Patent Application: US-52543505-A

Abstract:
it is disclosed a low - cholesterol whole shrimp a method of obtaining same comprising : to provide a plurality of frozen , peeled and deheaded shrimps ; to freeze drying the whole shrimps to a humidity content of approximately 1 to 10 %; to extract the cholesterol from the dehydrated shrimps by means of a stream of a supercritical solvent which is selective to lipids , at a temperature between 36 - 39 ° c . and at a pressure between 275 - 345 bar ; to rehydrate the shrimps in a vacuum chamber with water in a relationship of about 1 - 10 ml per g shrimp at vacuum and room temperature by about 1 - 5 hours ; and to cook said plurality of whole shrimp with steam .

Description:
the present invention refers to a low - cholesterol shrimp obtained from any of the species from the subgenus litopenaeus ( l . occidentalis , l . schmitti , l . setiferus , l . stylirostris , l . vannamei ). the procedure is also applicable to other genus , subgenus and species of shrimp and to their different sizes . a natural variability in the content of cholesterol is present among the different shrimp species . however , the process described in this invention will work equally well with only minor adjustments in the processing variables , particularly the volume of supercritical fluid used . a second aspect of this invention pertains to the process to obtain a low - cholesterol shrimp . for this purpose , peeled , headless shrimp are used as raw material . the proposed procedure consists of an initial dehydration step . the dehydrated shrimp immediately pass to the next processing step which consists of supercritical extraction of cholesterol using a highly selective solvent for lipids at a nominal pressure and temperature . for this purpose , supercritical extraction equipment with carbon dioxide as the supercritical fluid is utilized . the dehydrated shrimp are placed in the equipment extraction unit and carbon dioxide is compressed above its critical pressure ( 100 - 400 bar ). the resulting gas enters the extraction unit supplied with a heating jacket to allow the extraction temperature to be maintained in a range from 30 - 60 ° c . and pass through the sample to remove the cholesterol . this process can be applied to any shrimp species and sizes with slight variations in the operating conditions . the discharge gas containing the extract is then passed through an expansion valve . at this point the extract is released from the gas by precipitation since a pressure differential under supercritical conditions implies a decrease in density and a lowering of the solvating capacity . dehydrated shrimp containing lower cholesterol content are thus obtained and reconstituted with water using a ratio of 1 to 10 ml per gram of shrimp . rehydration is carried out by placing shrimp in a vacuum chamber at room temperature for a period of 1 - 5 hours . the dehydrated shrimp is steam - cooked before presentation to the final consumer in its original shape . the final product obtained through this process is a low - cholesterol shrimp which is a non - existent product up to the time of this invention . additionally , this product complies with all the nutritional labeling requirements established for low and reduced - cholesterol products by the food and drug administration . according to such requirements a cholesterol - reduced product must contain 75 % or less cholesterol than the original food from which it is obtained , and for a low - cholesterol product it must contain from 2 to 20 mg of cholesterol per serving ( fda , 1986 ). a standard error of 20 % is allowable in these levels and therefore a cholesterol content of less than 24 mg per serving is acceptable for low cholesterol foods ( fda , 1990 ). the final form of the product , subject of the present invention , consists of whole pieces of shrimp , not in chunks , or dices or powder , as has been the case with other products processed by supercritical extraction . also , the shrimp continues to possess its original sensory characteristics in terms of texture , flavor , color and overall appearance . a sensory test was performed to evaluate each of these attributes on dehydrated and supercritically - extracted shrimp after rehydration and cooking . such shrimp corresponded to the category of low - cholesterol shrimp ( less than 24 mg of cholesterol per serving ). the test was applied to a panel of 30 untrained subjects each of whom evaluated sample color , odor , and overall appearance . the evaluation score was from − 3 a + 3 . for a statistical analysis a non - parametric kolmogorov - smirnov test was performed . all attributes evaluated had a positive score from the panel members and no significant differences were evident in the acceptance scale . the texture and flavor attributes had a moderate acceptance score (+ 2 ) while smell , color and overall appearance gave a slight acceptance score (+ 1 ) ( fig1 ). in relation to smell and taste , several panelists observed that a favorable condition had been caused by the supercritical extraction process since it diminished the typically - strong smell of the product . these results show promising perspectives for the overall acceptance of low - cholesterol shrimp by the end consumer . the following example is used to illustrate the novelty and utility of the present invention , without intention to limit any of its aspects . the raw material used was “ blue shrimp ” ( litopenaeus stylirostris ) and “ white shrimp ” ( litopenaeus vannamei ), 16 - 20 count per pound and deheaded , which were kept under frozen storage (− 18 ° c .) until processed . shrimp are thawed , peeled and individually refrozen at − 40 ° c . for a period of 4 hours using a quick freezing system . the shrimp are then freeze - dried until a final water content of 1 - 5 % is reached . the temperature on the products surface as well as that inside is carefully monitored using thermocouples . when the equipment reaches a 0 . 1 mm hg vacuum the following program of conditions is to be followed : temperature ° c . time hs 29 1 0 1 50 4 - 5 a 35 15 - 20 b 25 1 - 3 c a the time will depend on the level of vacuum achieved , which should not exceed 0 . 2 mm hg . b the time will depend on when the shrimp reach a maximum temperature of 5 to 10 ° c . c depending on when the internal shrimp temperature becomes the same as that on their surface . once the freeze drying process is completed , the shrimp are ready for the extraction of cholesterol . cholesterol extraction is carried out in a supercritical extractor using a selective solvent ( carbon dioxide ) under supercritical conditions of 310 bar and 37 ° c . for this purpose supercritical extraction equipment with carbon dioxide is used . the extraction system consists of four basic components : a compressor or solvent pump , an extractor , a control system for pressure and temperature and a separator . once the shrimp have been placed within the extraction vessel the carbon dioxide is allowed to flow from the storage tank and through the compressor in order to attain the supercritical pressure of 310 bar . the resulting gas enters the extraction chamber containing a heated jacket which allows the operating temperature to be maintained at 37 ° c . upon contact of carbon dioxide with the shrimp sample , a process of selective extraction begins and the gaseous carbon dioxide picks up the free cholesterol in the shrimp tissue and produces a cholesterol - rich extract . both the volume of carbon dioxide and the flow speed are measured carefully . the flow speed should be maintained at 5 . 5 - 6 . 2 l / min but other flow velocities can also be used . once the supercritical extraction process is completed , the shrimp are subjected to rehydration using water at room temperature in a relationship of 5 ml of water per gram of shrimp . this process should take place under vacuum ( 533 mm hg ) for at least one hour . at the end of this period the shrimp is turned on its side and allowed to rehydrate under the same conditions for one more hour . upon rehydration , shrimp can be steam - cooked and later packaged in plastic containers under vacuum and quickly - frozen at − 40 ° c . the final product obtained with this process conditions complies with the requirements set forth by fda for low cholesterol food products . a surface response methodology was followed during the course of experimentation with the aim of determining the optimal conditions for cholesterol removal from shrimp by supercritical extraction . a compounded - central rotatory design was applied for three independent variables with five levels for each one . the number of experimental points in the design was sufficient to prove the statistical validity of the quadratic model obtained ( arteaga et al ., 1994 ). the variables used in the stage of cholesterol extraction were : pressure ( x 1 ), volume ( x 2 ) and temperature ( x 3 ). the minimum and maximum levels of the variables were fixed according to results obtained in preliminary experiments . the response variable ( y ) was the amount of cholesterol remaining in the final product ( dry weight basis ) as determined by gas chromatography . table i shows the average values of the remaining cholesterol content in the end product and the corresponding extraction index (%). table i y x1 x2 x3 cholesterol cholesterol p v t ( mg / 100 g ) ( mg per serving ) extraction treatment ( bar ) ( lco2 ) (° c .) dry basis wet basis % 1 289 909 36 225 . 10 52 . 25 61 . 99 2 331 909 36 292 . 71 67 . 95 50 . 56 3 289 2841 36 151 . 41 35 . 15 74 . 43 4 331 2841 36 81 . 96 19 . 26 85 . 99 5 289 909 38 224 . 88 52 . 20 62 . 02 6 331 909 38 211 . 06 49 . 00 64 . 35 7 289 2841 38 72 . 19 16 . 76 87 . 81 8 331 2841 38 52 . 02 12 . 08 91 . 21 9 275 1875 37 114 . 25 26 . 52 80 . 70 10 345 1875 37 99 . 23 23 . 03 83 . 24 11 310 250 37 366 . 61 85 . 11 38 . 08 12 310 3500 37 62 . 14 14 . 43 89 . 50 13 310 1875 35 125 . 44 29 . 12 78 . 81 14 310 1875 39 97 . 25 22 . 58 83 . 57 15 310 1875 37 99 . 68 23 . 14 83 . 16 in order to generate an equation that forecasts the effects of operating conditions ( x 1 , x 2 , x 3 ) on the cholesterol quantity remaining in the final product , a regression program was run . by multiple regression analysis a quadratic model was adjusted and a final regression equation calculated : y = 6065 . 3575 − 0 . 608833 p + 0 . 1424819 v − 303 . 0457 t + 0 . 0147289 p 2 − 0 . 000884 vp + 0 . 0000475 v 2 − 0 . 191346 tp − 0 . 003532 tv + 4 . 7773254 t 2 y = remaining cholesterol in final shrimp product ( mg / 100 g ) dry weight basis the results from the analysis of variance for the quadratic model of prediction are presented in table ii wherein a significant effect of the adjusted model ( p ≦ 0 . 05 ) is evident . also , the lack of fit resulted non - significant ( p & gt ; 0 . 05 ). this information supports the validity of the model . table ii source of variation df sum of squares mean square f - ratio p r 2 regression 9 121477 . 4 13497 . 49 18 . 31 0 . 000202 0 . 953705 linear effect 3 94030 . 26 31343 . 42 42 . 52 0 . 000029 0 . 738221 quadratic effect 3 24653 . 4 8217 . 8 11 . 15 0 . 003140 0 . 193551 interactions 3 2793 . 743 931 . 2475 1 . 26 0 . 350317 0 . 021933 total error 8 5896 . 731 737 . 0914 0 . 046295 lack of fit 5 5288 . 337 1057 . 667 5 . 22 0 . 102269 0 . 041518 pure error 3 608 . 3936 202 . 7978 0 . 004776 according to the analysis of variance , some linear and quadratic effects were significant ( p ≦ 0 . 05 ) for the supercritical extraction process from shrimp , with the most important quadratic effect being that of volume . fig2 shows a surface response graph which illustrates the final regression equation obtained through this experimentation . the effect of supercritical extraction operating conditions on the remaining shrimp cholesterol content on a dry weight basis highlights the effect of different solvent volumes required , according to the final cholesterol content desired . fig3 shows the amount of remaining cholesterol in the shrimp ( on a dry weight basis ) as a function of temperature at different volumes of carbon dioxide and a pressure of 345 bar . it can be observed that at such pressure the quantity of remaining cholesterol decreases with an increase in the volume of carbon dioxide with respect to temperature . in a supercritical fluid , the effect of temperature on solubility is quite complex due to two concurrent effects . one effect tends to increase solubility with an increase in temperature , while the other tends to decrease it . as the temperature increases , the solute vapor pressure also increases and this increases solubility . on the other hand , density decreases and this tends to decrease solubility . in this experimental region density is less sensitive to temperature changes and the vapor pressure is the dominant factor so that increases in temperature increase solubility . the temperature at which a minimum of cholesterol content remains is 39 ° c . ( 11 . 77 mg / 100 g , dry weight basis ). nevertheless the remaining amount of cholesterol ( 100 mg per 100 g of shrimp , on a dry weight basis ) is sufficient to achieve the fda requirements for a low - cholesterol food product once it has been rehydrated and cooked , i . e . less than 24 mg per shrimp serving on a wet basis . from fig4 it can be observed that with the conditions given in the example provided for this invention the residual cholesterol content attained is 100 mg per 100 g of shrimp on a dry weight basis . it is clear from fig3 and 4 that with different combinations of operating conditions during supercritical extraction , the same result is achieved . the conditions given are less drastic so that their adverse effects on the sensory properties of the final low - cholesterol shrimp product are significantly decreased . arteaga , g . e ., e . li - chan , m . c . vazquez - arteaga and s . nakai . 1994 . systematic experimental designs for product formula optimization . trends in food science & amp ; technology ( 5 ): 243 - 254 . cully j ., vollbrecht heinz - ruediger and schuetz e . 1991 . process for the removal of cholesterol and / or cholesterol esters from foodstuffs . de3929555 . dziezak , j . d . 1986 . innovative separation process finding its way into the food industry . food technology . 66 - 69 . fda . 1986 . proposals for cholesterol - free and low cholesterol foods . u . s . food and drug administration . fed . register ( november 25 ) 51 : 42584 . fda . 1990 . food labeling . 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