in step ( a ), wet gums can conveniently be obtained by treating crude vegetable oil such as soybean oil , rapeseed oil , sunflower seed oil and the like with warm water or live steam . this treatment is preferably carried out immediately after the extraction solvent has been removed from the oil miscella by evaporation . at that point in time , the crude oil has a temperature that hardly needs any adjusting for the water degumming process to be carried out . the amount of water to be used in the water degumming process varies but it is commonly about equal to the amount of mucilaginous matter to be removed from the crude oil by the water degumming process . accordingly , the wet gums obtained by this process usually have a water content in the range of 40 to 60 % by weight , but the process of the invention is in no way limited to a starting material with this water content . the temperature of the wet gums will hardly have changed during the water degumming process so that it will preferably be in the range of about 40 to 90 ° c . accordingly , the expense of heating or cooling the wet gums can often be avoided but the process of the invention in no way excludes a temperature adjustment of the wet gums before they are mixed with water containing a phospholipidolytic agent in step ( b ). this mixing step ( b ) is preferably carried out continuously but a batch operation is also possible . it has been found to be advantageous to mix the wet gums with the water containing a phospholipidolytic agent as soon as they become available from the water degumming process . then , these gums can still be considered to be sterile but when cooled and infected they may become subject to microbial spoilage . on the other hand , this spoilage is effectively avoided by the use of an acid phospholipidolytic agent . the water to be mixed into the wet gums is preferably brought to about the same temperature as that of the wet gums before being mixed with these gums but on the other hand , the water temperature can also be used to adjust the temperature of the mixture . if it is for instance deemed to be desirable that this temperature after mixing is lower than the temperature of the wet gums , the water to be mixed with the wet gums can be brought to a temperature that is lower than the temperature after mixing . this may be desirable when an enzymatic phospholipidolytic agent is employed . the amount of water to be mixed with the wet gums has been found to be hardly critical . mixtures with a dry matter content of about 15 weight % have been found to permit a good oil recuperation but this dry matter content can also be as high as about 40 weight % or even higher . since according to the invention this mixture will subsequently undergo a separation step ( c ) and an oil recuperation step ( d ), the volume of the mixture is therefore preferably minimised to a dry matter content of about 30 to 40 weight %. the acid which may be used as phospholipidolytic agent has been found not to be critical but food grade acids such as phosphoric acid or citric acid are preferred . accordingly , citric acid aqueous solutions with acid concentrations as low as about 3 weight % and as high as about 30 weight % have been found to be effective in hydrolysing the phospholipids present in the wet gums . however , lowering concentrations increases the holding time required for oil separation and the amount of recuperated oil may also be less than when for instance an acid concentration of about 9 weight % is employed . using much higher concentrations than about 9 weight % offers no significant advantages and although the acid water phase can be recycled , ( step e ) a high acid concentration also leads to an increased consumption of the acid . another phospholipidolytic agent that can profitably be used in the process according to the invention is a phospholipase , preferably a hydrolytic enzyme like lecitase ultra as produced by novozymes as ( bagsvaerd , denmark ). this is a microbial enzyme produced by t . lanuginosa and which acts as a phospholipase a1 . without wishing to be bound by theory , it is believed that this enzyme does not operate at the oil - water interface but rather in the oily phase . the optimum temperature for using this enzyme is usually within a range from about 50 ° c . to 60 ° c . ( depending upon ph , as is well known to the skilled person ), which means that the wet gums may have to be cooled down to or around this temperature before enzyme addition . the amount of enzyme to be used is again not critical . an amount within a range of about 50 ppm to 1 , 000 ppm , preferably 100 ppm to 250 ppm ( ranges based on the following text and suggested claim 5 ) calculated on the basis of dry matter to be treated has been found to be effective . much higher amounts are unnecessary for the efficiency of the invention . recycling the enzyme solution may be performed if necessary , depending upon the balance between enzyme consumption and cost for recycling . the mixing operation itself must ensure that the phospholipidolytic agent is thoroughly mixed through the wet gums . accordingly , an industrial execution of the process of the invention preferably employs a high shear , in - line mixer such as used for example for mixing caustic soda with oil during the chemical neutralisation process of edible oils . these can be rotary mixers such as for instance commercially available from westfalia separator food tec gmbh , oelde , germany , or static mixers of the kenics type . the separation stage ( c ) of the process according to the invention can be carried out in various ways , depending upon the oil recuperation method to be used subsequently . if this recuperation ( d ) is by overflow from a holding vessel , the contents of this vessel should preferably not be agitated . if on the other hand , the recuperation is by use of a decanter or centrifugal separator , a reasonably homogenous feed to this piece of equipment is preferred . then a gentle agitation of the holding vessel is preferably required to prevent its contents from settling . according to the process of the invention , a certain minimum holding time during the separation stage ( c ) between the high shear mixing stage ( b ) and the oil recuperation stage ( d ) is preferably required for the oil exudation to take place . macroscopically it can be observed that the fine and stable emulsion that is characteristic of the wet gums as obtained during water degumming gradually changes into a much coarser and less stable emulsion . this reduced stability manifests itself by oil moving upwards and an aqueous phase moving downwards when the mixture of the wet gums and the acidified water is left stagnant . however , in the process of the invention , three or even four different phases can be observed during this separation stage ( c ). the rate of oil exudation has been observed to vary with time . in the beginning , little seems to happen and the rate is low or even zero . then an oily top layer is formed at increasing rate but after a while , this rate decreases again . finally , macroscopic changes become hardly noticeable . at that point in time , there is no need to continue the separation stage but it could have been terminated before , for instance when the rate had dropped to about one third of the maximum rate observed . the top layer ( 1 ) is the oily layer to be recuperated . since the recuperation process according to the invention employs a phospholipidolytic agent , the phosphatides present in the wet gums will be partially hydrolysed during step ( c ) of the process , which hydrolysis will lead to the liberation of free fatty acids . these acids are oil - soluble and will thus be concentrated in the oil present in the system and thus also in the top layer ( 1 ). accordingly , the recuperation process according to the invention does not only liberate neutral oil from wet gums , it also liberates free fatty acids from phosphatides and then incorporates these free fatty acids into this neutral oil . since this is the oil to be recuperated and subsequently sold as crude oil , the phospholipidolytic agent thus increases the amount of crude oil to be sold and thus the profitability of the process . bottom layer ( 4 ) contains the phospholipidolytic agent and is therefore preferably recycled . however , the aqueous bottom layer may become enriched in water - soluble compounds present in the wet gums such as sugars . therefore a certain purge may become desirable whereby the extent of the purge mainly depends upon the agricultural origin of the crude oil . this purge is only necessary when the purge provided by the intermediate layers ( 2 ) and ( 3 ) is found to be insufficient . the two intermediate layers ( 2 ) and ( 3 ) contain the partially hydrolysed phosphatides . they also contain the triglyceride oil that has not floated to the top layer ( 1 ) and part of the aqueous phase . accordingly , the separation between the various layers need not be perfect . if the recuperated oil in top layer ( 1 ) contains a bit of layer ( 2 ), this will usually not cause the crude oil to which this layer is sent to be outside the crude oil specification . similarly , if the aqueous bottom layer contains some phosphatides , these may be separated from the aqueous layer next time and thus sent to the meal that time . the use of a three - phase decanter that simultaneously isolates the oily phase ( 1 ) and the aqueous bottom phase ( 4 ) from the two intermediate phases has been found to be advantageous and is therefore preferably recommended . the following examples are provided for illustration only and should in no way be understood as restricting the scope of the present invention . this illustrates the stability of wet gums as obtained by water degumming crude vegetable oil . a sample of wet gums resulting from water degumming crude soybean oil was analysed and found to contain 41 . 9 weight % of water . its dry matter was also analysed and found to contain 37 . 3 weight % acetone soluble matter with a 5 . 7 % free fatty acid content ( expressed as oleic acid ) and 2 , 335 ppm of phosphorus . an amount of 574 g of these wet gums was heated to 75 ° c . and mixed with warm distilled water to obtain a total weight of 1 , 060 g and agitated at 350 rpm for 1 hour . the mixture was then transferred to a 1 l measuring cylinder and placed in a water bath kept at 70 - 80 ° c . the cylinder was monitored regularly for phase separation and quite soon an aqueous bottom layer was observed but even after 48 hours only a very few drops of oil could be observed at the surface of the mixture . apparently , under the conditions employed in this example , the wet gums form a quite stable emulsion that does not allow any oil to be recovered . the same sample of wet gums as in example 1 was used in an experiment involving acidified water . this acidified water contained 5 % by weight of citric acid . the same weights of wet gums ( i . e . 574 g ) and water ( i . e . 486 g ) were used as in example 1 and the mode and time of mixing were also the same . however , the behaviour of the mixture in the measuring cylinder was totally different . when the cylinder was filled , a water phase of 150 ml separated almost immediately and after 1 hour , this phase had increased to 210 ml . after 2 hours , an oily top layer could be noted that was still quite small (& lt ; 10 ml ), but at 4 hours after filling the cylinder , this oily layer had increased to 20 ml , the aqueous bottom layer had increased to 310 ml so that the layer in between had decreased to 670 ml . during the remainder of the experiment the oily top layer increased to 60 ml and the aqueous bottom layer increased to 610 - 620 ml . very surprisingly the intermediate phase separated into two distinct layers , the upper one of which reached a volume of some 200 ml at 48 hours after filling the cylinder so that the lower layer accounted for 150 ml . analysis of the oily top layer revealed that its free fatty acid content had increased considerably from 5 . 7 % to 28 . 4 %; its phosphorus content ( 2 , 635 ppm ) had hardly increased in comparison with the crude oil . accordingly , this oily layer could be recuperated in full by mixing it with the crude , water degummed oil . in a similar experiment as example 2 , but employing 800 g of the same citric acid solution ( 5 % by weight ) and 200 g of the same wet gums , the phosphatide compositions of the two intermediate phase layers were determined , by using 31 p - nmr ( nuclear magnetic resonance ), by spectral service gmbh ( cologne , germany ). this determination showed that the lyso - content of the phosphatides had increased from 1 . 7 % in the starting material to 45 . 3 % in the upper phosphatide layer ( 110 ml ) and even to 51 . 2 % in the lower phosphatide layer ( 20 ml ). accordingly , the average lyso - content of the two layers was 46 . 2 % and had thus increased by 44 . 7 %. the citric acid had thus acted as phospholipidolytic agent . the acetone insoluble content of the gums used as starting material in this experiment was 35 % so that about 70 g phosphatides were used . hydrolysing these 70 g phosphatides to 46 . 2 % lyso - phosphatides liberated some 15 g of free fatty acids . the acetone soluble fraction was 21 . 5 % so the amount of triglyceride oil present in this experiment was 43 g . the oily layer ( 30 ml or 27 g ) showed a free fatty acid content ( by titration ) of 29 . 9 % so that the total amount of free fatty acids present in the original 43 g of oil is some 18 g . this figure is quite close to the amount of free fatty acids formed by the hydrolysis of the phosphatides during the process according to the invention . accordingly , the process according to the invention only causes phospholipids to hydrolyse and leaves triglyceride oil intact . again the sample of wet gums as described in example 1 was used to study the effect of the use of a phospholipase enzyme on oil recuperation . the amount of wet gums was 583 g and these were mixed with 477 g water containing lecitase ultra ( novozymes as , bagsvaerd , denmark ). the amount of the enzyme was 250 ppm calculated on the dry matter in the gums . the mixture was held at 55 c . very little happened in the beginning and after 5 hours no phase separation could be observed at all . however , after some 20 hours , four distinct layers were clearly visible and after 92 hours , the oily upper layer , having a free fatty acid content of 24 . 7 % amounted to 70 ml . given the dry matter content of the gums of 58 . 1 % and the acetone soluble content of the dry matter of 37 . 3 %, this corresponds to some 126 g in this example . thus a recuperation of 70 ml ( 63 g ) amounts to some 50 % of theory when the free fatty acids are not taken into account . a different sample of wet gums was used in this example . it was also obtained by water degumming soybean oil and its water content was 46 . 0 %. on a dry basis its impurities content ( hexane insoluble ) was 2 . 1 %, its acetone insoluble content was 64 . 4 % and thus its acetone soluble content was 33 . 5 %. an amount of 554 g of gums was mixed with about 370 g of four different citric acid solutions with concentrations of 1 %, 3 %, 9 % and 30 % by weight respectively at a temperature of 75 ° c . the mixtures were agitated for a period of 1 hour at 120 rpm whereupon they were transferred to measuring cylinders that were positioned in a water bath kept at 70 - 80 ° c . no oily layer appeared in the measuring cylinder containing the mixture prepared with the 1 % citric acid solution . apparently , this acid concentration is insufficient for phospholipidolytic activity . the 3 % by weight concentrated solution caused an oily layer of 10 ml to appear after some 30 hours , which layer increased to 25 ml after 40 hours and stabilised at 30 ml after 48 hours . this leads to the conclusion that an acid concentration of 3 % citric acid already has a marked phospholipidolytic activity . higher acid strengths have a higher activity since the oily layer resulting from an acid concentration of 9 % by weight amounted to 30 ml after 20 hours and even 40 ml after 48 hours . increasing the acid concentration to 30 % by weight led to both a faster oil separation and a more extensive separation in that a layer of some 10 ml was already discernable after 4 hours and that the final layer amounted to 50 ml attained after 65 hours . in this example phosphoric acid was used as the phospholipidolytic agent . an acid concentration of 9 % by weight was chosen and the temperature was 75 ° c . using again some 554 g of wet gums ( same as used in example 5 ) and 373 g phosphoric acid solution , an oily phase of 50 ml ( 45 . 6 g ) resulted after some 48 hours . this oily phase had a free fatty acid content of 31 . 5 %. it also had a higher phosphorus content than the samples treated with citric acid according to examples 2 to 5 . analysis of the phosphatide layer showed its lyso - content to be 40 % which is well in line with the free fatty acid content of the oily layer . the example also shows that the chemical nature of the phospholipidolytic acid is not critical . using the gum sample of examples 5 and 6 , lecitase ultra was employed as a phospholipidolytic agent in an amount of 250 mg per kg dry gum matter and at a temperature of 55 ° c . again , the appearance of an oily layer was slow in that after 6 hours no oily drops could yet be discerned ; these appeared after some 30 hours and after 120 hours the oily layer amounted to 77 % of the oil present in the gums . in addition , the phosphorus content of the oily layer at 65 ppm was lower than with any other phospholipidolytic agent studied and this also holds for the iron , calcium and magnesium contents of the oily layer resulting from the use of the phospholipase enzyme . the oily layer also had a less pronounced colour than attained by the use of an acid phospholipidolytic agent in examples 2 to 6 .