification of the method of Schmidt G. and Thannhauser, S. J., J. Biol.Chem., 1945, 161, 83.

Method of analysis for Total Nitrogen (TN) Automatic Kjeldahl digestor (Technicon). A. Ferrari, Ann. N.Y. Sci. 87, 792 (1960).

Amino nitrogen (AN) TNBS (modified). M. A. Pinnegar, Technicon Symponium 1965, p. 80.

Fusarium graminearum IMI 145425 was cultivated by the following procedure: Medium in distilled water: K.sub.2 HPO.sub.4     15.05  gL.sup.-1 (NH.sub.4).sub.2 HPO.sub.4 6.64   gL.sup.-1 tri Sodium Citrate    15.7   gL.sup.-1 Citric Acid           5.48   gL.sup.-1 K.sub.2 SO.sub.4      1.0    gL.sup.-1 Choline chloride      50     mgL.sup.-1 Biotin                50     .mu.gL.sup.-1 Glucose               30     gL.sup.-1 Minimal Salts MgCl.sub.2.6H.sub.2 O 0.2    gL.sup.-1 ZnSO.sub.4            0.003  gL.sup.-1 MnCl.sub.2 4H.sub.2 O 0.005  gL.sup.-1 FoCl.sub.3.6H.sub.2 O 0.01   gL.sup.-1 CuCl.sub.2.6H.sub.2 O 0.001  gL.sup.-1 NaMoO.sub.4.2H.sub.2 O 0.001  gL.sup.-1 CoCl.sub.2.6H.sub.2 O 0.001  gL.sup.-1 CaCl.sub.2.2H.sub.2 O 0.015  gL.sup.-1 ______________________________________

All components with the exception of glucose are sterilized together, and the amounts of these materials required for 1 liter of modium are dissolved, made up to 850 ml. and distributed into 5 1 liter conical flasks, each containing 170 ml. A 30% w/v solution of glucose is prepared and sterilised in 20 ml. portions in universal bottles. Sterilisation is effected in an autoclave at 15 p.s.i. for 15 minutes.

Before inoculation with 10 ml. of a growing culture, the contents of one bottle of sterile glucose solution is added to each flank. Culture of A3/5 then proceeds on an Orbital Shaker, with 2 inch throw, at 160 r.p.m. and a temperature of 30.degree. C. The culture is harvested after 18 hours.

Cells were collected and washed on a Buchner filtration system and treated as follows: buffer at pH 8.6 and 45.degree. C. for various times. The incubations were carried out at a slurry concentration of approximately 10 g/l with stirring. Results Time of Micro- Trout-   Incubation % RNA  % Amino % Total fungi  ment     Minutes   Content Nitrogen Nitrogen ______________________________________ F. grami- None     None      10.86  7.57   9.80 nearium Nucleic  Zero      9.86   8.23   10.93 acid Reduc- tion Nucleic  20        2.29   8.84   10.43 acid Reduc- tion Nucleic  40        1.88   8.68   9.91 acid Reduc- tion Nucleic  60        1.69   8.73   10.56 acid Reduc- tion ______________________________________

The level of nucleic acid was effectively reduced by the treatment described. procedure:

The medium is made up with hot tap water, and dispensed in 200 ml. aliquots into conical shake flasks.

0.1 ml. of liquid amylase was added to each shake flask and incubated at 70.degree. C. for 15 minutes so that the starch was broken down and the viscosity reduced.

The flasks were sterilised in an autoclave at 15 p.s.i. for 20 minutes.

A sporo inoculum was added to each flask and the culture grown at 30.degree. C. on an orbital shaker with a 2 inch throw at 160 r.p.m. After growth for 24 hours, 10 ml. of the growing culture was used as growing inoculum which was added to more flasks containing the starch medium. Cells produced after a further 24 hour growth were harvested, washed and used as follows: C. buffer at pH 8.6and 40.degree. C. for various times. The incubations were carrried out at a slurry concentration of approximately 10 gm/l with stirring. Results Time of Incubation % RNA % Amino % Total % Biomass Microfungi Treatment Minutes content Nitrogen Nitrogen Loss __________________________________________________________________________ P. notatum- None  None  7.19 5.78 7.58 0 chrysogenum P. notatum- Nucleic 15    3.60 6.64 8.47 30 chrysogenum Acid Reduction P. notatum- Nucleic 40    3.25 6.47 8.52 32 chrysogenum Acid Reduction P. notatum- Nucleic 60    3.32 6.34 8.04 32 chrysogenum Acid Reduction __________________________________________________________________________

The level of nucleic acid was reduced by the treatment described. Penicillium funiculosum IMI 79195 was cultivated by the following procedure: Medium KH.sub.2 PO.sub.4  15    g/l NaOH               1     g/l Dextran            1     g/l Castor Oil         10    g/l Solution A.sup.+   5     ml/l Solution B.sup.+   5     ml/l Solution C.sup.+   5     ml/l Yeast extract      10    g/l Minimal salts A.sup.+       B.sup.+     C.sup.+ MgSO.sub.4 50 g/l  CaCl.sub.2 3 g/l FeSO.sub.4 1 g/l ZnSO.sub.4 1 g/l MnSO.sub.4 1 g/l   CaCl.sub.2 0.2 g/l CuSO.sub.4 0.2 g/l ______________________________________

All in distilled water.

Adjust pH of medium to 5.5 before sterilisation. Autoclave all components together. (50 minutes 15 p.s.i.)

(Batch culture)

Cells were collected and washed on a Buchner filtration system and treated as follows: buffer at pH 8.6 and 37.degree. C. for 60 minutes. The incubation was carried out at a slurry concentration of approximately 10 g/l with stirring. Results % RNA     % Amine Microorganism Treatment content   N      % Total N ______________________________________ P. funiculosum None      4.23      3.74  5.81 P. funiculosum Nucleic   2.80      4.46  7.34 Acid Reduction ______________________________________

The level of nucleic acid was reduced by the treatment described.

Aspergillus niger NRRL 330 was cultivated by the following procedure:

The medium and sterilisation procedure were identical to that described for P. notatum-chrynogenum.

Growth conditions were also identical except that cells grown directly from spores were used instead of cells cultivated from growing inoculum.

Cells were collected and washed on a Buchner filtration system and treated as follows: buffer at pH 8.6 and 40` C. for various times. The incubations were carried out at a slurry concentration of approximately 10 g/l with stirring. Results Time of  %     %     %     % Incu-    RNA   Amino Total Bio- Micro-           bation   Con-  Nitro- Nitro- mass fungi  Treatment Minutes  tent  gen   gen   loss ______________________________________ A. niger None      None     6.36  4.03  5.70  none "      Nucleic   zero acid Reduction "      Nucleic   15       1.88  4.40  6.30  27 acid Reduction "      Nucleic   30       1.86  4.35  5.77  28 acid Reduction "      Nucleic   60       1.82  4.25  5.62  32 acid Reduction ______________________________________

The level of nucleic acid was effectively reduced by the treatment described. REDUCTION PROCESS

F. gramincarum IMI 145425, cultivated as described in Example A, was contacted with various isopropyl alcohol/water mixtures at 20.degree. C. for 2 minutes. The treated cells were then incubated in 0.1M NH.sub.4 Cl/NH.sub.4 OH buffer pH 8.5 at 37.degree. C. for 20 minutes. The incubations were carried out at a slurry concentration of approximately 10 g/l with stirring. Results % IPA     %         Biomass (by volume) Treatment loss       % RNA remaining ______________________________________ 0        None      0.0        9.33 0        Nucleic   1.8        9.33 acid reduction 10        Nucleic   1.1        10.68 acid reduction 20        Nucleic   11.3       9.74 acid reduction 30        Nucleic   19.4       8.87 acid reduction 40        Nucleic   25.6       4.58 acid reduction 50        Nucleic   26.5       3.03 acid reduction 60        Nucleic   28.0       3.25 acid reduction 70        Nucleic   27.6       2.86 acid reduction 80        Nucleic   26.3       3.35 acid reduction 90        Nucleic   23.8       3.69 acid reduction 100       Nucleic   25.1       4.58 acid reduction ______________________________________

The nucleic acid removal process is most effective in the range of 40-100% isopropyl alcohol.

In the case of the treatment with 10 & 20% IPA the final RNA content is greater than the starting material; this is because RNA is removed to a lesser extent than biomass lost. NUCLEIC ACID REDUCTION PROCESS

F. graminearum IMI 145425, cultivated as described in Example A, was contacted with 100% IPA at 0.degree., 20.degree., 40.degree., and 60.degree. C. for 2 minutes, then incubated with 0.1M NH.sub.4 Cl/NH.sub.4 OH buffer pH 8.5 for 20 minutes at 39.degree. C. The incubations were carried out at a slurry concentration of approximately 10 g/l with stirring. Results Temperature of IPA treatment % RNA remaining ______________________________________ No treatment  9.04 0.degree. C. 3.42 20.degree. C. 3.47 40.degree. C. 2.52 60.degree. C. 2.33 ______________________________________

The nucleic acid reduction process if effective over the temperature range studied.

F. graminearum IMI 145425, cultivated as described in Example A, was contacted with 100% iso-propyl alcohol, 70% iso-propyl alcohol, 70% propyl alcohol, 100% ethyl alcohol or 100% methyl alcohol at 20.degree. C. for two minutes, then incubated with 0.1N NH.sub.4 Cl/NH.sub.4 OH buffer pH 8.5 at 37.degree. C. or 40.degree. C. for various time periods. The incubations were carried out at a slurry concentration of approximately 10 g/l with stirring. Results Time and temperature Alcohol used of second incubation % RNA remaining ______________________________________ None         None           9.16 100% iso-propyl 30 mins. at 37.degree. C. 2.53 alcohol 100% iso-propyl 120 mins. at 37.degree. C. 0.70 alcohol 70% iso-propyl 20 mins. at 40.degree. C. 1.81 alcohol 70% propyl alcohol 20 mins. at 40.degree. C. 1.93 100% ethyl alcohol 30 mins. at 37.degree. C. 2.17 100% ethyl alcohol 120 mins. at 37.degree. C. 0.64 100% methyl alcohol 30 mins. at 37.degree. C. 5.50 100% methyl alcohol 120 mins. at 37.degree. C. 1.17 ______________________________________

The RNA reduction process is successfully activated by a lower alkanol containing up to three carbon atoms.

F. graminearum IMI 145425, cultivated as described in Example A, was contacted with 66% (v/v) IPA at 20.degree. C. for various times thon incubated in 0.1N NH.sub.4 Cl/NH.sub.4 OH buffer pH 8.5 at 37.degree. C. for 60 minutes. The incubations were carried out at a slurry concentration of approximately 10 g/l with stirring. Results Contact time   % RNA     % Biomass with 66% IPA   remaining lost ______________________________________ 0             9.25       0 15 seconds     1.12      36 1 minute      1.14      38 2 minutes     0.98      40 5 minutes     1.23      -- 15 minutes     1.27      41 ______________________________________

Over the contact times studied nucleic acid removal was efficient. In practice the contact time for best RNA reduction is around 2 minutes, at longer contact times the % biomass lost tends to rise to unacceptably high values.

F. graminearum IMI 145425, cultivated as described in Example A, was contacted with 100% iso-propyl alcohol at 20.degree. C. and incubated with the following series of buffers at 30.degree. C. for 3 hours. The incubations were carried out at a slurry concentration of approximately 10 g/l with stirring. Results Buffer in second stage % RNA Remaining ______________________________________ 0.1M NH.sub.4 Cl + HCl to bring to pH 4.0 11.49 0.1M NH.sub.4 Cl + HCl to bring to pH 4.5 9.07 0.1M NH.sub.4 Cl + HCl to bring to pH 5.0 5.85 0.1M NH.sub.4 Cl + HCl to bring to pH 5.5 3.52 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 6.0 2.63 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 6.5 1.60 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 7.0 0.96 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 7.5 0.97 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 8.0 0.59 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 8.5 0.91 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 9.0 1.69 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 9.5 3.84 0.1M NH.sub.4 Cl + NH.sub.4 OH to bring to pH 10.0 7.00 ______________________________________

The nucleic acid removal is effective with this buffer system over the pH range 5-9.5. IONIC STRENGTHS

F. graminearum IMI 145425 cultivated as described in Example A, was contacted with 66% (v/v) IPA at 20.degree. C. for 1 minute, and incubated in buffers or non-buffered solutions of varying ionic strengths at 45.degree. C. The incubations were carried out at approximately 10 g/l with stirring. Results Time of incubation at 45.degree. C. % Amino % Total Buffer system   Treatment  (Minutes) % RNA Nitrogen Nitrogen __________________________________________________________________________ None            None       None  10.89 7.57  9.80 Distilled water Nucleic acid reduced 0    11.21 7.82 10.53 20    7.38 8.07 10.22 pH 5.7                     40    4.79 7.97 10.12 60    2.57 8.40  9.84 Non-buffered    "           0    11.17 8.35 10.81 ammonia solution           20    4.54 8.85 10.07 sufficient to bring to pH 8.5 40    3.14 8.85 10.68 60    2.55 8.79 10.30 0.02 M NH.sub.4 Cl/NH.sub.4 OH "           0    9.96 8.46 10.89 20    3.21 8.62 10.38 buffer pH 8.5              40    2.39 8.73 10.36 60    1.82 8.90 10.12 0.1M NH.sub.4 Cl/NH.sub.4 OH "           0    9.86 8.23 10.98 20    2.29 8.84 10.45 buffer pH 8.5              40    1.88 8.68  9.91 60    1.69 8.73 10.56 0.5M NH.sub.4 Cl/NH.sub.4 OH "           0    10.02 8.21 10.58 20    5.85 8.35 10.13 buffer pH 8.5              40    5.63 8.42 10.01 60    5.58 8.54 10.12 1.0M NH.sub.4 Cl/NH.sub.4 OH "           0    10.19 7.56 10.89 20    10.45 7.72 10.48 buffer pH 8.5              40    9.96 7.99 10.81 60    9.89 8.15 10.58 __________________________________________________________________________

Nucleic acid is most effectively reduced at lower ionic strengths. The optimum conditions for rapid reduction being 0.1N buffer.

F. graminearum IMI 145425, cultivated as described in Example A, was contacted with 66% (v/v) IPA at 20.degree. C. for 2 minutes, and incubated in 0.1M NH.sub.4 Cl/NH.sub.4 OH buffer pH 8.5 for various durations at various temperatures. The incubations were carried out at approximately 10 g/l with stirring. Results Temperature Time of incubation of buffer  minutes       % RNA remaining ______________________________________ Control    --            9.44 30.degree. C. 0             10.83 30.degree. C. 20            8.40 30.degree. C. 40            7.06 30.degree. C. 60            7.45 30.degree. C. 90            4.76 30.degree. C. 120           4.11 37.degree. C. 0             10.12 37.degree. C. 20            5.02 37.degree. C. 40            3.55 37.degree. C. 60            -- 37.degree. C. 90            1.80 37.degree. C. 120           1.02 45.degree. C. 0             10.09 45.degree. C. 20            2.58 45.degree. C. 40            0.99 45.degree. C. 60            0.69 45.degree. C. 90            0.69 45.degree. C. 120           0.61 55.degree. C. 1.5           2.16 55.degree. C. 3.0           1.10 55.degree. C. 4.5           0.76 60.degree. C. 1.5           1.96 60.degree. C. 3.0           1.78 60.degree. C. 4.5           1.11 70.degree. C. 2.0           4.19 70.degree. C. 3.5           3.30 70.degree. C. 5.0           3.56 80.degree. C. 1.5           5.65 80.degree. C. 3.0           5.40 80.degree. C. 4.5           5.31 ______________________________________

Nucleic acid reduction takes place over the temperature range 30.degree. C.-80.degree. C. The most efficient conditions are at a temperature of 60.degree. C., where satisfactory reduction of RNA was achieved within 90 seconds.

## Claims

1. An edible protein-containing substance of reduced nucleic acid content of between 1.7 and 0.59% obtained by a process consisting essentially of contacting a grown nontoxic microfungus of the genus Fusarium with a solvent comprising between 40% and 100% by volume of a lower alkanol containing up to three carbon atoms and the remainder being water, substantially separating said solvent from said microfungus, incubating said microfungus at a pH between 5 and 9.5 and at a temperature between 30.degree. C. and 80.degree. C. for a time of at least 90 seconds and thereafter recovering said microfungus as said edible protein-containing substance which is harvested by vacuum filtration in the form of a washed moist product suitable for food use, said substance having a filamentous structure due to the presence of retained fungal cell wall material and being characterized by improved ease of processing to a form suitable for food use and an improved whiter color such as to make the protein-containing substance compatible with food use.

2. An edible protein-containing substance as claimed in claim 1 wherein the strain of Fusarium is a strain of Fusarium graminearum Schwabe, Fusarium oxysporum or Fusarium solani.

3. An edible protein-containing substance as claimed in claim 2, wherein the strain of Fusarium graminearum Schwabe is a strain of Fusarium graminearum Schwabe deposited with the Commonwealth Mycological Institute and assigned the number IMI 145425 (A.T.C.C. 20334).

4. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum possessing a reduced level of RNA of below 4%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

5. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Penicillium notatum-chrysogenum IMI 138291 possessing a reduced level of RNA of below 4%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

6. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum possessing a reduced level of RNA of below 1.5%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

7. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum possessing a reduced level of RNA of below 1.27%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

8. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum possessing a reduced level of RNA of below 1%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

9. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum Schwabe IMI 145425 (A.T.C.C. No. 20334) possessing a reduced level of RNA of below 0.99%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

10. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum possessing a reduced level of RNA of below 0.70%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

11. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum possessing a reduced level of RNA of between about 1.27% and about 0.59%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

12. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum Schwabe IMI 145425 (A.T.C.C. No. 20334) possessing a reduced level of RNA of between about 0.99% and about 0.59%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

13. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum Schwabe IMI 145425 (A.T.C.C. No. 20334) possessing a reduced level of RNA of between about 1.70% and about 0.59%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

14. An edible protein-containing substance in the form of a washed product suitable for food use comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum, said product having a filamentous structure due to the presence of retained fungal cell wall material and possessing a reduced level of RNA of below 3%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use.

15. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum Schwabe IMI 145425 (A.T.C.C. No. 20334), said product having a high net protein utilization value of the order of 67 or above based on .alpha.-amino nitrogen and possessing a reduced level of RNA of below 1.5%, and being further characterized by an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material and being capable of processing by vacuum filtration and washing on the filter in the form of a moist product suitable for food use.

16. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum, said product having a high net protein utilization value of the order of 52 or above based on the total nitrogen and possessing a reduced level of RNA of below 1.5%, and being further characterized by improved ease of processing to a form suitable for food use and an essentially white color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material.

17. An edible protein-containing substance comprising a non-viable edible non-toxic fungal mycelium of a non-toxic strain of Fusarium graminearum Schwabe IMI 145425 (A.T.C.C. No. 20334), said product having a high net protein utilization value of the order of 67 or above based on .alpha.-amino nitrogen and possessing a reduced level of RNA of below about 0.59%, and being further characterized by an improved whiter color such as to make the protein-containing substance compatible with food use and a filamentous structure due to the presence of retained fungal cell wall material and being capable of processing by vacuum filtration in the form of a washed moist product suitable for food use.