NZ207666A

NZ207666A - Treating soybean material with alcohol

Info

Publication number: NZ207666A
Application number: NZ207666A
Authority: NZ
Inventors: N G Stahel
Original assignee: Land O Lakes Inc
Priority date: 1984-03-28
Filing date: 1984-03-28
Publication date: 1987-08-31

Description

<div class="application article clearfix" id="description"> New Zealand Paient Spedficaiion for Paient Number £07666 S 9 6 RegIl9U) Fee: $80.00 7666 fnorityOd-fcoO c^es. ^..3^- Pubiicat'a-i p-0. Jcur.iaf, iyn: 3 i' AUG 1987 ■ 1! Insert number of Provisional Speci fication(s) (if any) and date(s) of fiLing; otherwise leave blank. PATENTS ACT 195 3 Number: Da te: COMPLETE SPECIFICATION N-Z. PATENT OFf ICE 28MARW84*JI ;received. ;Insert Title of Invention. ;Insert full name, full street- address and nationality of (each) applicant. ;IMPROVED METHOD OF TREATING SOYBEAN MATERIAL ;&/WE LAND 0'LAKES, INC. of 4001 Lexington Avenue North, Arden Hills, Minnesota 55112, United States of America, a corporation organized under the laws of the state of Minnesota, United States of America hereby declare the invention for which I/we pray that a patent may be granted to me/us and the method by which it is to be performed, to be particularly described in and by the following statement:- ;Indicate if following page is numbered '1(a)' ;- 1 - ;c. 0 / 66 o ;- 2 - ;IMPROVED METHOD OF TREATING SOYBEAN MATERIAL BACKGROUND OF THE INVENTION 1. Field of the Invention. ;The present invention relates to the preparation of improved high-protein food products from soybeans, in particular, it relates to a process for making the soybean food product more digestable and for removing a substantial amount of the undesirable flavor constituents using lower alcohols. ;2. Description of the Prior Art. ;The use of alcohols as a solvent in the extraction of oil from soybeans is noted in the two volume treatise on "Soybeans and Soybean Products," edited by Markley, inter science, 1950 . In one instance, mentioned by the editor, as being described by Beckel and Smith in Vol. 16 of "Food Industries," 1944, pages 616-644, alcohol with a small proportion of water was used under- pressure to extract the oil while avoiding denaturization of the protein. . ;Nbre recently, in the Moshy United States Patent Specification No. 3,168,406, a process is disclosed wherein alcohol and water are used to treat soybean meal to make the soybean meal bland and odorless. The process includes mixing soybean flour with alcohol to form a slurry such that the pH is adjusted to the isoelectric range of soy proteins, that is about pH 4-6. The slurry is then heated to a temperature range of 175?-212°F (79°-100°C) and cooked for preferabl,^!1^^^^. ;/v ' B ;r 15 JUNI987ii- ;C \J I (j(ob ;- 3 ;minutes. The supernatent liquid is then removed from the soybean flour by any well known process and the resulting filter cake is washed a number of times with water to remove the alcohol. In one example, the filter cake was dried in a vacuum pan dryer at 28 inches (71 centimeters) of vacuum at 110°F (43°C). ;In the Kakade United States Patent Specifications Nos 4,079,155 and 4,132,808, which are assigned to the same assignee as the present application, a proteinaceous soybean material is subjected to a lower alcohol vap^r in a pressure chamber under superatmospheric pressure. Simultaneously, the alcohol vapors are slowly and continuously removed from the chamber to volatilize certain undesirable flavor constituents, carrying off the flavor constituents with the escaping vapors. Although the process, as disclosed in the Kakade Patents, produces a satisfactory product in terms of a bland and odorless soybean product, a considerable amount of alcohol is used. Specifically, the ratio of alcohol to soybean flour used was 33 pounds (15.0 kilograms) of alcohol to 60 pounds (27.2 kilograms) of soybean flour or approximately one part of alcohol to every two parts of soybean flour that is treated. ;SUMMARY OF THE INVENTION The present invention is an improved process for treating soybean material to make the soybean material ;process uses a substantially smaller amount of alcohol than other known processes to remove the undesirable flavor constituents naturally found within the soybean meal and directly subjects the soybean material to a minimal amount of steam. ;material in a closed vessel and adding the alcohol to the soybean material -tn a preferred ratio of approximately at least 9 pounds (4.1 kilograms) material to 60 pounds (27.2 kilograms) soybean material. The vessel has suitable agitators that agitate the soybean material sufficiently to "fluidize" the material within the vessel. Steam is injected into the vessel and through the soybean material, heating the material to a preferred treatment temperature of approximately 220°F (104°C). The combination of the alcohol vapor and the fluidization of the soybean material maximizes the efficient use of the alcohol in altering the structure of the protein for better digestability of the soybean meal and extracting undesirable flavor constituents from the soybean meal. ;reached a temperature of approximately 220°F (104°C), the flow of steam to the material is stopped and the material is sustained at approximately 220°F (104°C) ;using a suitable heat source within the vessel, such as steam within a jacket in the vessel, until the soybean material reaches ;PDI of less than 10. Minimizing direct contact of steam with the ;Briefly, the process includes placing the soybean ;When the proteinaceous soybean material has ;207666 ;- 5 - ;soybean material avoids unnecessary soaking and overcooking of the soybean material. After thirty minutes, the vessel is vented at subatmospheric pressure thereby removing substantially all of the alcohol from the 5 proteinaceous soybean material. ;DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS ;The present invention employs a process which uses a minimum amount of a lower alcohol in treating a proteinaceous soybean material to remove undesirable 10 flavor constituents and odors from the soybean material without overcooking. The lower alcohols useful in the process are methyl, ethyl and isopropyl alcohols although presently ethyl alcohol is preferred. Using a minimal amount of alcohol decreases several costs including the 15 initial purchase cost of the alcohol, the disposal of the alcohol after usage and the cost of keeping track of the amount of alcohol in the user's possession per various government regulations. The proteinaceous soybean material is preferably in the form of a soybean flour, 20 however, the process also works quite well on soy flakes before they are ground into flour. ;The process may be applied to full-fat, low-fat or defatted cracked beans, grits or flour, although its greatest field of utilization appears presently to be in 25 the treatment of defatted flour. Pretreated and partially denatured soybean materials such as, for example, those that have been heat-treated during extraction, tempering, ;2 076 66 ;- 6 - ;flaking or grinding, may also be improved by the present process, including such materials as those partially denatured products having a PDI (protein dispersability index) of as low as 20 or 30. ;5 Preferably, the soybean flour has a PDI of approximately 90. The process of the present invention decreases the PDI to approximately less than 10. The PDI is useful as a measure of the denaturization that occurs in the soy protein of the flour that alters the structure 10 of the protein molecule resulting in the soybean material being more digestable. As the PDI of the flour is decreased, the denaturization of the protein is increased. It is believed that the molecular structure of the soybean is so changed that it can be more readily 15 attacked by the enzymes and microorganisms of the digestive system. ;The soybean material is contained within a closed vessel having an agitator. The material is continuously agitated such that the material within the bed is 20 "fluidized". ;In a preferred process as is discussed further in a subsequent example, the vessel used to treat the soybean meal is a commercially available reactor, known as "DVT", manufactured by Littleford Bros., Inc. of Florence, 25 Kentucky. The reactor has a central shaft with plough-shaped blades and at least one additional agitator, positioned on an inner wall of the vessel rotating at a ;2076 6h ;- 7 - ;higher speed than the central shaft with plough-shaped blades. The combined rotation of the agitators and ploughs and the speed at which they are rotated "fluidize" the soybean material within the reactor. ;A pressure of approximately 15 PSI to 26 PSI is used within the vessel in treating the soybean material. In a preferred system, ethyl alcohol is initially present along with a minor amount of water with the soybean material. Live steam is introduced in. a suitable manner into the vessel, heating the proteinaceous soybean material and vaporizing the alcohol and water such that the soybean material is placed in intimate contact with the alcohol vapor. Sufficient amounts of live steam are injected into the vessel to bring the temperature of the proteinaceous soybean material to preferably 220°F (104°C) and then the steam is turned off. ;Through experimentation it has been determined that the desirable amount of alcohol that should be used is 9 pounds (4.1 kilograms) of alcohol to every 60 pounds (27.2 kilograms) of soybean material. Substantially less alcohol such as 6 pounds ;(27.2 kilograms) does not sufficiently treat the soybean material. Although 9 pounds (4.1 kilograms) of alcohol to 60 pounds (27.2 kilograms) of soybean material is a preferable ratio, more alcohol can be used to obtain a satisfactorily treated soybean material and greater ratios of alcohol are includable within the present invention. ;076 66 ;However, greater ratios of alcohol increase the cost of treating the soybean material. ;The vessel containing the proteinaceous soybean material is preferably a jacketed vessel having a suitable 5 heating medium such as steam supplied into the jacket. The heat from the jacket sustains the proteinaceous soybean material at approximately 220°F (104°C) during the course of treating the material with the alcohol vapors while minimizing direct contact of the soybean material 10 with steam. The proteinaceous soybean material is sustained at 220°F (104°C) for approximately at least thirty minutes which allows sufficient time for the alcohol to extract the undesirable flavor constituents from the soybean material and produce a digestable soybean 15 material. ;The previously-mentioned requirements are subject to some variation depending upon the temperature and the time the soybean material is treated with the alcohol. For example, if 240°F (115°C) was used to treat the 20 material, then the soybean material would be held at approximately 240°F (115°C) for approximately 5 minutes. It has been found that the top temperature that can be used to treat the soybean material without detrimental effects to the material is approximately 280°F (138°c) 25 with no hold time. Once the temperature reaches 280°F (138°C), the treatment with alcohol is stopped as discussed subsequently in Example 2. Exceeding the ;2 076 6 6 ;temperature and time constraints generally results in a burned product that is grainy and brown in color. It has also been found that proteinaceous soybean material treated at 190°F (88°C) for any length of time produces 5 an unacceptable product. An acceptable product is reached at approximately 200°F (93°C) and a product having preferred qualities achieved at a treatment temperature of at least 215°F (102°C) for at least thirty minutes. However, in all cases the process parameters are so 10 selected as to reduce the PDI to well below the initial value, and generally to a final value of no higher than 10. ;After the proteinaceous soybean material has been sufficiently treated with the alcohol vapors, the vessel is vented to a vacuum environment, preferably 25-26 inches 15 (63-66 centimeters) Hg with a vacuum pump. At 25-26 inches (63-66 centimeters) of Hg, water boils at approximately 126°F (52°C). The proteinaceous soybean material is kept at preferably approximately 130°F (54°C) and no higher than 135°F (57°C) to remove the alcohol 20 vapor without browning the proteinaceous soybean material. A preferred temperature range during venting to remove the alcohol from the proteinaceous soybean material is approximately 125°F to 130°F (52°C to 54°C). ;The low PDI value of less than 10, obtained in 25 soybean materials processed in accordance with the present invention, makes possible the preparation of a high protein concentrate with minimal loss of protein values. ;2 076 66 ;- 10 - ;Simple water extraction may be used to remove the water-soluble and none-nutritive carbohydrate components without appreciable loss of the protein. The result after drying is a concentrate containing at least about 70% of 5 total protein by Kjedahl Nitrogen, Association of Official Analytical Chemists, method 2.057, 1980 13th Edition. The high protein content and a substantial absence of undesirable flavor constituents render the product particularly attractive as a food supplement. The food 10 supplement is especially useful in the feeding of young domestic animals, ruminant or otherwise, which employ monogastric digestion, e.g., calves. The product obtained through the process of the present invention when combined with other materials in a milk-like form, i.e., a fluid 15 mixture of soybean flour and other materials in water, when, fed to calves or other young domestic animals, provides a significant, increase in the growth rate of the animal as compared with that obtained with milk substitutes prepared from conventionally heat-treated 20 soybean products. ;The following examples are illustrative only and are not intended to limit the present invention. The examples are submitted in order to demonstrate more explicitly the process of the present invention. 25 Example 1 ;In a pilot plant process, 60 pounds (27.2 kilograms) of a commercially defatted soybean flour having ;2 076 6 f. ;- 11 - ;a PDI of approximately 90 is loaded into a commercially available reactor known as a "DVT-130-(1-Z) Polyphase Reactor" manufactured by the Littleford Bros., Inc. of Florence, Kentucky having a generally horizontal agitator 5 with plough-type blades and at least one other agitator, referred to as a "chopper". The soybean flour is mixed in the reactor with 9 pounds (2.7 kilograms) of type 3A alcohol (a specially denatured ethyl alcohol - 90% ethanol, 5% methanol and 5% water) and 6 pounds (2.7 10 kilograms) of water. The reactor is then sealed off and the alcohol and water are mixed with the soybean flour using the agitators of the reactor. The agitators in the reactor are turned on and the mixture is blended for approximately 5 minutes. After 5 minutes, steam is turned 15 on into the jacket of the reactor to bring the product temperature to approximately 125°F (52°C). The agitators in the reactor "fluidize" the material for better contact with the alcohol. At approximately 125°F (52°C), a valve is opened and steam is injected directly into the 20 "fluidized" soybean flour/alcohol mixture until the temperature of the flour/alcohol mixture reaches 220°F (104°C). At approximately 220°F (104°C), the steam injection is stopped and the flour/alcohol mixture is held within the reactor for approximately 30 minutes. The 25 flour/alcohol mixture is held at a pressure range of 15 psi to 26 psi within the reactor. If the flour/alcohol mixture temperature starts to fall, steam is introduced ;2 076 66 ;- 12 - ;once again into the jacket of the reactor to hold the temperature at approximately 220°F (104°C) for the 30 minutes. Alternatively, if the flour/alcohol mixture temperature rises, cold water is introduced into the 5 jacket to bring the temperature down to 220°F (104°C). After approximately 29 minutes, the agitators are turned off and the flour/alcohol mixture is allowed to settle. At the end of the 30 minute period, the reactor is slowly vented to 25-26 inches (63-66 centimeters) Hg of vacuum by 10 a conventional vacuum pump. Slow venting prevents the drawing off of excess product into the vacuum lines. After venting, the agitator with the plough-type blades is turned on and the temperature is allowed to fall to approximately 130°F (54°C). At approximately 26 inches 15 (66 centimeters) of mercury the boiling point of water is 126°F (52°C), and the boiling point of ethyl alcohol is 95°F (35°C). By maintaining the reactor temperature at 125-130°F (52-54°C), all of the alcohol is removed from the product and most of the water is removed. After 20 approximately 25-30 minutes of drying, the agitator with the plough is turned off along with the vacuum and the product removed from the reactor and processed further into an animal food supplement. The flour has a generally bland taste with substantially no soybean odor, and a 25 generally white non-grainy appearance having water retentive properties. ;2 076 66 ;- 13 - ;Feeding tests were conducted on calves, in which the calves were fed three types of milk replacer. The first type (A) was an all milk replacer whose source of protein was whey and casein. The second type (B) included 5 soybean material prepared using conventional heat treating of the soybean flour and having a PDI of approximately 20. The third type (C) included soybean material processed in accordance with the present invention. In each case, the protein source was mixed with other common 10 nutrients such as whey, animal or vegetable fat, vitamins, and minerals. The protein source was mixed with the nutrients in approximately the ranges of 26-27% protein source, 22-23% fat based powder, 45-48% whey and 1-1/2% vitamins and minerals. This mixture was then mixed with 15 water to form a milk-like substance which was fed to the animals. In each instance, the test extended for 28 days. ;Table 1 below shows the gain in weight, in lbs., during the tests. Each column represents one 28 day test with the last column, titled "OVERALL", indicating the 20 average of the five tests for each type of replacer. A normalized percentage is given in parantheses in the last column, with the all milk replacer being used as a base of 100% for comparing overall results. As can be seen, the replacer using protein material processed in accordance 25 with the present invention is quite close to an all milk replacer. ;2 07666 ;- 14 - ;TABLE 1 ;Weight Gain in Pounds (Kilograms) in 28 Days ;TEST OVERALL ;REPLACER 12 3 4 5 AVERAGE (%) ;A ;34 ;.9 ;26 ;.9 ;15 ;.9 ;32 ;.3 ;21.1 ;26 ;.2 ;(100%) ;(15 ;.8) ;(12 ;.2) ;( 7 ;.2) ;(14 ;.7) ;( 9.6) ;(11 ;.9) ;B ;23 ;.6 ;20 ;.3 ;15 ;.5 ;16 ;.5 ;13.5 ;17 ;.9 ;(68.3%) ;(10 ;.7) ;( 9 ;.2) ;( 7 ;.0) ;( 7 ;.5) ;( 6.1) ;( 8 ;.1) ;C ;30 ;.5 ;26 ;.9 ;19 ;.4 ;24 ;.1 ;18.1 ;23 ;.8 ;(90.8%) ;(13 ;.8) ;(12 ;.2) ;( 8 ;.8) ;(10 ;.9) ;( 8.2) ;(10 ;.8) ;Table 2 shows the replacer consumption per calf for 28 days for the trials conducted in Table 1 and indicates that the calves in the test ate approximately the same amount of milk replacer. ;TABLE 2 ;Replacer Consumption - pounds (Kilograms) Per 28 Days Per Calf ;TEST OVERALL ;REPLACER 12 3 4 5 AVERAGE ;A ;46 ;.55 46 ;.23 40 ;.03 47 ;.68 36 ;.82 ;43 ;.46 ;' (21 ;.13)(21 ;.09) (18 ;.17)(21 ;.65)(16 ;.72) ;(19 ;.73) ;B ;44 ;.10 44 ;.04 43 ;.91 43 ;.75 34 ;.28 ;42 ;.02 ;(20 ;.02) (20 ;.00) (19 ;.94) (19 ;.86)(15 ;.56) ;(19 ;.08) ;C ;46 ;.92 47 ;.80 45 ;.35 47 ;.76 38 ;.48 ;45 ;.26 ;(21 ;.30) (21 ;.70) (20 ;.59) (21 ;.68) (17 ;.47) ;(20 ;.55) ;Table 3 shows the effect on the health of the calves in the trials for the three types of milk replacers. The numbers in each column represent a score scour for the 28 days with normal = 1; loose = 2; watery = 3; and blood or mucus =4. As indicated by the overall ;2 076 6 & ;- 15 - ;average, the replacer using soy material made in accordance with the present invention results in the calves being in a more normal health state than the other types of replacers. ;TABLE 3 Scour Score for 28 Days ;TEST ;OVERALL ;REPLACER ;1 ;2 ;3 ;4 ;5 ;AVERAGE ;A ;1.38 ;1.37 ;1.51 ;1.31 ;1 ;.27 ;1.37 ;B ;1.29 ;1.31 ;1.36 ;1.32 ;1 ;.29 ;1.31 ;C ;1.25 ;1.20 ;1.21 ;1.16 ;1 ;.21 ;1.21 ;5 Example 2 ;The procedure of Example 1 was repeated, except that live steam was injected into the reactor until the flour/alcohol mixture temperature reached 280°F (138°C). At that time, the steam injection was turned off along 10 with the agitators and the vessel vented. The temperature of the flour/alcohol mixture was allowed to fall to approximately 130°F (54°C) for drying. A flour having a generally bland taste with substantially no soybean odor, and a generally white non-grainy appearance with water 15 retentive properties was produced. ;Example 3 ;The procedure of Example 1 was followed, except that steam injection into the reactor was continued until the flour/alcohol mixture reached approximately 240°F 20 (116°C). At approximately 240°F (116°C), the steam injection was turned off along with the chopper and the ;<2 076 £ £ ;- 16 - ;product held for approximately 5 minutes with the plough-type blade agitator mixing the product for the 5 minutes. At the end of the 5 minute hold period, the reactor is vented as in example 1 and the temperature 5 allowed to fall to approximately 130°F (54°C). A flour having a generally bland taste with substantially no soybean odor, and a generally white non-grainy appearance with water retentive properties was produced. ;Examples 4-8 ;10 Trials using various ratios of alcohol with respect to soybean material were performed using the conditions and procedures of Example 1. The amounts of alcohol tried were 3 pounds (1.4 kilograms), 6 pounds (2.7 kilograms), 9 pounds (4.1 kilograms), 18 pounds (8.2 15 kilograms) and 27 pounds (12.3 kilograms) with 60 pounds (27.2 kilograms) of soybean flour. The soybean flour treated in the trials with 9, 18, and 27 pounds (4.1, 8.2 and 12.3 kilograms) of alcohol to 60 pounds (27.2 kilograms) of soybean material exhibited similar band 20 characteristics in gel electrophoresis as the material in Example 1. The soybean flour treated in the trials using 3 and 6 pounds (1.4 and 2.7 kilograms) of alcohol did not exhibit similar band characteristics in gel electrophoresis as the material tested in Example 1. From 25 Examples 4-8, it is understood that at least approximately 9 pounds (4.1 kilograms) of alcohol with 60 pounds (27.2 kilograms) of soybean material must be used to treat the ;10 ;* 207666 - 17 - soybean material satisfactorily using the process of the present invention. Although the levels of alcohol between 6 and 9 pounds (2.7 and 4.1 kilograms) were not specifically tested, it is also understood that soybean material treated with amounts of alcohol between 6 and 9 pounds (2.7 and 4.1 kilograms) per 60 pounds (27.2 kilograms) of soybean material, that exhibits band characteristics in gel electrophoresis which are similar to the material tested in Example 1, is intended to be within the scope of the present invention. CONCLUSION The present invention provides an improved process that treats soybean material by making the soybean material digestable and extracting undesirable tastes and 15 odors from the soybean material using a minimum amount of alcohol. The process directly subjects the soybean material to a minimum amount of steam, avoiding unnecessary soaking and overcooking of the soybean material. Substantially all of the alcohol, used to treat 20 the soybean material, is removed in an easy and efficient manner by subjecting the alcohol to subatmospheric pressure at an elevated temperature that will not brown the soybean material. Although the present invention has been described 25 with reference to preferred embodiments, workers skilled in the art will recognize that changes may be madj^Fgr 15 JUN1987) </div>

Claims

<div class="application article clearfix printTableText" id="claims"> 2 076 6 6 - 18 - form and detail without departing from the spirit and scope of the invention. 5 10 15 25 #307666 - 19 - . t ■ WHAT WE CLAIM IS:

1. A process for treating soybeans, comprising: mixing a lower alcohol with a proteinaceous soybean material in a ratio that is at least greater than 6 pounds (2.7 kilograms) of alcohol to 60 pounds (27.2 kilograms) of soybean material in a closed vessel; fluidizing the proteinaceous soybean material/alcohol mixture? introducing steam directly to the proteinaceous soybean material/alcohol mixture to heat the material to a treatment temperature of a maximum of 280°F (138°C); subjecting the proteinaceous soybean material to lower alcohol vapors under superatmospheric pressure; stopping the steam flow to the proteinaceous soybean material/alcohol mixture after the treatment temperature has been reached; holding the soybean material/alcohol without further introduction of steam and until the soybean material reaches a PDI of less than 10; and venting the lower alcohol vapors from the enclosed vessel to subatmospheric pressure while holding the temperature of the proteinaceous soybean material above the boiling point of the lower alcohol at the subatmospheric pressure thereby removing substantially all of the lower alcohol from the proteinaceous soybean material.

2. The process of claim 1 wherein the steam is introduced to the proteinaceous soybean material/alcohol mixture until a 207666 • * f - 20 -

3. The process of claim 2 wherein the proteinaceous soybean material is held for approximately thirty minutes at approximately 220"F (104°C).

4. The process of claim 3 wherein the proteinaceous soybean material is held for approximately thirty minutes at approximately 220°F (104°C) by introducing steam into a jacket of the closed vessel.

5. A substantially digestable soybean materail having a PDI of less than 10 characterized by its bland taste, lack of soybean odor, generally white appearance, and exhibiting water-retentive characteristics when produced in accordance with the process of claim 1.

6. The process of claim 1 wherein the lower alcohol is susbstantially all ethanol.

7. The process of claim 1 wherein the lower alcohol is a mixture by weight of 90% ethanol, 5% methanol and 5% water.

8. The process of claim 1 wherein the proteinaceous soybean material is treated with lower alcohol vapors under a pressure range of 15 psi to 26 psi.

9. The process of claim 1 wherein the closed vessel is vented to a pressure range of 25-26 inches C63-66 centimeters) Hg.

10. The process of claim 9 wherein the temperature of the proteinaceous soybean material is kept at a maximum of 130°F (54°C) after venting. 2 "JUL 1987' 'V 207666 - 21 -

11. The process of claim 1 wherein the proteinaceous soybean material is fluidized by a plurality of agitators located within the vessel.

12. A process for treating soybeans according to any preceding claim, substantially as hereinbefore described with reference to any one of the Examples 1 to 8 herein. , J. D. HA nDIE & co Pcrfent Attorneys for' the Applicant^). </div>