in the process according to the invention the flax seed used as a basic material can be the seed of a flax variety , e . g . linum usitatissimum cv . brown , l . usitatissimum cv . goldline and the like . according to one preferred embodiment of the process of the present invention the aqueous enzyme solution of the desired composition can be prepared from the necessary enzymes . the seeds are swollen in the enzyme solution which is prepared beforehand . the flax seed may be placed in plastic bags with small holes or plastic net , the mesh of which is about 0 . 2 mm . the enzyme solution contains pectinolytic and cellulolytic and optionally proteolytic enzymes . as a pectinolytic enzyme pectinase , e . g . macerozyme r - 10 or a pectinase derived from aspergillus niger , as a cellulolytic enzyme cellulase , e . g . onozuka r - 10 , glucuronase , helicase or sulfatase ; as a proteolytic enzyme lysosyme , protease and the like can be used . in a preferred embodiment of the invention a pectinolytic ( pectin - splitting ) enzyme is used together with a cellulolytic ( cellulose - splitting ), preferably pectinase derived from aspergillus niger and glucuronase . according to another preferred embodiment , a pectinase is used together with lysosyme , which is well known to be a multifunctional enzyme . in another preferred embodiment , a pectinolytic enzyme is used together with cellulolytic enzymes , namely glucuronase and sulfatase . the aqueous enzyme solution contains the pectinolytic enzymes in 1 - 10 u / ml , preferably 1 - 5 u / ml concentration , the cellulolytic enzymes in 2 - 50 u / ml , preferably 5 - 15 u / ml concentration and the proteolytic enzymes in 10 - 500 u / ml , preferably 50 - 200 u / ml concentration . the composition of the enzyme solution depends on the flax variety . according to another preferred embodiment the supernatants originating from fermentation broth of micro - organisms producing specific extracellular enzymes , as pectinolytic , cellulolytic and proteolytic enzymes , are used as aqueous enzyme solution . the supernatants are adjusted to pectinase enzyme activity . the fermentation broth can be originated from fermenting bacteria or fungi , e . g . trichoderma sp ., as trichoderma rosea , glyociadium catenulatum and the like . the mucilaginous material originated from the process according to this invention can be used as fermentation media , too . the fermentation broth is centrifuged , the supernatant is separated and optionally sterilized by sterile filtration , or by treatment with chloroform , and the like . the fermentation broth is optionally filtered to be cell - free . the application of fermentation broth as a natural source of enzyme in the process according to this invention allows the significant reduction of costs of the production , first of all the costs of the production on an industrial scale . the ph of enzyme solution is mildly acid , preferably 6 . 5 , which can be adjusted with organic or inorganic acids or with acidic salts . for this purpose hydrochloric acid , acetic acid or potassium dihydrogen phosphate , preferably acetic acid can be used . the seeds are treated with an enzyme solution of a volume ratio from one - and - a - half to two , preferably one - and - a - half parts calculated to one volume unit of the seeds . during this treatment the seeds take up the enzyme solution , then they are incubated at temperatures of 20 - 30 ° c ., preferably 25 - 28 ° c . for 6 - 24 hours , preferably for 18 - 20 hours . then the seeds are swollen to their water absorbing capacity ( about fivefold of dry seed volume ). the swelling can be promoted with a gentle mechanical agitation , preferably stirring . the aqueous , gel - like mucilaginous material is separated from the seeds by applying a mild pressure , preferably pressing to the wet seed volume . in this manner about 90 % of the mucilaginous material can be separated . because the sterilization of seeds is necessary for the germination , the rest of mucilaginous material has to be removed from the seeds . it can be achieved by an intensive watery washing . the washing of seeds is continued until the wash liquid turns transparent ( not opalescent ), and mucilaginous material cannot be detected in the wash liquid , neither by touch nor with a chemical method . then the free water between flaxseeds can be removed by draining , vacuumsuction or centrifugation , and the seeds obtained in this manner are directly used for sprouting . then the seeds perfectly cleaned of their mucilage are sterilized . for this purpose different sterilizing agents e . g . sodium hypochlorite , hydrogen peroxide , hyamine and the like are used . the seeds are preferably sterilized in a sodium hypochlorite solution of low concentration for 30 - 50 , preferably 40 - 45 minutes during continuous stirring , then the sterilizing agent is removed by washing with water , preferably by repeated washings , and the free water is removed by one of the above mentioned procedures . the seeds obtained in this manner are germinated by spreading them in a layer of 2 - 3 cm . the germination can be carried out in the usual way , preferably in darkness , at temperature 18 - 30 ° c . for 6 - 48 hours . the humidity left on the seeds is sufficient for them to sprout . the sprouts are grown up to a length of about 1 - 5 mm , preferably 2 - 4 mm , then they are harvested and are used directly or after drying . the flax sprouts obtained in this way are free from mucilaginous material . this is proved by the fact that the liquid flowing out after repeated watery steeping of flax sprouts do not contain sugar - like materials after acid treatment . they can be stored well and can be utilized directly for consumption or in food preparations . it was found that for example by packing the sprouts in plastic foil , and storing them at a temperature of 4 ° c . for 60 days no loss in quality occurred , e . g . the original taste and consistency was preserved . the objective of the preparation of industrial food products containing fresh flax sprout is that the flax sprout used as an additive should be kept in a active , not decayed condition for a time as long as possible . our aim has been that the fresh flax sprout should preserve its original taste and consistency in the product . for this purpose it has to be taken into consideration that the temperature during the processing should not exceed temperature 40 - 45 ° c . ; in this manner the premature decay of flax sprout and the oxidation of multiple unsaturated fatty acids can be prevented . another very important point of view is , however , that the total osmotic pressure of food ( in an aqueous medium , e . g . cheese ), to which the flax sprout is added , should not exceed the isoosmotic value . in the case of high osmotic pressure the flax sprout looses water during the storage and its consistency changes . for other applications the flax sprout can be dried and crushed , and the product obtained in this manner can be stored similarly as a kind of cereal , e . g . wheat or wheat meal . the drying is performed gently , preferably under temperature of 30 ° c . in such a manner that the flaxseed sprouts are dried to 75 - 90 percent of their initial seed weight , preferably to 80 - 85 percent of weight . the product obtained this way can be consumed as it is , or it can be mixed into food or animal fodders . for human purpose , it can be also used as a food supplement or nutriment or in a food preparation , first of all as a supply of essential fatty acids and phyto - hormones . for this purpose it can be used as instant granules together with auxiliary materials usually employed in the food industry or in the preparations of pharmaceuticals , as e . g . maltose , maltodextrine , binder materials , aroma materials , sweeteners , food colouring agents , etc ., or together with materials usually employed in the preparation of nutriments , as e . g . protein , carbohydrate , minerals , vitamins , etc ., or it can be pressured to tablets or encapsulated in a manner known per se . one of the advantages of the process according to the invention is that the flax sprout obtained in this manner is free of mucilage and therefore likely to be absorbed well , and its valuable components can be utilized in the living organisms . another advantage of the process according to the present invention lies therein that 90 % of the separated mucilaginous material originating as a by - product can be recovered and utilized . the squeezed , concentrated mucilaginous material can be precipitated with organic solvents suitable for precipitation of polysaccharides , thus , e . g . it can be precipitated with alcohols or chloroform . the squeezed , concentrated mucilaginous material is precipitated preferably in 50 % ( v / v ) aqueous ethanol solution at a temperature of 4 ° c . after leaving it at rest for at least 12 hours , and it can be separated well by centrifugation . the precipitating agent ( e . g . ethanol ) can be recovered from the filtrate . the precipitate obtained by centrifugation can be dehydrated with 96 percent ethanol , and the dehydrated precipitate is centrifuged again , then the precipitate obtained in this manner is dried . at the end of this process an amorphous material is produced which can be pulverized and packed . the flax mucilaginous material obtained in this manner can be perfectly dissolved again in water . the mucilaginous material obtained by this process can be utilized in many fields . it can be utilized in cosmetic agents , e . g . in body lotions as an emulsifying agent and foaming material . it can be also utilized for food industrial purposes as a consistency improver . it can be used in microbiological processes as a culture medium or as a component of culture media for the cultivation of pectinolytic micro - organisms and / or micro - organisms utilizing polysaccharides , e . g . aspergillus niger or glyocladium catenulatum . in fact , it can be employed as a lubricant with a water basis for e . g . lubrication of rotating instruments . the demucilaged flax sprout according to the invention eliminates the hindering factors which obstructs the possibility of utilizing of the flax seed in the food industry and in other fields . the demucilaged flax sprout does not contain materials hindering the digestion and preventing the absorption of nutrients . the demucilaged flax sprout can in a dried form and in a form of a grist respectively be stored for a long period without refrigeration , similar to the products made from cereals . the demucilaged flax sprout according to the invention can be popular because the valuable active ingredients and taste materials are biologically protected and they do not change during storage . the method worked out for the preparation of demucilaged flax sprout makes it possible completely to mechanize the process and allow for a large scale production . in consequence of this fact new products having high biological value can appear in the food - and fodder market and also among the pharmaceutical products . additionally , according to the invention there is a possibility to process the flaxseed without any loss during the preparation of flax sprout since the by - product obtained can be utilized further . the invention is illustrated with the following examples which , however , are not to be considered as limiting the invention disclosed herein . the seeds of variety linum usitatissimum cv , brown with high sprouting ability , purified for food industrial purposes ( 1 kg ) are placed into a 10 litre plastic bag ( similar to dense weaved curtain material ) with meshes of 0 . 2 mm . the bag is placed in closed form into 1 . 5 litres enzyme solution , contains the followings : 2 % macerozyme r - 10 ( manufacturer : kinki yakult mfg co ., japan ), 0 . 5 % cellulase “ ozonuka ” r - 10 ( manufacturer : kinki yakult mfg co ., japan ) and 1500 ml tap water , ph 6 . 5 which is adjusted by 1n acetic acid . the seeds are gently agitated up till the time as the total amount of liquid will be absorbed ( generally 20 - 30 minutes ). at this time the seeds generally settled into one block . the seeds together with the bag are incubated at 25 ° c . for 24 hours . after the expiry of incubation periods the bag containing the seeds is placed into lukewarm water , and applying gentle agitation the seeds are allowed to be perfectly saturated with water . then the bag is placed in a press and is pressed to seed volume with mild pressure ( e . g . with a wine - press ). in consequence of the pressing 90 % of mucilaginous material can be separated . this compressed material is suitable to further processing . the rest of mucilaginous material is washed out from the seeds and the bag , respectively , by intensive washing in running water , for about 15 minutes . the washing of seeds is continued until the flowing liquid is no longer opalescent , and mucilaginous material cannot be detected by touch . to allow sterilisation no traces of mucilaginous material may remain on the surface of the husk . the free water is drained from the demucilaged seeds in the bag , then the seeds are used for further processing . the process is practically the same as in example 1 , but the seeds are soaked in an enzyme solution with the following composition : in the case of the above described combination the seeds have to be incubated at higher temperature , 28 ° c ., to obtain similar results . the seeds of variety linum usitatissimum cv , goldenline 90 with high sprouting ability , purified for food industrial purposes ( 1 kg ) are placed into a 10 litre plastic netbag with perforations of 0 . 2 mm . the bag is placed in closed form into 1 . 5 litres enzyme solution . the composition of enzyme solution is the following : the incubation is performed according to example 1 . after expiry of the incubation period the bags ( three times 1 kg treated seed ) are flushed with mechanical washing , interrupted by five centrifuging periods . the wash liquid is checked visually for opalescence and by touch for mucosity . if the wash liquid appears to be clear as water the washing is stopped . from the bags the free water is removed by drainage or centrifugation , and then the content of bags is used for further processing . 2 liters of first pressure of flax mucilage is added to 8 liters of potato extract and is put into new brunswick m - 100 fermenter . the sterilization is accomplished at 121 ° c ., ˜ 1 . 2 × 10 5 pa ( 1 . 2 bar ) for 40 minutes . after sterilization the fermentation broth is cooled to 25 ° c . the fermentation broth is inoculated with 100 ml glyocladium catenulatum inoculum suspension previously grown on shaker machine for 24 hours . in order to grow glyocladium catenulatum ( a microparasitic , but non - plant parasitic fungus producing extracellular enzymes ) in the fermenter the regime should be as follows : temperature : 27 ° c ., stirring 150 rpm , ph should be adjusted to 6 , 5 during the whole fermentation cycle , relative oxygen saturation should be kept at 60 %, aeration control should be cascaded from oxygen control . foam control is necessary during the fermentation . the fermentation regime should be controlled by ml - 100 multiloop controller . the fermentation period is 36 - 48 hours . after finishing the fermentation the whole fermentation broth is centrifuged at 16000 rpm for 40 minutes in a sorwall high - speed centrifuge . the supernatant is used as enzyme solution . ( the pellet could be used as a biological antifungal agent .) alternatively 2 ml chloroform is added to 10 litres of supernatant to kill remaining spores and cells , or the supernatant is sterilized by filtration , then the filtrate is allowed to settle for 10 hours at room temperature . in that case if no any sterilization process is used for the supernatant containing enzymes , an additional , repeated sodium hypochlorite treatment of the flax seed is necessary after removal of the mucilaginous material . the enzyme activity could be measured and adjusted according to kalac j . and rexova l . ( biochim . biophys . acta 167 ( 3 ): 590 - 596 , 1968 ). further processes are similar to example 1 - 3 . with this alternative process the production costs in the large - scale industrial production of demucilaged flax sprouts could be significantly decreased . holding the seeds perfectly freed of mucilaginous materials in a plastic bag ( according to examples 1 - 3 ) are immersed for the purpose of the sterilization of their surface in 5 % ( w / v ) sodium hypochlorite solution for 40 minutes in the course of continuous moving , then the seeds in the bag are flushed twice and drained well . then the bag is placed in a tray , and the seeds are spread out ( within the bag ) in a uniform layer . the seeds smoothed down in this manner ( about 3 cm thick layer ) are incubated in darkness at 18 - 22 ° c . for 24 - 48 hours . generally the amount of water absorbed by the seeds during the enzymatic treatment and further treatments is enough to start the sprouting and to develop 2 - 5 mm long sprouts during the incubation period . during the incubation period the seed mass consumes the water adhered on seeds , and normally no further drying is necessary . at the end of the incubation period the ratio between sprouted and non - sprouted seeds are established ( 300 seed samples can give a correct result ). 98 - 100 % of the seeds demucilaged according to examples 1 - 3 sprout proving the fact that the demucilaged flax seed are viable . the flax sprouts have a mildly hazelnut taste in this stage , and have no unpleasant by - taste . as far as the utilization of fresh flax seed sprout produced according to example 5 is concerned , there are many possibilities . trials were made in connection with the use of known packing techniques and compared to how long the product obtained according to the invention can be stored . the results of experiments are summarized in the following table 2 . 500 grams of cake - plating , tempered chocolate are melted in a water bath at 32 ° c ., then a chocolate melting mold is formed in a thin layer ( about 1 mm thick ). then the chocolate layer is allowed to cool down slightly and to become hard . on this layer 300 g flax sprouts are evenly spread and this layer is again covered with melted chocolate in a manner that the total amount of flax sprout should be covered , while being careful that the temperature of pouring chocolate should not exceed 32 ° c . after hardening of this layer finally a thin top - layer is poured from chocolate . the product can be stored at least for 60 days in room temperature without reduction of quality . this example is to show that in the preparation of industrial food products it is necessary to apply such a technology in which the fresh flax sprout is not in contact with air in order to preserve the original values of flaxseed as long time as possible . in the case of milk - and meat products the procedure is similar . the flaxseeds of variety linum usitatissimum cv . goldenline 90 with high sprouting ability , purified for food industrial purposes ( 1 kg ) are placed into a 10 litre bag made of plastic net with mesh of 0 . 2 mm . the bag of closed form is placed into 1 . 5 litres enzyme solution . the composition of enzyme solution is the following . after 18 hours incubation the flax seeds are to be freed perfectly from the mucilage . the cleaned seeds are sterilised and sprouted according to example 4 . when the size of sprouts become 2 - 5 mm long ( about 18 hours ), the sprouted flaxseeds are spread out in a thin layer ( at last 1 cm ) and they are dried at a temperature less than 30 ° c . to 85 percent of the initial weight in a usual way or by the help of a mechanical equipment ( e . g . vacuum pump ). the demucilaged flax sprouts dried in this mild manner can be utilized as they are or as an additive for foods . for example , the chocolate prepared from this product can be stored for 18 months in room temperature . from demucilaged flax sprouts dried according to example 7 , a rough preparation is prepared in a quick - blade grinding machine . the quick - blade grinding machines are suitable for this purpose because it can be ensured that during the grinding the temperature does not exceed 30 ° c . the grist obtained in this manner can be stored for a long time similarly to the grist prepared from cereals . the flaxseeds treated according to example 1 - 3 perfectly swollen in water and held in bags are put in a press ( e . g . wine - press is suitable ), then the mass are pressed to such an extent that 90 % of mucilaginous material should be pressed out and the seed should not injured . the pressed out , concentrated mucilaginous material is mixed with 96 % ethanol in a ratio 1 : 1 . from the about 50 - 50 % water - ethanol solution the mucilaginous material is allowed to precipitate standing at least 12 hours at 4 ° c . after precipitation the mucilaginous material can be removed by centrifugation ( e . g . preparative centrifuge , separator ) and the alcohol can be recovered . the precipitate - obtained in this manner is almost dehydrated with 96 % alcohol , then the pure precipitate is dried ( at 120 ° c .). after drying a hard amorphous material is obtained , which can be packed and utilized . the thus - obtained mucilaginous material can be completely dissolved in water . 10 grams of dried and pulverized mucilaginous material prepared according to example 9 are solved in 100 ml lukewarm milk . for redissolving the mucilaginous material 30 minutes are necessary at 40 ° c ., and 2 hours are necessary at 15 ° c . under constant stirring . after dissolution 200 ml fresh yoghurt is added and the mixture is spiced according to the manufacturer &# 39 ; s wish . the mixture is whipped to a foam . in this manner 500 ml stable yoghurt foam is obtained which can be stored for 6 days at 4 ° c . the product also acts as a laxative . 30 grams of dried and pulverized mucilaginous material are dissolved in 300 ml water at 80 ° c ., 200 ml maize germ oil is added and the mixture is cooled down to 50 ° c . the mixture is stirred in a homogenizer with high speed rotation , then the white cream obtained in this manner is cooled to 5 ° c . into the basic body lotion prepared in this manner any active ingredient can be taken to reach the desired product . 5 - 10 grams dried and pulverized mucilaginous material prepared according to example 9 are added into 1 liter potato extract ( the liquid of boiled potato ). this mixture is sterilized at 120 ° c ., then after cooling is inoculated aspergillus niger inoculum and the liquid is fermented in a manner known per se . the culture of aspergillus niger is harvested after 48 hours and is processed further . while the present invention has been described in conjunction with the specific embodiments set forth above , many alternatives , modifications and other variations thereof will be apparent to those of ordinary skills in the art . all such alternatives , modifications and variations are intended to fall within the spirit and scope of the present invention .
the present invention relates to demucilaged flax sprouts derived from flaxseeds freed of their mucilage . the flax sprouts according to the invention are easily digestible and can be utilized in different fields , e . g . in food industry , therapy and hus - handry . the invention also relates to the production process and applications of the demucilaged flax sprouts . the present invention further relates to a process for recovering mucilaginous substance generated as a by - product in the production process as well as to various applications thereof .