IE55746B1 - Whey derivatives - Google Patents

Whey derivatives

Info

Publication number
IE55746B1
IE55746B1 IE952/83A IE95283A IE55746B1 IE 55746 B1 IE55746 B1 IE 55746B1 IE 952/83 A IE952/83 A IE 952/83A IE 95283 A IE95283 A IE 95283A IE 55746 B1 IE55746 B1 IE 55746B1
Authority
IE
Ireland
Prior art keywords
whey
protein
lactose
hydrolysing
enzymes
Prior art date
Application number
IE952/83A
Original Assignee
Kerry Operative Creameries
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kerry Operative Creameries filed Critical Kerry Operative Creameries
Priority to IE952/83A priority Critical patent/IE55746B1/en
Priority to DK206484A priority patent/DK206484A/en
Priority to GB08410713A priority patent/GB2139071B/en
Priority to EP84302805A priority patent/EP0127938A1/en
Publication of IE55746B1 publication Critical patent/IE55746B1/en

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

Description

This Invention relates to preparations which are useful in the production of silage from grass or other plant aaterial « or as animal feed additives or supplements· In particular, the invention relates to S a method of preparing from whey produced as a by-product in the dairy industry, derivatives which will be suitable for use for the aforementioned purposes· The principal object of the invention is to provide a method which will make it possible to obtain from liquid whey, preparations of reduced volume and good stability, which will be suitable for the aforementioned uses.
The total solids level that can be attained in whey and other by-product streams produced in the dairy Industry is generally limited by the solubility of the lactose contained therein· The solubility of this component can be increased by hydrolysis using chemical or enzymic techniques.
The invention is based on our observation that when using certain crude preparations of lactose-hydrolysing enzymes to hydrolyse lactose in whey and other dairy streams, it was possible to produce products with superior properties. We found that with these crude enzyme preparations, it was possible to obtain solutions of low viscosity at solids levels much higher than those normally attained when using lactose-hydrolysing enzymes. Me then noted that thia enhancing effect was the result of proteolytic enzyme contamination, as a result of which we established that by including treatment with certain proteolytic enzymes in processes involving the hydrolysis of whey with lactosehydrolysing enzymes, it was possible to produce products with superior properties on a regular and reliable basis.
IO This result was surprising as, hitherto. It had been found that proteolysis of milk proteins usually results in precipitation and dis improvement In flow characteristics. Similarly, most milk proteins can only be partially solubilised, and this following denaturation and precipitation, and in these situations significant amounts of Insoluble material are normally generated.
We believe that a likely explanation of our finding, is that hydrolysis of tdiey and other milk proteins in solution by our method results in a decrease of protein viscosity, but this is controlled so that it does not cause protein and peptide precipitation.
Xn general it is our finding that hy adding protease enzymss to a whey-hydrolysis system, either simultaneously with the addition of lactose-hydrolysing enzymes, oc before oc after euch addition, it ie possible to hydrolyse the protein present in such a manner as to enable solutions vith high solid levels to be prepared, which are highly stable both microbiogically and chealcally. and which can be readily handled as compared with media containing non-hydrolysed protein. This leads to ..the solutions prepared being highly suitable for use in the treatment of grass for silage and as a component in animal feed. Hitherto, the use of whey for these purposes has given rise to difficulty,: because whey concentration was a limiting factor and concentrated whey caused handling problems.
Accordingly the invention provides a method for preparing & whey derivative for use in the production of silage from grass or other plant material, or for use as an animal feed additive, the method comprising treating liquid whey either sequentially or simultaneously with protein-hydrolysing and lactose-hydrolysing enzymes, so as to hydrolyse protein and lactose contained in the whey, the pH of the reaction medium being less than 7.0 during at least a part of the treatment vith the protein-hydrolysing enzyme or enzymes, and concentrating the medium containing the hydrolysed protein snd l. .
We have found that when both the protein and carbohydrate components are hydrolysed in this way, tbe resulting product is of relatively low viscosity and it can be readily concentrated without the---—? carbohydrate crystallizing. The concentrated product. . is then suitable for use as a silage additive, or as a component in animal feeds, as a substitute for Molasses, for example.
Xn applying the Method of the invention to whey (and also to other substances encountered in the dairy Industry) it is possible for the whole of the protein and carbohydrate content to be hydrolysed enzymatically Alternatively a significant percentage of the protein present in whey can be removed by ultrafiltration or heat treatment and the remaining soluble protein component is then hydrolysed by protease enzyme treatment. The presence of hydrolysed protein as opposed to unhydrolysed protein may be biologically significant In the use of high solids streams in certain applications, especially where they are used as promoters of microbial growth or as feeds. Xn both Instances the biological system may utilise the hydrolysed protein more efficiently than the unhydrolysed protein. Consequently in certain applications it may also be beneficial to supplement the product with crude or refined hydrolysed protein or other products. Xt may also be beneficial In respect of use or storage, that the product be acidic. This may be effected by addition of organic or mineral acids, or by generating acid conditions by omitting to add alkali during the action of the protease enzyme. Alternatively, microbial fermentation can be employed to promote in situ acid production. The presence of microbial species, especially Lactobacillus sp. may be beneficial in certain applications, such as in the use of these streams as ensilage promoters.
The invention will now be described in greater detail, by reference to the following Examples which illustrate the preparation of whey derivatives by the method of the invention.
EXAMPLE 1 A whey solution is prepared, having a solids level of 5 to 30%, either by concentrating liquid whey obtained as a dairy by-product, or by reconstituting whey powder. The solution is adjusted to pH 5.5 to 7.0 with 4N potassium hydroxide and the temperature is adjusted to 40°C. To the resulting solution there is added 0.15% by weight of a commercially available B-galactosidase of such an activity as to give hydrolysis of greater than 60% of the lactose within a five hour period. Either at the same time, or within one hour of the 6-galactosidase addition, an addition of a commercially available proteolytic enzyme is made. The preferred enzyme is that supplied by Novo under the designation Alcalase 0.6L (Alcalase is a Trade Mark).
Alcalase 0.6L is a serine endoproteinase preparaton having an activity uf 0.0 AnsOri units pei gram, the major enzyme component thereof being Subtilisin A. This preparation is added at levels up to 0.1% by weight so as to attain approximately 10% protein * 15 hydrolysis In a four to five hour period. Following the Incubation period, the resulting solution is concentrated by evaporation to 70% total solids content.
EXAMPLE 2 Zn a similar manner to Example 1, a whey solution is prepared with a solids level of 5 to 30% solids, and this is adjusted to pH 8.5 with 4K potassium hydroxide and the temperature is adjusted to 40*C. To this an addition of a comnercially available proteolytic enzyme is made. Again, the preferred enzyme is Novo Alcalase 0.6L which Is added to levels up to 0.1% by weight so as to attain approximately 10% protein hydrolysis In three to four hours. During this time the pH of the system falls to about pH 6.5 and is adjusted to pH 6.3 with concentrated hydrochloric acid or 4N sodium hydroxide as required. To this, 0.15% by weight of commercially available B-galactosidase is added, of such activity as to give hydrolysis of greater than 80% of the lactose within a five hour period. At the end of the incubation period the resulting solution is concentrated by evaporation to 70% total solids content.
The products of Examples 1 and 2 can be supplemented, or their pH or solids levels may be adjusted so as to provide the desired characteristics for particular applications.
Xt will be noted that the procedures described above in Examples 1 and 2 result in high levels of protein hydrolysis of 10% or more. Such a high level of hydrolysis has not been achieved hitherto in connection with protein hydrolysis procedures.
The derivatives prepared in accordance with Examples 1 and 2 have been found to be highly effective for use in connection with the ensilage of grass, for which purpose they may be applied by spraying at the rate of 1} to 2) gallons per ton of grass.
The major advantage of the method of the invention is the ability of the hydrolysed product to be concentrated to a high solids level while remaining mlcrobially and chemically stable. The high solids levels attained by the application of the invention overcome problems associated with whey and other dairy streams when concentrated by techniques in use hitherto, in that the volumes which are applied can be greatly reduced.
The details of the processes described above have, of course, been given by way of exanple only and may be modified ln various ways, within the scope of the invention.

Claims (9)

1. A method for preparing a whey derivative for use in the production of silage from grass or other plant material, or for use as an animal feed additive, the method comprising treating liquid whey either sequentially or simultaneously with protein-hydrolysing and lactose-hydrolysing enzymes, so as to hydrolyse protein and lactose contained in the whey, the pB of the reaction medium being less than 7.0 during at least a part of the 10 treatment with the protein-hydrolysing enzyme or enzymes, and concentrating the medium containing the hydrolysed protein and lactose,
2. A method according to claim l in which the protein-hydrolysing enzyme is a serine endoproteinase L r > preparation, the treatment being effected with up to.0.1% by weight of this preparation for from J to 5 hours whereby hydrolysis of at least io% of the protein present in the liquid whey is effected. .
3. A method according to claim l or claim 2 in which the 20 whey is subjected to ultrafiltration to remove a part of the protein prior to treatment with the enzymes.
4. A method according to any of the preceding claims in which the concentration is effected by evaporation.
5. A method according to any of the preceding claims in 25 which the lactose-hydrolysing enzyme is p-galactosidase. 4. A method according to any of the preceding claims further comprising adding an organic acid or a mineral acid after the concentration step. ζ
6. 7. A method according to any of the preceding claims further comprising adding a microbial culture after the concentration step.
7. 8. A method for preparing a whey derivative for use 5 in the production
8. 9. A whey derivative prepared by a process according
9. 10 to any of the preceding claims.
IE952/83A 1983-04-26 1983-04-26 Whey derivatives IE55746B1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
IE952/83A IE55746B1 (en) 1983-04-26 1983-04-26 Whey derivatives
DK206484A DK206484A (en) 1983-04-26 1984-04-25 PROCEDURE FOR THE PREPARATION OF FORESTRY DERIVATIVES
GB08410713A GB2139071B (en) 1983-04-26 1984-04-26 Whey derivatives
EP84302805A EP0127938A1 (en) 1983-04-26 1984-04-26 Whey derivatives

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IE952/83A IE55746B1 (en) 1983-04-26 1983-04-26 Whey derivatives
IE95284 1984-04-19

Publications (1)

Publication Number Publication Date
IE55746B1 true IE55746B1 (en) 1991-01-02

Family

ID=26319008

Family Applications (1)

Application Number Title Priority Date Filing Date
IE952/83A IE55746B1 (en) 1983-04-26 1983-04-26 Whey derivatives

Country Status (1)

Country Link
IE (1) IE55746B1 (en)

Similar Documents

Publication Publication Date Title
JP2509436B2 (en) Non-phosphorylated peptide
US4770706A (en) Aqueous ink and process for its manufacture
US4473589A (en) Protein liquefication process and products
SU1463120A3 (en) Method of making silage from vegetable raw material
CN102960570B (en) Processing anti-corrosion method of aquatic feed
CN110029140A (en) A kind of preparation method of wheat active peptide and the wheat active peptide of preparation
US4259357A (en) Stabilized milkproteins-containing compositions
NL8102744A (en) PROCESS FOR HYDROLYZING LACTOSE.
JP2005534340A (en) Method for recovering peptides / amino acids and oils / fat from raw materials containing one or more proteins, products produced by the method, and use of the products
US20100255147A1 (en) Non-Settling Galacto-Oligosaccharide-Rich Liquid Concentrate and Related Methods and Nutritional Compositions
US4684527A (en) Process for producing seasoning
EP0127938A1 (en) Whey derivatives
EP1562442B1 (en) Process for preparing microbial stable protein suspensions
KR880002177B1 (en) Process for beverage of acid milk
IE55746B1 (en) Whey derivatives
WO2012127005A1 (en) Chymosin formulation
NZ208265A (en) Preparing whey derivatives by enzymatic treatment of liquid whey
US20030022274A1 (en) Partially hydrolysed protein nutrient supplement
JPS6314681A (en) Production of enzymic hydrolyzate of egg white
CN113647591A (en) Royal jelly zymolyte and preparation method and application thereof
NO135255B (en)
Mehaia et al. Hydrolysis of whey permeate lactose in a continuous stirred tank membrane reactor
JPH025829A (en) Method for removing bitterness from protein hydrolysate and obtained product
Sizer Enzymes and their applications
SU659620A1 (en) Nutrient medium for growing l-lysine producer microorganisms

Legal Events

Date Code Title Description
MK9A Patent expired